Reciprocating plunger assembly of heat-conducting reciprocating pump built in front section of plunger assembly

文档序号:1335169 发布日期:2020-07-17 浏览:4次 中文

阅读说明:本技术 柱塞组件前段内置导热往复泵的往复柱塞组件 (Reciprocating plunger assembly of heat-conducting reciprocating pump built in front section of plunger assembly ) 是由 何巨堂 何艺帆 于 2020-03-27 设计创作,主要内容包括:柱塞组件前段内置导热往复泵的往复柱塞组件,柱塞组件前段的柱塞与柱塞函之间有内置液腔FQ,往复运动通过FQ的柱塞段含有驱动导热液往复流动的辅泵腔塞QS,FQ腔壁也是导热液DL与柱塞函、柱塞之间的动态换热面,形成导热往复泵即辅泵;柱塞进程靠近主液缸时,辅泵前腔V6的DL自V6接口N6排出流向传热部件HX换热,HX内DL经辅泵内腔接口N1正向流返回辅泵内腔V1进行导热;柱塞返程远离主液缸时,V1的DL自N1排出流向HX,同时HX内DL经N6逆向流返回V6;可提高柱塞密封件与主液缸之间的操作温差而优化柱塞密封件温度,提高主液缸的操作温度范围和体积效率,降低冲洗油耗量,扩大柱塞往复泵应用范围。(A reciprocating plunger assembly of a heat-conducting reciprocating pump is arranged in the front section of a plunger assembly, a built-in liquid cavity FQ is arranged between a plunger and a plunger box of the front section of the plunger assembly, reciprocating motion of the plunger through the FQ comprises an auxiliary pump cavity plug QS for driving heat-conducting liquid to flow in a reciprocating mode, the wall of the FQ cavity is also a dynamic heat exchange surface between the heat-conducting liquid D L and the plunger box and the plunger to form the heat-conducting reciprocating pump, namely an auxiliary pump, when a plunger process is close to a main liquid cylinder, D L of an auxiliary pump front cavity V6 is discharged from a V6 interface N6 to flow to a heat-conducting component HX for heat exchange, D L in the HX positively flows back to an auxiliary pump inner cavity V1 through an auxiliary pump inner cavity interface N1 for heat conduction, when the plunger process is far away from the main liquid cylinder, D L of V1 is discharged from N1 to HX, D L in the HX reversely flows back to V6 through N6, the operating temperature difference between the plunger seal and the main liquid cylinder can be improved, the plunger seal temperature is optimized, the operating temperature.)

1. The reciprocal plunger subassembly of the built-in heat conduction reciprocating pump of plunger subassembly anterior segment, its characterized in that:

a reciprocating plunger assembly U100, at least comprising a plunger U110, a plunger housing U130, and a plunger seal U120 installed in the plunger housing;

the plunger U110 is placed in the inner cavity of the plunger U130 and used for reciprocating motion;

the end face of the plunger letter U130, which is in contact with the main hydraulic cylinder, is the front end face of the plunger letter U130, and the end face of the plunger letter U130, which is far away from the main hydraulic cylinder, is the rear end face of the plunger letter U130;

the reciprocating plunger assembly U100 at least uses 2 plunger seals, the plunger seal closest to the rear end face of the plunger box U130 is an outer plunger seal U129, the other plunger seals belong to plunger main seals, and the plunger main seal closest to the outer plunger seal U129 is also called as the outer plunger main seal;

when 2 or more plunger main seals are used in the reciprocating plunger assembly U100, the numbers are sequentially numbered from near to far according to the distance from the front end face of the plunger letter U130, the plunger main seal closest to the front end face of the plunger letter U130 is a1 st plunger main seal U121, and the other plunger main seals are a 2 nd plunger main seal U122, a 3 rd plunger main seal U123 and the like;

the part of the plunger letter U130 between the front end face of the plunger letter U130 and the 1 st plunger main seal U121 is called as the front section of the plunger letter U130;

the part of the plunger letter U130 between the rear end face of the plunger letter U130 and the main seal of the plunger at the outer side is called the rear section of the plunger letter U130;

when the reciprocating plunger assembly U100 uses 2 or more plunger main seals, the plunger letter U130 part between the 1 st plunger main seal U121 and the plunger main seal at the outer side is called the middle section of the plunger letter U130;

a plunger pocket U130 containing at least the plunger packing pocket fitted with or contacting the plunger seal U120 and possibly a plunger barrel not fitted with the plunger seal U120, the plunger barrel adjacent to the main cylinder being referred to as a plunger front barrel;

the reciprocating plunger assembly U100 is characterized by also comprising a built-in auxiliary heat exchange reciprocating PUMP 7PUMP (auxiliary PUMP);

the auxiliary pump is composed and works according to the following principle:

① plunger function U130 front section and reciprocating between the plunger U110 front section, constituting built-in auxiliary pump fluid chamber FQ, plunger U110 front section reciprocating through FQ position set up auxiliary pump fluid chamber plug QS which pushes auxiliary pump fluid chamber FQ fluid movement;

when the plunger U110 reciprocates, the auxiliary pump cavity plug QS is driven to reciprocate to push heat-conducting liquid in the auxiliary pump liquid cavity FQ to reciprocate, and the auxiliary pump cavity plug QS plays a role of a reciprocating pump plunger;

an auxiliary pump liquid cavity FQ is divided into an auxiliary pump inner cavity and an auxiliary pump front cavity by taking an auxiliary pump cavity plug QS as a boundary;

the part of an auxiliary pump liquid cavity FQ far away from the front end surface of the plunger piston U130 by taking an auxiliary pump cavity plug QS as a boundary is an auxiliary pump inner cavity,

the part of an auxiliary pump liquid cavity FQ close to the front end surface of the plunger U130 is an auxiliary pump front cavity by taking an auxiliary pump cavity plug QS as a boundary,

in the reciprocating process of the plunger U110, the liquid suction and discharge space of the inner cavity of the auxiliary pump is called as an inner dynamic cavity of the auxiliary pump, and the volume of the inner dynamic cavity of the auxiliary pump is a dynamic variable quantity;

in the reciprocating process of the plunger U110, the liquid suction and discharge space of the front cavity of the auxiliary pump is called as a front moving cavity of the auxiliary pump, and the volume of the front moving cavity of the auxiliary pump is a dynamic variable quantity;

the auxiliary pump inner cavity is communicated with the auxiliary pump front cavity through a channel and a heat transfer element HX, and the auxiliary pump inner cavity is communicated with the auxiliary pump front cavity through a communicating vessel;

②, the heat transfer element HX is used for receiving the heat-conducting liquid discharged from the auxiliary pump liquid cavity FQ, transferring heat to the heat-conducting liquid to change the temperature of the heat-conducting liquid, returning the heat-conducting liquid after the temperature change of the heat transfer to the auxiliary pump liquid cavity FQ, and heating the wall surface of the auxiliary pump liquid cavity FQ;

③ the heat-conducting liquid in the auxiliary pump fluid cavity FQ reciprocates along with the reciprocating motion of the auxiliary pump cavity plug QS, contacts with the wall of the auxiliary pump fluid cavity FQ to perform reciprocating flow contact heat conduction on the inner surface of the front section of the plunger U130 and the outer surface of the front section of the plunger, the wall of the auxiliary pump fluid cavity FQ is also a heat-conducting surface, and the auxiliary pump fluid cavity FQ is also called as an auxiliary pump heat-conducting cavity;

when the main plunger U110 moves forwards, the main plunger U110 moves forwards close to the main hydraulic cylinder, heat-conducting liquid is discharged from the front movable cavity of the auxiliary pump through the interface N6X and enters the heat transfer element HX, and the heat-conducting liquid with changed temperature discharged from the heat transfer element HX is used as forward cold flow to return to the inner movable cavity of the auxiliary pump through the interface N1X;

when the main plunger U110 makes a return movement, the main plunger U110 makes a return movement away from the main hydraulic cylinder, the heat-conducting liquid is discharged from the internal movable cavity of the auxiliary pump through the interface N1X and enters the heat transfer element HX, and the heat-conducting liquid with the temperature changed and discharged from the heat transfer element HX is returned to the front movable cavity of the auxiliary pump as a reverse cold flow through the interface N6X.

2. The reciprocating plunger assembly of claim 1, wherein:

and (b) a form of auxiliary pump cavity plug QS selected from 1 or a combination of several of the following:

① the outer side surface is a smooth cylinder;

②, a cylinder with 1 or 2 or more inner grooves is arranged outside;

③ cylindrical body with internal screw thread on its outer side;

④ is provided with a cylinder communicating the minute passages of the sub pump rear chamber and the sub pump front chamber.

3. The reciprocating plunger assembly of claim 1, wherein:

the inner cavity form of the front section of the plunger letter U110 is selected from 1 or a combination of several of the following components:

① equal diameter channels with the same inner diameter;

② the inner diameter of the side close to the main cylinder is smaller than that of the side far from the main cylinder;

③ is larger than the main cylinder on the side away from the main cylinder.

4. The reciprocating plunger assembly of claim 1, wherein:

the heat transfer element HX is in a form selected from 1 or a combination of several of the following forms:

① independent of the heat transfer element of the plunger barrel;

② converge on the heat transfer element of the plunger barrel.

5. The reciprocating plunger assembly of claim 1, wherein:

the heat transfer element HX is in a form selected from 1 or a combination of several of the following forms:

① the heat pipe is a smooth pipe, the guide vane liquid flows in the heat exchange pipe;

② the heat exchange tube is a screw tube, the guide vane liquid flows in the heat exchange tube, the inner side and/or outer side of the heat exchange tube is provided with screw thread;

③ the heat exchange tube is the finned tube, and guide vane liquid flows in the heat exchange tube, and the finned tube is arranged to the heat exchange tube inboard and/or the outside.

6. The reciprocating plunger assembly of claim 1, wherein:

the heat transfer element HX is a heat transfer element independent from the plunger sleeve, and the relation between the central elevation of the heat transfer element HX and the central elevation of the plunger sleeve U130 is selected from 1 of the following types:

① are equal in height;

②, the central elevation of the heat transfer element HX is lower than the central elevation of the plunger letter U130;

③ the height of the center of the heat transfer element HX is higher than the height of the center of the plunger letter U130.

7. The reciprocating plunger assembly of claim 1, wherein:

the heat transfer element HX uses a heat transfer medium which is in heat transfer with the heat transfer liquid and is selected from 1 of the following types:

① gas, possibly air;

② liquid, which may be water or oil;

③ gas-liquid mixture.

8. The reciprocating plunger assembly of claim 1, wherein:

the volume infusion amount of the built-in auxiliary heat exchange reciprocating PUMP 7PUMP-RW is in a ratio K700 to the volume infusion amount of the main hydraulic cylinder U100-RW driven by the reciprocating plunger assembly U100, wherein K700 is (7PUMP-RW)/(U100-RW), and K700 is selected from 1 of the following types:

① is less than 0.1;

②0.1~0.3;

③0.3~1.0;

④ is greater than 1.0.

9. The reciprocating plunger assembly of claim 1, wherein:

the cavity wall area of the front moving cavity of the auxiliary pump is K300 times of the cavity wall area of the inner moving cavity of the auxiliary pump, and K300 is selected from 1 of the following types:

①0.5~1.0;

②1.0~3.0;

③ is greater than 3.0.

10. The reciprocating plunger assembly of claim 1, wherein:

reciprocating plunger subassembly U100 sets up 2 plunger seals, and its effect is:

① outside plunger seal, preventing the liquid in the space between 2 plunger seals from leaking to the outside environment;

② plunger primary seal, preventing leakage of primary cylinder media into the space between the 2 plunger seals.

11. The reciprocating plunger assembly of claim 1, wherein:

reciprocating plunger subassembly U100 sets up 3 plunger seals, and its effect is:

① outside plunger seal, preventing the liquid in the space between the outside plunger seal and the outside plunger main seal from leaking to the outside environment;

② the 2 nd or outer plunger primary seal prevents liquid in the space between the 2 nd and 1 st plunger primary seals from leaking into the space between the outer and 2 nd plunger primary seals;

③ plunger primary seal 1, prevents leakage of primary cylinder media into the space between plunger primary seal 1 and plunger primary seal 2.

12. The reciprocating plunger assembly of claim 1, wherein:

reciprocating plunger subassembly U100 sets up 4 plunger seals, and its effect is:

① outside plunger seal, preventing the liquid in the space between the outside plunger seal and the outside plunger main seal from leaking to the outside environment;

② the 3 rd plunger main seal, i.e. the outer plunger main seal, prevents the liquid in the space between the 3 rd plunger main seal and the 2 nd plunger main seal from leaking into the space between the outer plunger main seal and the 3 rd plunger main seal;

③ plunger primary seal 2, preventing liquid in the space between the plunger primary seal 2 and the plunger primary seal 1 from leaking into the space between the plunger primary seal 2 and the plunger primary seal 3;

④ plunger primary seal 1, prevents leakage of primary cylinder media into the space between plunger primary seal 1 and plunger primary seal 2.

13. The reciprocating plunger assembly of claim 1, wherein:

the reciprocating plunger assembly U100 is provided with at least 2 plunger seals;

and the sealing liquid is continuously or discontinuously replaced in the gap between the outer plunger seal and the outer plunger main seal, so that the liquid material passing through the outer plunger main seal is prevented from polluting the outer plunger seal.

14. The reciprocating plunger assembly of claim 1, wherein:

the reciprocating plunger assembly U100 is provided with at least 2 plunger seals;

at plunger letter U130 anterior segment, use and keep apart the flush fluid, continuous or be interrupted the injection plunger letter U130 anterior segment, the isolation flush fluid of injection finally enters into main hydraulic cylinder, prevents that the liquid material that comes from main hydraulic cylinder from polluting plunger letter U130 anterior segment and then polluting the 1 st plunger main seal.

15. The reciprocating plunger assembly of claim 1, wherein:

the reciprocating plunger assembly U100 is provided with at least 3 plunger seals, namely at least 2 plunger main seals;

in the gap JX-23 between any 2 plunger main seals, continuous or intermittent replacement of flushing liquid is used to prevent liquid material from the space near the main cylinder side from penetrating the plunger main seal into the gap JX-23 to cause pollution.

16. The reciprocating plunger assembly of claim 1, wherein:

the reciprocating plunger assembly U100 is provided with at least 2 plunger seals;

an isolation flushing liquid is continuously or discontinuously injected into the front section of the plunger letter U130 at the front section of the plunger letter U130, and the injected isolation flushing liquid finally enters the main hydraulic cylinder to prevent liquid materials from the main hydraulic cylinder from polluting the front section of the plunger letter U130 and further polluting the 1 st plunger main seal;

the working mode of the isolation flushing liquid is selected from 1 of the following modes:

①, the plunger U110 moves to the whole distance to separate and flush based on the reciprocating motion of the plunger U110;

② the return process of the plunger U110 is isolated and washed by taking the reciprocating motion of the plunger U110 as the reference;

the isolation flushing liquid adopts a working mode of plunger return synchronous injection, when the plunger U110 is in a return stroke, the main hydraulic cylinder sucks liquid materials, and the plunger of the injection pump for isolating the flushing liquid acts to flush the isolation liquid cavity at the front section of the plunger of the reciprocating plunger assembly U100; when the plunger U110 is in a forward stroke, the main cylinder discharges liquid materials, the plunger of the injection pump for isolating flushing liquid acts to suck the isolating liquid, and the front section of the plunger U130 of the reciprocating plunger assembly U100 is not flushed.

17. The reciprocating plunger assembly of claim 1, wherein:

a plunger shaft U130 in a form selected from 1 of:

① are one-piece components;

② is the assembly of the anterior segment of plunger case and the posterior segment of plunger case of 2 separate parts, the anterior segment of plunger case is a part, the posterior segment U131 of plunger case is another part;

③ is an assembly of multiple separate parts;

when the plunger assembly U130 comprises 2 or more plunger assembly sections, the complete plunger assembly U130 is formed after assembly.

18. The reciprocating plunger assembly of claim 1, wherein:

the plunger letter U130 is an assembly of front sections and rear sections of 2 split parts, wherein the front section is one part, and the rear section is the other part;

a reciprocating plunger assembly U100 provided with at least 2 plunger U110 seals;

at least 1 plunger U110 seal is arranged at the rear section of the plunger box, and at most all the plunger U110 seals are arranged.

19. The reciprocating plunger assembly of claim 1, wherein:

the plunger letter U130 is an assembly of front sections and rear sections of 2 split parts, wherein the front section is one part, and the rear section is the other part;

a reciprocating plunger assembly U100 provided with at least 2 plunger U110 seals;

at least 1 plunger U110 seal is arranged at the front section of the plunger box.

20. The reciprocating plunger assembly of claim 1, wherein:

the reciprocating plunger assembly U100 is provided with an auxiliary pump follow-up cavity, an auxiliary pump main cavity plug ZQS and an auxiliary pump auxiliary cavity plug FQS;

the auxiliary pump follow-up cavity is communicated with the inner cavity of the auxiliary pump through a passage AN1 and a heat transfer element HX which can be used, and the auxiliary pump follow-up cavity is communicated with the front cavity of the auxiliary pump through a passage AN2 and a heat transfer element AHX which can be used;

the auxiliary pump is provided with at least one heat transfer component which is a heat transfer component HX and/or a heat transfer component AHX;

the auxiliary pump follow-up cavity, the auxiliary pump inner cavity and the auxiliary pump front cavity are in a communicating vessel relationship.

21. The reciprocating plunger assembly of claim 1, wherein:

the relationship between reciprocating plunger assembly U100, auxiliary pump chamber plug QS and plunger box, 1 of the following is selected:

① the auxiliary pump cavity plug QS is not in contact with the plunger cage, and a gap exists;

② contact between the auxiliary pump cavity plug QS and the plunger box, the contact part is the auxiliary pump cavity separating filler which is installed on the plunger U110;

③ the auxiliary pump chamber plug QS is in contact with the plunger housing at the contact portion where the auxiliary pump chamber partition packing is mounted on the plunger housing U130.

22. The reciprocating plunger assembly of claim 1, wherein:

the absolute value of the difference between the operating temperature T2 of the reciprocating ram assembly U100, the ram primary seal closest to the primary cylinder, i.e., the 1 st ram primary seal, and the primary cylinder operating temperature T1 is selected from 1 of the following:

①30~60℃;

②60~90℃;

③90~150℃;

④150~200℃;

⑤ is greater than 200 ℃.

23. The reciprocating plunger assembly of claim 1, wherein:

the reciprocating plunger assembly U100 is provided with a heat exchange jacket on the cylinder body of the plunger assembly U130, and the medium flowing in the heat exchange jacket and the working mode are selected from 1 or the combination of several of the following types:

① the heat-extracting medium with cooling effect is gas phase and/or liquid phase;

② the heating medium for heating is gas phase and/or liquid phase;

③ the heat-extracting medium with cooling and temperature control functions is in gas phase and/or liquid phase;

④ are used for heating medium with temperature control function, and are in gas phase and/or liquid phase.

24. A plunger-type reciprocating pump using the reciprocating plunger assembly of claim 1, characterized in that:

the main hydraulic cylinder K10 used with the reciprocating plunger assembly U100 is a pump cylinder K10 of a plunger type reciprocating pump APUMP.

25. The plunger-type reciprocating pump of claim 24, wherein:

plunger reciprocating pump APUMP systems use 1 or 2 or more single pump chamber type pump cylinders.

26. The plunger-type reciprocating pump of claim 24, wherein:

plunger type reciprocating pump APUMP system, the integral pump cylinder body used has 1 or 2 or more pump chambers.

27. The plunger-type reciprocating pump of claim 24, wherein:

the pumping target liquid of the plunger type reciprocating pump APUMP is selected from 1 or more of the following materials:

① high temperature liquid material;

② low temperature liquid material;

③ high-pressure liquid material;

④ high temperature and high pressure liquid material;

⑤ high temperature and high pressure solid-liquid containing material;

⑥ liquid material containing easily coagulating component;

⑦ liquid material containing volatile component;

⑧ contains a solid slurry;

⑨ liquid material containing corrosive components;

⑩ liquid material containing explosive component;

liquid material containing toxic components;

a liquid material containing radioactive components.

28. The plunger-type reciprocating pump of claim 24, wherein:

the working mode of the filling liquid added into a stuffing box or a plunger sleeve of the plunger type reciprocating pump APUMP is selected from 1 or more of the following modes:

① can be used for long term after being injected once;

② intermittent injection and discharge are performed, and the injected liquid finally enters the pump cavity of the pump body and is discharged out of the pump cavity along with the pumped target liquid;

③ the injection is continuously discharged, and the discharged injection liquid finally enters the pump cavity of the pump body and is discharged out of the pump cavity along with the pumping target liquid.

29. The plunger-type reciprocating pump of claim 24, wherein:

the operating conditions of the plunger type reciprocating pump APUMP are as follows: the temperature is 150-400 ℃, the inlet pressure is 0.3-1.0 MPa, the outlet pressure is 2.0-30.0 MPa, the weight concentration of solid particles is 0-55%, and the volume flow rate of liquid material at the inlet of the pump cavity is 0.1-150 m3/h。

30. The plunger-type reciprocating pump of claim 24, wherein:

the plunger type reciprocating pump APUMP is an oil coal slurry booster pump in the coal hydrogenation direct liquefaction reaction process or the kerosene co-refining hydrogenation reaction process, and the operation conditions are as follows: the temperature is 150-350 ℃, the inlet pressure is 0.3-1.0 MPa, the outlet pressure is 2.0-30.0 MPa, the weight concentration of solid particles is 25-60%, and the volume flow rate of liquid material at the inlet of the pump cavity is 0.1-200 m3/h。

31. The plunger-type reciprocating pump of claim 24, wherein:

the plunger type reciprocating pump APUMP is an oil coal slurry booster pump in the coal hydrogenation direct liquefaction reaction process or the kerosene co-refining hydrogenation reaction process, and the operation conditions are as follows: the temperature is 150-350 ℃, the inlet pressure is 0.3-1.0 MPa, the outlet pressure is 5.0-30.0 MPa, the weight concentration of solid particles is 40-55%, and the volume flow rate of liquid material at the inlet of the pump cavity is 10-150 m3/h。

32. The plunger-type reciprocating pump of claim 24, wherein:

the plunger type reciprocating pump APUMP is an oil coal slurry booster pump in the coal hydrogenation direct liquefaction reaction process or the kerosene co-refining hydrogenation reaction process, and the quantity of working fluids of a plunger, a packing box and a plunger outer sleeve is as follows: the hourly volume flow of the injected liquid is 0.5-5% of the volume flow of the pumping target liquid of the plunger type reciprocating pump APUMP.

33. The plunger-type reciprocating pump of claim 24, wherein:

the plunger type reciprocating pump APUMP is arranged in the following way: the axis of the plunger (111) is arranged horizontally, the pump cylinder K10 is arranged vertically, the used divider XKP is arranged vertically, and the used liquid guide tube (33) is arranged vertically.

34. The plunger-type reciprocating pump of claim 24, wherein:

at the driving end of the plunger type reciprocating pump APUMP system, a prime motor is selected from 1 of the following types:

① a motor;

② variable frequency motor;

③ diesel engines;

④ a hydraulic motor;

⑤ steamer.

35. The plunger-type reciprocating pump of claim 24, wherein:

the driving end of the plunger type reciprocating pump APUMP system drives the hydraulic end to work after a transmission is used for converting high-rotation-speed motion of a prime motor into low-rotation-speed motion.

36. The plunger-type reciprocating pump of claim 24, wherein:

the plunger type reciprocating pump APUMP system comprises 1 or 2 or more pump cylinders, 1 or 2 or more plunger assemblies are matched for use, and 2 or more plunger assemblies use a heat transfer device HX for each plunger assembly and use the same heat transfer medium.

37. The plunger-type reciprocating pump of claim 36, wherein:

the plunger type reciprocating pump APUMP and the system thereof form an integrated skid-mounted structure by part or all of components.

Technical Field

The invention relates to a reciprocating plunger assembly of a heat-conducting reciprocating pump arranged in the front section of a plunger assembly, wherein a built-in liquid cavity FQ is arranged between a plunger and a plunger box of the front section of the plunger assembly, the reciprocating motion of the plunger through the FQ comprises an auxiliary pump cavity plug QS for driving heat-conducting liquid to flow in a reciprocating manner, the wall of the FQ cavity is also a dynamic heat exchange surface between the heat-conducting liquid D L and the plunger box and the plunger to form a heat-conducting reciprocating pump, namely an auxiliary pump, when a plunger process is close to a main liquid cylinder, D L of an auxiliary pump front cavity V6 is discharged from a V6 interface N6 to flow to a heat-conducting component HX for heat exchange, HX inner D L positively flows back to an auxiliary pump inner cavity V1 for heat conduction through an auxiliary pump inner cavity interface N1, and when the plunger return stroke is far away from the main liquid cylinder, D L of V1 is discharged from N1 to flow to HX, and simultaneously D L in the HX returns to V6 through N6, so that the operating temperature difference between the plunger seal and the main liquid cylinder is improved, the temperature of the.

Background

The reciprocating plunger assembly U100 of the present invention refers to an assembly comprising a plunger, a plunger housing, a plunger seal mounted within the plunger housing, and other components that may be used. The plunger case can also be called a stuffing case and a stuffing sealing case, and the part of the multi-section plunger case which is not contacted with the plunger sealing stuffing can also be called a plunger sleeve. The plunger sealing element fixed in the plunger case contacts the surface of the plunger to provide support for the plunger during axial movement of the plunger, a sealing isolation is formed between a high-pressure chamber and a low-pressure chamber in the plunger case to prevent liquid leakage, meanwhile, sliding friction between the sealing material and the contact surface of the plunger belongs to sliding friction with lubricating oil, and the lubricating oil lubricates and cools the sliding friction contact surface.

According to the reciprocating plunger assembly U100 disclosed by the invention, in a normal working state, the plunger U110 reciprocates in the plunger box U130 provided with the plunger sealing piece U120, namely the plunger U110 reciprocates relative to a contact surface of the plunger sealing piece U120, and the plunger sealing piece U120 has the function of supporting the plunger U110 and is used for preventing or reducing the main medium in the main cylinder from leaking to the middle section and the rear section of the plunger box through the No. 1 plunger main seal so as to reduce the pollution degree of the liquid (or lubricating oil or flushing liquid) in the plunger box by the main medium.

The reciprocating plunger assembly U100 of the present invention utilizes a plunger seal, typically in the form of a packing seal.

When the reciprocating plunger assembly U100 is used for liquid conveying equipment such as a liquid plunger reciprocating pump, a hydraulic cylinder which is matched with the assembly U100 and used for conveying target process fluid is called as a main hydraulic cylinder, so that the reciprocating plunger assembly U100 is distinguished from an auxiliary pump liquid cavity FQ which is internally provided with a heat-conducting reciprocating pump and uses heat-conducting liquid and is provided with the plunger assembly U100; meanwhile, the process fluid conveyed by the main liquid cylinder is taken as a main medium, and is distinguished from other materials such as heat-conducting liquid, flushing liquid, sealing liquid and the like used by the plunger assembly U100.

According to the reciprocating plunger assembly U100, the end face of the plunger letter U130, which is in contact with a main cylinder, is the front end face of the plunger letter U130, and the end face of the plunger letter U130, which is far away from the main cylinder, is the rear end face of the plunger letter U130;

the reciprocating plunger assembly U100 of the present invention may use 1 or 2 or more plunger seals, but typically uses at least 2 plunger seals to ensure the safety of the outside plunger seal (no leakage of primary media to the environment).

The reciprocating plunger assembly U100 of the invention generally uses at least 2 plunger seals, the plunger seal 1 furthest away from the main hydraulic cylinder is called an outer plunger seal, and the rest plunger seals are called plunger main seals; the plunger main seals are numbered sequentially from near to far according to the distance from the main hydraulic cylinder, the 1 plunger main seal closest to the main hydraulic cylinder is called a1 st plunger main seal, and other plunger main seals sequentially become a 2 nd plunger main seal, a 3 rd plunger main seal and the like; the plunger primary seal closest to the outboard plunger seal is also referred to as the outboard plunger primary seal.

According to the reciprocating plunger assembly U100, when 2 plunger seals are used, the 1 st plunger main seal is also the outer plunger main seal at the same time; according to the reciprocating plunger assembly U100, when 3 plunger seals are used, the 2 nd plunger main seal is also the outer plunger main seal; when 4 plunger seals are used, the 3 rd plunger main seal is also the outer plunger main seal at the same time in the reciprocating plunger assembly U100 of the invention.

The reciprocating plunger assembly U100 of the present invention generally uses packing seals, at least 2 plunger packing seals, the 1 plunger packing seal closest to the main cylinder is called the 1 st plunger main packing seal, and the 1 plunger packing seal farthest from the main cylinder is called the outside plunger packing seal.

The reciprocating plunger assembly U100 of the invention generally uses packing for sealing, and when at least 3 plunger packings are used, the plunger packing packings between the 1 st plunger main packing and the outer plunger packing are sequentially sorted from the 1 st plunger main packing to the outer plunger packing as the 2 nd plunger main packing and the like.

The front section of the reciprocating plunger assembly U100 of the invention specifically refers to a plunger box part and a plunger part between a1 st plunger main seal and a main cylinder.

The rear section of the reciprocating plunger assembly U100 specifically refers to a plunger box part and a plunger part which are bound by an outer plunger main seal and reach the rear end face of the plunger box U130, namely the plunger box part and the plunger part which are bound by the outer plunger main seal and are far away from a main hydraulic cylinder.

When the reciprocating plunger assembly U100 of the present invention uses at least 3 plunger seals, the plunger portion of the 1 st plunger primary seal that is the plunger housing portion, the plunger portion, that is the outboard plunger primary seal is referred to as the mid-section of the reciprocating plunger assembly U100.

The operational life of the plunger seal U120 of the reciprocating plunger assembly U100 is affected by the operating temperature, operating pressure, and the nature of the lubrication medium, where operating temperature is an important parameter.

The invention is suitable for a high-temperature plunger reciprocating pump or a low-temperature plunger reciprocating pump, and mainly aims to improve the temperature difference between the operating temperature of a plunger seal and the operating temperature of a main hydraulic cylinder, so as to optimize the operating temperature of the plunger seal (generally aiming at being as close to the ambient temperature as possible), so as to reduce the abrasion speed of the plunger seal, improve the lubricating performance, prolong the service life of the seal and improve the sealing performance, and further allow the operating temperature range of the main hydraulic cylinder to be widened.

The invention is mainly described by combining a high-pressure plunger reciprocating pump for conveying a main medium with high temperature and high solid particle concentration, one example is the high-pressure reciprocating pump for conveying high-temperature coal slurry for a coal hydrogenation direct liquefaction device, the temperature of the main medium is as high as 290-350 ℃, the content of solid coal powder is as high as 48.5-55 wt%, and the outlet pressure can be as high as 15-30 MPa.

For the sliding friction process of the contact surface between the plunger packing U120 and the plunger U110 in the presence of lubricating fluid, generally, the lubricating performance of the lubricating oil and the anti-abrasion performance of the sealing element are reduced when the operating temperature is too high or too low, and the deformation quantity generated on the plunger, the plunger box, the metal part of the plunger sealing element and the sealing material is larger when the operating temperature deviates from the ambient temperature, so the plunger sealing element abrasion speed is higher when the temperature is higher; the larger the deviation of the operating temperature of the friction part of the plunger sealing element and the plunger from the ambient temperature, the shorter the service life of the plunger sealing element, on the contrary, if the operating temperature of the friction part of the plunger sealing element and the plunger can be effectively controlled to be close to the ambient temperature as much as possible, the service life of the plunger sealing element can be effectively prolonged, the leakage rate of the plunger sealing element can be reduced, the pollution of a main medium to the rear section of the plunger assembly U100 is reduced, and the operating safety of the plunger assembly U100 is improved.

For a long time, the delivery of high-temperature liquid materials by a plunger reciprocating pump is a difficult problem in the plunger reciprocating pump industry, which limits the selection or optimization of a plurality of process flows, and the most important reason is that a method for reducing the temperature of a sealing contact surface, which has the advantages of simple system, simple structure, good heat exchange effect, low energy consumption, small occupied space volume and small influence on the volume efficiency of a main liquid cylinder, cannot be found, but the invention aims to provide a structural scheme or a design method capable of basically meeting the comprehensive requirements, namely a novel mechanical structure of the front section of a plunger assembly U100 to effectively and controllably realize the heat conduction and the temperature reduction of the front section of the plunger assembly U100 and provide a corresponding working system.

In the prior art, the common material of the front section of the plunger assembly U100 is a metal or alloy material with good thermal conductivity, therefore, the heat transferred by the main cylinder fluid or the main cylinder wall can be quickly transferred to the rear section of the plunger function and the rear section of the plunger, so that the operating temperature of the 1 st plunger primary seal is less different from the bulk temperature of the primary cylinder process fluid, while the higher the operating temperature of the 1 st plunger primary seal, the greater the leakage probability and wear rate of the 1 st plunger primary seal, in order to effectively lower the operating temperature of the 1 st plunger main seal, the temperature difference DT between the operating temperature of the 1 st plunger main seal and the operating temperature of the main cylinder main medium must be effectively increased, that is, a heat conducting mechanism with a simple structure must be arranged at the front section of the plunger assembly U100, the plunger assembly U100 is effectively thermally conductive (heat extraction) to the plunger housing front end, and then transfers this heat release out of the plunger assembly U100.

In the existing technical scheme, the following 2 ways of generating the temperature difference DT are available:

① indirect heat conduction mode, wherein a heat transfer pore canal is arranged on the entity of the front section of the plunger box, the method belongs to the cooling of the outer side part of the plunger box with small heat transfer load, and is indirect cooling for the plunger sealing piece, and the cooling amplitude is limited;

② direct heat conduction mode, wherein a direct heat conduction mode is used for directly flushing the gap between the plunger and the plunger box at the front section of the plunger assembly by using a cooling flushing liquid and finally entering the main hydraulic cylinder so as to cool the outer surface of the plunger at the front section of the plunger assembly U100 and the inner surface of the plunger box, but the operation mode has limited flow of the flushing liquid, limited cooling amplitude and unsatisfactory cooling effect;

the reason why the flow rate of the flushing liquid cannot be large is that: the larger the flow of the flushing liquid is, the lower the volumetric efficiency of the reciprocating pump is, the larger the increase of the volume of the hydraulic cylinder is caused, the power of the reciprocating pump can be increased greatly, and the power of the flushing liquid conveying pump is also large; meanwhile, the larger the flow of the flushing liquid is, the greater the efficiency of the process device is reduced, which is uneconomical and infeasible for a small-flow reciprocating pump; in an actual industrial device, the ideal mode is to use the flushing liquid with the least amount as possible to complete the intermittent return flushing.

In order to form a simple cooling system for the front section of the plunger assembly U100 without using a large amount of heat transfer fluid, or even with little heat transfer fluid supplied externally, it is necessary to design a heat transfer system having the following dynamic characteristics and flow path characteristics:

① is characterized in that an external power system of the heat conduction system, namely a heat conduction liquid injection system (including a heat conduction liquid injection pump) must be cancelled, obviously, the drive of the heat conduction liquid heat conduction flow process can be completed only by the plunger with the reciprocating motion function of the plunger assembly U100, namely, the liquid cavity and the cavity plug of the auxiliary reciprocating pump are required to be arranged at the front section of the plunger assembly U100;

② flow path is characterized in that in order to reduce the flow rate of externally supplied heat conduction liquid and satisfy the heat conduction requirement of the front section of the plunger assembly U100, the heat conduction liquid must be fully or partially recycled, that is, the inner cavity of the auxiliary reciprocating pump cavity is communicated with the front cavity, based on the principle of the heat conduction liquid circulating and reciprocating flow, the circulation liquid can be flexibly increased without externally supplied heat conduction liquid, so that the heat conduction liquid reciprocates and releases heat through the heat transmitter, generally, the reciprocating frequency and stroke of the plunger are limited by the working parameters of the main cylinder and are inconvenient to adjust, and the radial flow area of the auxiliary pump liquid cavity can be flexibly set, so that the larger the radial flow area of the auxiliary pump liquid cavity is, the larger the heat conduction liquid flow rate of the auxiliary pump is, and the larger the heat conduction capacity is, thus the design flexibility of the heat conduction liquid flow rate is increased;

③ because the pressure difference between the front and back cavities of the auxiliary pump is small, even if the flow of the heat transfer liquid is large, the power consumed by the auxiliary pump is low;

④ Heat transfer component matching with the heat transfer component HX of the heat transfer system to meet the control requirement of the temperature difference DT, the flexibility of design and operation control is large, 1 or 2 parameters of the inlet temperature and flow of the heat transfer medium of the heat transfer component HX can be selected as control parameters, thereby flexibly controlling the temperature of the heat transfer liquid discharged by the HX, namely controlling the temperature of the heat transfer liquid entering the auxiliary pump cylinder.

So far, the concept of providing a built-in heat-conducting reciprocating pump at the front section of the plunger assembly U100 has been proposed, and for the sake of simplifying the description, the present invention also refers to the built-in heat-conducting reciprocating pump as an auxiliary pump.

In the built-in heat-conducting reciprocating pump of the plunger assembly U100, an auxiliary pump liquid cavity FQ (auxiliary pump hydraulic cylinder) is formed by the structures and relative positions of the front section part of a plunger and the front section part of a plunger.

The plunger front section part of the plunger assembly U100 of the invention comprises an auxiliary pump cavity plug QS for driving heat-conducting liquid to flow in a reciprocating manner; the auxiliary pump chamber plug QS contains at least an auxiliary pump main chamber plug ZQS; when the auxiliary pump is provided with a follower chamber, the auxiliary pump chamber plug QS also contains an auxiliary pump auxiliary chamber plug FQS.

According to the plunger assembly U100, reciprocating motion is achieved through an auxiliary pump cavity plug QS contained in a plunger section of an auxiliary pump liquid cavity FQ and used for driving heat conducting liquid to flow in a reciprocating mode, so that the wall of the FQ cavity is also a dynamic heat exchange interface between the heat conducting liquid D L and a plunger box front section part and a plunger front section part, the auxiliary pump cavity FQ is also a heat conducting cavity (heat conducting device), and based on the dual functions, the auxiliary pump is called as a built-in heat conducting reciprocating pump.

The auxiliary pump at the front section of the plunger assembly U100 of the present invention uses heat transfer fluid D L, and the auxiliary pump cavity plug QS reciprocates with the plunger, and the motion form of the auxiliary pump cavity plug QS is necessarily reciprocating motion and is completely inside the plunger box, so the fluid cavity of the auxiliary pump necessarily comprises at least 2 chambers bounded by the cavity plug, the chamber far away from the main fluid cylinder (usually, the chamber determining the single-stroke fluid discharge amount of the auxiliary pump) is called the auxiliary pump inner cavity, and the auxiliary pump chamber near the main fluid cylinder (usually, the chamber providing more heat transfer area of the auxiliary pump) is called the auxiliary pump front cavity.

In order to prevent the auxiliary pump moving member (auxiliary pump chamber plug QS) from colliding with the auxiliary pump fixing member (plunger case), the auxiliary pump at the front section of the plunger assembly U100 according to the present invention must leave a free space in front of the stroke end position and in front of the return stroke end position of the plunger.

The invention is basically characterized in that a reciprocating plunger assembly of a heat-conducting reciprocating pump is arranged in the front section of the plunger assembly, a built-in liquid cavity FQ is arranged between a plunger and a plunger box of the front section of the plunger assembly, the reciprocating plunger assembly comprises an auxiliary pump cavity plug QS for driving heat-conducting liquid to flow in a reciprocating mode through the plunger section of the FQ, the wall of the FQ cavity is also a dynamic heat exchange surface between a heat-conducting liquid D L and the plunger box and the plunger to form the heat-conducting reciprocating pump, namely the auxiliary pump, when the plunger moves to be close to a main liquid cylinder, D L of an auxiliary pump front cavity V6 discharges from a V6 interface N6 to flow to a heat transfer component HX for heat exchange, D L in the HX returns to a V1 for heat conduction through an auxiliary pump inner cavity interface N1 in a forward flow mode, when the plunger moves back to be far away from the main liquid cylinder, D L of 1 discharges to flow to the HX through N1, meanwhile, D L in the HX returns to V6 through N6, the operation between the plunger seal and the main liquid cylinder can be improved, the operation temperature of the plunger seal and the main liquid cylinder, the plunger assembly can be obviously reduced in the application range of the plunger assembly, and the plunger.

The construction and operation of the plunger assembly U100 to achieve the objectives of the present invention are suitable and some specific construction solutions are proposed.

The conveying of high-temperature or low-temperature main medium liquid is a ubiquitous working condition, so that the invention has certain universal application value.

The structural information of the plunger type reciprocating isolating pump is disclosed in the structural information of a publication A01, ①, the name of coal liquefaction technology, pages 118 to 120, ② retrieval uses book codes, ISBN codes, 7-5020-2335-6, ③ Chinese edition library CIP data letters (2003), No. 063071, ④ main codes, Shu-Gong-Ping, ⑤ publisher, coal industry publisher, and the publication introduces the working principle and schematic diagram of the isolating pump for keeping an isolating liquid interface, but does not relate to the plunger component of the built-in heat-conducting reciprocating pump.

The structural information of the plunger type reciprocating isolation pump is disclosed in the patent document A02: ① publication name, the direct coal liquefaction process and engineering (published: 2015 02/h), pages 232 to 233; ② retrieval uses written codes: ISBN codes: 9-78703-04308-23; ③ publication: Wuxiu chapter, Shuyiping, Likejian, Schensh; ④ publication: scientific publishing Co., Ltd.) which describes an oil-coal slurry plunger type reciprocating pump, the working mode of synchronously injecting oil (isolation oil, injection oil), flushing oil and sealing oil is adopted in the plunger sealing box, the stuffing box is a double stuffing box of a metal throttling ring and a special PTFE stuffing ring, the injection oil is injected into a high-pressure stuffing through a synchronously driven shaft head injection pump, the end stuffing is cooled and lubricated by adopting sealing oil, the flushing oil is injected between a low-pressure stuffing and a high-pressure stuffing, the flushing oil is injected into the low-pressure stuffing and the high-pressure stuffing, the action of lubricating and possibly bringing solid particles by the high-pressure stuffing is realized by using a 3 channel stuffing, 2 plunger type stuffing is arranged at the inner end of a main plunger type heat-exchange cylinder, the plunger type heat-exchange plunger assembly (heat-exchange plunger type heat-exchange plunger heat-exchange cylinder heat-exchange plunger heat-exchange.

The plunger reciprocating pump comprises a pump body, a liquid guide pipe, an inlet valve (comprising a valve ball and a valve seat), an outlet valve (comprising the valve ball and the valve seat), a plunger front sleeve, a stuffing box, stuffing and a steam heat-insulation jacket, the plunger reciprocating pump system also comprises driving, sealing oil, steam heat insulation, cooling water, lubricating oil and a variable frequency control system besides the plunger reciprocating pump, an injection pump is configured, an inlet branch pipe, an outlet branch pipe, a main pipe, an inlet buffer tank, an outlet buffer tank and a safety valve, in the document of the Chinese patent Z84, the stuffing box comprises three layers of stuffing which are arranged in sequence from the inside (close to a main liquid cylinder) to the outside (far away from the main liquid cylinder) along the axis of the plunger, the three layers of stuffing are respectively a first layer of stuffing, a second layer of stuffing and a third layer of stuffing, a flushing oil inlet and a flushing oil outlet which are used for flushing the surface of the plunger, a flushing oil inlet and a flushing oil outlet are arranged in the side wall of the stuffing box, the first layer of the stuffing box is respectively a first layer of stuffing, a second layer of stuffing and a third layer of stuffing, a flushing oil inlet and a flushing oil outlet are arranged between the first layer of the stuffing and the second layer of stuffing, a flushing oil outlet, the flushing oil outlet is a flushing oil outlet, the flushing oil outlet is a flushing oil outlet, the flushing oil outlet is arranged in the flushing oil outlet, the flushing oil outlet is arranged in the flushing.

The Chinese patent application No. 201811205520.0, whose application date is 2018, 10 and 10, is a plunger type reciprocating pump, which is suitable for the pressurized delivery of high-temperature oil-coal slurry of a direct coal hydrogenation liquefaction device, and the hydraulic end comprises a main hydraulic cylinder for sucking and discharging the coal slurry and a reciprocating plunger, the structure of a U-shaped flow path of isolation liquid in a conventional main hydraulic cylinder is reserved, and a separator is used for increasing a front flow channel of the isolation liquid contacting with the wall of the main hydraulic cylinder; the path of the injected oil flowing through the inner wall of the main liquid cylinder is prolonged, so that the existing path or the flow path of the injected oil in the main liquid cylinder is in an N shape or a W shape, and the like, and the probability of environment pollution caused by the pollution or leakage of a plunger front sleeve, a plunger and a plunger stuffing box by harmful substances (high-temperature liquid, solid slurry, corrosive or explosive or toxic or radioactive components and the like) is greatly reduced; the heat transfer area and the heat absorption capacity of the cooling main cylinder wall can be obviously increased by the oil injection preposed flow channel, and the heat transferred to the main cylinder wall and the plunger end can be greatly reduced by the steep reduction of the area of the high-temperature coal slurry contacting the main cylinder wall; the pump can convey liquid materials with higher temperature, obviously improves the operation safety of the plunger end and enlarges the application range of the reciprocating pump. The plunger stuffing box assembly of the pump set uses 3 layers of stuffing, 2 layers of stuffing seals are intensively arranged at the outer end (far away from the main cylinder end) of the stuffing box, and 1 layer of stuffing seals is arranged at the inner end (close to the main cylinder end) of the stuffing box; the plunger packing box sealing structure can be applied to working conditions of large flow (namely long plunger formation) and medium and high pressure (such as the pressure of 2.0-25.0 MPa), but does not relate to the plunger assembly of the built-in heat-conducting reciprocating pump.

Similar to the technical scheme of the invention, no report is found.

The first purpose of the invention is to provide a reciprocating plunger assembly with a heat-conducting reciprocating pump arranged in the front section of the plunger assembly.

The second purpose of the invention is to provide a reciprocating plunger pump, wherein the front section of the reciprocating plunger assembly used in the reciprocating plunger pump is provided with a built-in heat conduction reciprocating pump.

Disclosure of Invention

The invention discloses a reciprocating plunger assembly of a heat-conducting reciprocating pump arranged in the front section of the plunger assembly, which is characterized in that:

a reciprocating plunger assembly U100, at least comprising a plunger U110, a plunger housing U130, and a plunger seal U120 installed in the plunger housing;

the plunger U110 is placed in the inner cavity of the plunger U130 and used for reciprocating motion;

the end face of the plunger letter U130, which is in contact with the main hydraulic cylinder, is the front end face of the plunger letter U130, and the end face of the plunger letter U130, which is far away from the main hydraulic cylinder, is the rear end face of the plunger letter U130;

the reciprocating plunger assembly U100 at least uses 2 plunger seals, the plunger seal closest to the rear end face of the plunger box U130 is an outer plunger seal U129, the other plunger seals belong to plunger main seals, and the plunger main seal closest to the outer plunger seal U129 is also called as the outer plunger main seal;

when 2 or more plunger main seals are used in the reciprocating plunger assembly U100, the numbers are sequentially numbered from near to far according to the distance from the front end face of the plunger letter U130, the plunger main seal closest to the front end face of the plunger letter U130 is a1 st plunger main seal U121, and the other plunger main seals are a 2 nd plunger main seal U122, a 3 rd plunger main seal U123 and the like;

the part of the plunger letter U130 between the front end face of the plunger letter U130 and the 1 st plunger main seal U121 is called as the front section of the plunger letter U130;

the part of the plunger letter U130 between the rear end face of the plunger letter U130 and the main seal of the plunger at the outer side is called the rear section of the plunger letter U130;

when the reciprocating plunger assembly U100 uses 2 or more plunger main seals, the plunger letter U130 part between the 1 st plunger main seal U121 and the plunger main seal at the outer side is called the middle section of the plunger letter U130;

a plunger pocket U130 containing at least the plunger packing pocket fitted with or contacting the plunger seal U120 and possibly a plunger barrel not fitted with the plunger seal U120, the plunger barrel adjacent to the main cylinder being referred to as a plunger front barrel;

the reciprocating plunger assembly U100 is characterized by also comprising a built-in auxiliary heat exchange reciprocating PUMP 7PUMP (auxiliary PUMP);

the auxiliary pump is composed and works according to the following principle:

① plunger function U130 front section and reciprocating between the plunger U110 front section, constituting built-in auxiliary pump fluid chamber FQ, plunger U110 front section reciprocating through FQ position set up auxiliary pump fluid chamber plug QS which pushes auxiliary pump fluid chamber FQ fluid movement;

when the plunger U110 reciprocates, the auxiliary pump cavity plug QS is driven to reciprocate to push heat-conducting liquid in the auxiliary pump liquid cavity FQ to reciprocate, and the auxiliary pump cavity plug QS plays a role of a reciprocating pump plunger;

an auxiliary pump liquid cavity FQ is divided into an auxiliary pump inner cavity and an auxiliary pump front cavity by taking an auxiliary pump cavity plug QS as a boundary;

the part of an auxiliary pump liquid cavity FQ far away from the front end surface of the plunger piston U130 by taking an auxiliary pump cavity plug QS as a boundary is an auxiliary pump inner cavity,

the part of an auxiliary pump liquid cavity FQ close to the front end surface of the plunger U130 is an auxiliary pump front cavity by taking an auxiliary pump cavity plug QS as a boundary,

in the reciprocating process of the plunger U110, the liquid suction and discharge space of the inner cavity of the auxiliary pump is called as an inner dynamic cavity of the auxiliary pump, and the volume of the inner dynamic cavity of the auxiliary pump is a dynamic variable quantity;

in the reciprocating process of the plunger U110, the liquid suction and discharge space of the front cavity of the auxiliary pump is called as a front moving cavity of the auxiliary pump, and the volume of the front moving cavity of the auxiliary pump is a dynamic variable quantity;

the auxiliary pump inner cavity is communicated with the auxiliary pump front cavity through a channel and a heat transfer element HX, and the auxiliary pump inner cavity is communicated with the auxiliary pump front cavity through a communicating vessel;

②, the heat transfer element HX is used for receiving the heat-conducting liquid discharged from the auxiliary pump liquid cavity FQ, transferring heat to the heat-conducting liquid to change the temperature of the heat-conducting liquid, returning the heat-conducting liquid after the temperature change of the heat transfer to the auxiliary pump liquid cavity FQ, and heating the wall surface of the auxiliary pump liquid cavity FQ;

③ the heat-conducting liquid in the auxiliary pump fluid cavity FQ reciprocates along with the reciprocating motion of the auxiliary pump cavity plug QS, contacts with the wall of the auxiliary pump fluid cavity FQ to perform reciprocating flow contact heat conduction on the inner surface of the front section of the plunger U130 and the outer surface of the front section of the plunger, the wall of the auxiliary pump fluid cavity FQ is also a heat-conducting surface, and the auxiliary pump fluid cavity FQ is also called as an auxiliary pump heat-conducting cavity;

when the main plunger U110 moves forwards, the main plunger U110 moves forwards close to the main hydraulic cylinder, heat-conducting liquid is discharged from the front movable cavity of the auxiliary pump through the interface N6X and enters the heat transfer element HX, and the heat-conducting liquid with changed temperature discharged from the heat transfer element HX is used as forward cold flow to return to the inner movable cavity of the auxiliary pump through the interface N1X;

when the main plunger U110 makes a return movement, the main plunger U110 makes a return movement away from the main hydraulic cylinder, the heat-conducting liquid is discharged from the internal movable cavity of the auxiliary pump through the interface N1X and enters the heat transfer element HX, and the heat-conducting liquid with the temperature changed and discharged from the heat transfer element HX is returned to the front movable cavity of the auxiliary pump as a reverse cold flow through the interface N6X.

The invention, in general, is in the form of an auxiliary pump plug QS selected from 1 or a combination of several of the following:

① the outer side surface is a smooth cylinder;

②, a cylinder with 1 or 2 or more inner grooves is arranged outside;

③ cylindrical body with internal screw thread on its outer side;

④ is provided with a cylinder communicating the minute passages of the sub pump rear chamber and the sub pump front chamber.

In the invention, the inner cavity form of the front section of the plunger letter U110 is selected from 1 or a combination of several of the following types:

① equal diameter channels with the same inner diameter;

② the inner diameter of the side close to the main cylinder is smaller than that of the side far from the main cylinder;

③ is larger than the main cylinder on the side away from the main cylinder.

According to the invention, the heat transfer element HX is, in general, in the form of 1 or a combination of several selected from the group consisting of:

① independent of the heat transfer element of the plunger barrel;

② converge on the heat transfer element of the plunger barrel.

According to the invention, the heat transfer element HX is, in general, in the form of 1 or a combination of several selected from the group consisting of:

① the heat pipe is a smooth pipe, the guide vane liquid flows in the heat exchange pipe;

② the heat exchange tube is a screw tube, the guide vane liquid flows in the heat exchange tube, the inner side and/or outer side of the heat exchange tube is provided with screw thread;

③ the heat exchange tube is the finned tube, and guide vane liquid flows in the heat exchange tube, and the finned tube is arranged to the heat exchange tube inboard and/or the outside.

In the present invention, the heat transfer member HX is a heat transfer member independent of the plunger sleeve, and the relationship between the elevation of the center of the heat transfer member HX and the elevation of the center of the plunger housing U130 is selected from 1 of the following:

① are equal in height;

②, the central elevation of the heat transfer element HX is lower than the central elevation of the plunger letter U130;

③ the height of the center of the heat transfer element HX is higher than the height of the center of the plunger letter U130.

In the present invention, in general, the heat transfer member HX, and the heat transfer medium used for heat transfer with the heat transfer fluid are selected from 1 of the following:

① gas, possibly air;

② liquid, which may be water or oil;

③ gas-liquid mixture.

In the invention, in general, the ratio K700 of the volume infusion amount 7PUMP-RW of the built-in auxiliary heat exchange reciprocating PUMP 7PUMP to the volume infusion amount U100-RW of the main hydraulic cylinder driven by the reciprocating plunger assembly U100 is (7PUMP-RW)/(U100-RW), and K700 is selected from 1 of the following types:

① is less than 0.1;

②0.1~0.3;

③0.3~1.0;

④ is greater than 1.0.

According to the invention, generally, the cavity wall area of the front dynamic cavity of the auxiliary pump is K300 times of the cavity wall area of the internal dynamic cavity of the auxiliary pump, and K300 is selected from 1 of the following types:

①0.5~1.0;

②1.0~3.0;

③ is greater than 3.0.

In the invention, the reciprocating plunger assembly U100 can be provided with 2 plunger seals, and the functions of the reciprocating plunger assembly U are as follows:

① outside plunger seal, preventing the liquid in the space between 2 plunger seals from leaking to the outside environment;

② plunger primary seal, preventing leakage of primary cylinder media into the space between the 2 plunger seals.

In the invention, the reciprocating plunger assembly U100 can be provided with 3 plunger seals, and the functions of the reciprocating plunger assembly U are as follows:

① outside plunger seal, preventing the liquid in the space between the outside plunger seal and the outside plunger main seal from leaking to the outside environment;

② the 2 nd or outer plunger primary seal prevents liquid in the space between the 2 nd and 1 st plunger primary seals from leaking into the space between the outer and 2 nd plunger primary seals;

③ plunger primary seal 1, prevents leakage of primary cylinder media into the space between plunger primary seal 1 and plunger primary seal 2.

In the invention, the reciprocating plunger assembly U100 can be provided with 4 plunger seals, and the functions of the reciprocating plunger assembly U are as follows:

① outside plunger seal, preventing the liquid in the space between the outside plunger seal and the outside plunger main seal from leaking to the outside environment;

② the 3 rd plunger main seal, i.e. the outer plunger main seal, prevents the liquid in the space between the 3 rd plunger main seal and the 2 nd plunger main seal from leaking into the space between the outer plunger main seal and the 3 rd plunger main seal;

③ plunger primary seal 2, preventing liquid in the space between the plunger primary seal 2 and the plunger primary seal 1 from leaking into the space between the plunger primary seal 2 and the plunger primary seal 3;

④ plunger primary seal 1, prevents leakage of primary cylinder media into the space between plunger primary seal 1 and plunger primary seal 2.

The present invention, generally, a reciprocating plunger assembly U100, provides at least 2 plunger seals;

and the sealing liquid is continuously or discontinuously replaced in the gap between the outer plunger seal and the outer plunger main seal, so that the liquid material passing through the outer plunger main seal is prevented from polluting the outer plunger seal.

The present invention, generally, a reciprocating plunger assembly U100, provides at least 2 plunger seals;

at plunger letter U130 anterior segment, use and keep apart the flush fluid, continuous or be interrupted the injection plunger letter U130 anterior segment, the isolation flush fluid of injection finally enters into main hydraulic cylinder, prevents that the liquid material that comes from main hydraulic cylinder from polluting plunger letter U130 anterior segment and then polluting the 1 st plunger main seal.

According to the invention, the reciprocating plunger assembly U100 can be provided with at least 3 plunger seals, namely at least 2 plunger main seals;

in the gap JX-23 between any 2 plunger main seals, continuous or intermittent replacement of flushing liquid is used to prevent liquid material from the space near the main cylinder side from penetrating the plunger main seal into the gap JX-23 to cause pollution.

The present invention, generally, a reciprocating plunger assembly U100, provides at least 2 plunger seals;

an isolation flushing liquid is continuously or discontinuously injected into the front section of the plunger letter U130 at the front section of the plunger letter U130, and the injected isolation flushing liquid finally enters the main hydraulic cylinder to prevent liquid materials from the main hydraulic cylinder from polluting the front section of the plunger letter U130 and further polluting the 1 st plunger main seal;

the working mode of the isolation flushing liquid can be selected from 1 of the following modes:

①, the plunger U110 moves to the whole distance to separate and flush based on the reciprocating motion of the plunger U110;

② the return process of the plunger U110 is isolated and washed by taking the reciprocating motion of the plunger U110 as the reference;

the isolation flushing liquid adopts a working mode of plunger return synchronous injection, when the plunger U110 is in a return stroke, the main hydraulic cylinder sucks liquid materials, and the plunger of the injection pump for isolating the flushing liquid acts to flush the isolation liquid cavity at the front section of the plunger of the reciprocating plunger assembly U100; when the plunger U110 is in a forward stroke, the main cylinder discharges liquid materials, the plunger of the injection pump for isolating flushing liquid acts to suck the isolating liquid, and the front section of the plunger U130 of the reciprocating plunger assembly U100 is not flushed.

The invention, in general, is a plunger U130, in a form selected from 1 of:

① are one-piece components;

② is the assembly of the anterior segment of plunger case and the posterior segment of plunger case of 2 separate parts, the anterior segment of plunger case is a part, the posterior segment U131 of plunger case is another part;

③ is an assembly of multiple separate parts;

when the plunger assembly U130 comprises 2 or more plunger assembly sections, the complete plunger assembly U130 is formed after assembly.

In the invention, generally, the plunger letter U130 is an assembly of a plunger letter front section and a plunger letter rear section which are 2 split parts, wherein the plunger letter front section is one part, and the plunger letter rear section is the other part;

a reciprocating plunger assembly U100 provided with at least 2 plunger U110 seals;

at least 1 plunger U110 seal is arranged at the rear section of the plunger box, and at most all the plunger U110 seals are arranged.

In the invention, generally, the plunger letter U130 is an assembly of a plunger letter front section and a plunger letter rear section which are 2 split parts, wherein the plunger letter front section is one part, and the plunger letter rear section is the other part;

a reciprocating plunger assembly U100 provided with at least 2 plunger U110 seals;

at least 1 plunger U110 seal can be arranged at the front section of the plunger box.

According to the reciprocating plunger assembly U100, an auxiliary pump follow-up cavity can be arranged, and an auxiliary pump main cavity plug ZQS and an auxiliary pump auxiliary cavity plug FQS are arranged;

the auxiliary pump follow-up cavity is communicated with the inner cavity of the auxiliary pump through a passage AN1 and a heat transfer element HX which can be used, and the auxiliary pump follow-up cavity is communicated with the front cavity of the auxiliary pump through a passage AN2 and a heat transfer element AHX which can be used;

the auxiliary pump is provided with at least one heat transfer component which is a heat transfer component HX and/or a heat transfer component AHX;

the auxiliary pump follow-up cavity, the auxiliary pump inner cavity and the auxiliary pump front cavity are in a communicating vessel relationship.

In general, the relationship between the reciprocating plunger assembly U100, the auxiliary pump chamber plug QS and the plunger box, 1 of the following is selected for the present invention:

① the auxiliary pump cavity plug QS is not in contact with the plunger cage, and a gap exists;

② contact between the auxiliary pump cavity plug QS and the plunger box, the contact part is the auxiliary pump cavity separating filler which is installed on the plunger U110;

③ the auxiliary pump chamber plug QS is in contact with the plunger housing at the contact portion where the auxiliary pump chamber partition packing is mounted on the plunger housing U130.

In the present invention, in general, the absolute value of the difference between the operating temperature T2 of the plunger main seal closest to the main cylinder, i.e., the 1 st plunger main seal, and the main cylinder operating temperature T1 of the reciprocating plunger assembly U100 is selected from 1 of the following:

①30~60℃;

②60~90℃;

③90~150℃;

④150~200℃;

⑤ is greater than 200 ℃.

In the invention, the reciprocating plunger assembly U100 can be provided with a heat exchange jacket on the cylinder body of the plunger assembly U130, and the medium flowing in the heat exchange jacket and the working mode are selected from 1 or the combination of several of the following types:

① the heat-extracting medium with cooling effect is gas phase and/or liquid phase;

② the heating medium for heating is gas phase and/or liquid phase;

③ the heat-extracting medium with cooling and temperature control functions is in gas phase and/or liquid phase;

④ are used for heating medium with temperature control function, and are in gas phase and/or liquid phase.

The main cylinder K10, typically the pump cylinder K10 of a plunger reciprocating pump apomp, is used in conjunction with the reciprocating plunger assembly U100 of the present invention.

The plunger type reciprocating pump APUMP system can use 1 or 2 or more pump cylinders with single pump cavities.

The plunger type reciprocating pump APUMP system of the invention uses an integrated pump cylinder body which can have 1 or 2 or more pump chambers.

The pumping target liquid material of the plunger type reciprocating pump APUMP can be selected from 1 or more of the following materials:

① high temperature liquid material;

② low temperature liquid material;

③ high-pressure liquid material;

④ high temperature and high pressure liquid material;

⑤ high temperature and high pressure solid-liquid containing material;

⑥ liquid material containing easily coagulating component;

⑦ liquid material containing volatile component;

⑧ contains a solid slurry;

⑨ liquid material containing corrosive components;

⑩ liquid material containing explosive component;

liquid material containing toxic components;

a liquid material containing radioactive components.

The working mode of the injection liquid added into the stuffing box or the plunger sleeve of the plunger type reciprocating pump APUMP is selected from 1 or more of the following types:

① can be used for long term after being injected once;

② intermittent injection and discharge are performed, and the injected liquid finally enters the pump cavity of the pump body and is discharged out of the pump cavity along with the pumped target liquid;

③ the injection is continuously discharged, and the discharged injection liquid finally enters the pump cavity of the pump body and is discharged out of the pump cavity along with the pumping target liquid.

In the present invention, the operating conditions of the plunger type reciprocating pump APUMP are, in general: the temperature is 150-400 ℃, the inlet pressure is 0.3-1.0 MPa, the outlet pressure is 2.0-30.0 MPa, the weight concentration of solid particles is 0-55%, and the volume flow rate of liquid material at the inlet of the pump cavity is 0.1-150 m3/h。

The plunger type reciprocating pump APUMP can be an oil coal slurry booster pump in the direct coal hydrogenation liquefaction reaction process or the kerosene co-refining hydrogenation reaction process, and the operation conditions are as follows: the temperature is 150-350 ℃, the inlet pressure is 0.3-1.0 MPa, the outlet pressure is 2.0-30.0 MPa, the weight concentration of solid particles is 25-60%, and the volume flow rate of liquid material at the inlet of the pump cavity is 0.1-200 m3/h。

The invention relates to a plunger type reciprocating pumpThe APUMP can be an oil coal slurry booster pump in the coal hydrogenation direct liquefaction reaction process or the kerosene co-refining hydrogenation reaction process, and the operation conditions are as follows: the temperature is 150-350 ℃, the inlet pressure is 0.3-1.0 MPa, the outlet pressure is 5.0-30.0 MPa, the weight concentration of solid particles is 40-55%, and the volume flow rate of liquid material at the inlet of the pump cavity is 10-150 m3/h。

The plunger type reciprocating pump APUMP can be an oil coal slurry booster pump in the coal hydrogenation direct liquefaction reaction process or the kerosene co-refining hydrogenation reaction process, and the quantities of working fluids of a plunger, a packing box and a plunger outer sleeve are as follows: the hourly volume flow of the injected liquid is 0.5-5% of the volume flow of the pumping target liquid of the plunger type reciprocating pump APUMP.

Generally, the plunger type reciprocating pump APUMP of the invention is arranged in the following way: the axis of the plunger (111) is arranged horizontally, the pump cylinder K10 is arranged vertically, the used divider XKP is arranged vertically, and the used liquid guide tube (33) is arranged vertically.

Generally, at the drive end of the plunger type reciprocating pump APUMP system of the invention, the prime mover is selected from 1 of the following:

① a motor;

② variable frequency motor;

③ diesel engines;

④ a hydraulic motor;

⑤ steamer.

Generally, the driving end of the plunger type reciprocating pump APUMP system uses a speed changer to convert high-speed motion of a prime motor into low-speed motion, and then drives a hydraulic end to work.

In general, the plunger type reciprocating pump APUMP system of the present invention comprises 1 or 2 or more pump cylinders, 1 or 2 or more plunger assemblies are used together, and 2 or more plunger assemblies use a heat transfer device HX and use the same heat transfer medium.

In general, the plunger type reciprocating pump APUMP and the system thereof form an integrated skid-mounted structure by part or all of components.

Drawings

FIG. 1 is a schematic diagram of a plunger type reciprocating pump of a plunger assembly of a conventional structure using return flushing oil for conveying coal slurry for a coal hydrogenation direct liquefaction device.

Fig. 2 is a detailed view of a portion of the plunger assembly and associated components of fig. 1.

As shown in fig. 1 and 2, the plunger assembly of the plunger type reciprocating pump comprises a stuffing box 115 and a plunger front sleeve 119.

The plunger assembly of the plunger type reciprocating pump shown in fig. 1 and 2 is provided with 3 filler seals, namely a1 st plunger main seal, a 2 nd plunger main seal and an outer plunger seal, in sequence from the side close to the main cylinder to the side far from the main cylinder according to the plunger axis.

As shown in fig. 1 and 2, the 1 st plunger main seal belongs to a high-pressure packing seal, the 2 nd plunger main seal (also an outer plunger main seal) belongs to a low-pressure packing seal, the outer plunger seal belongs to a low-pressure packing seal, and the functions and working modes of the plunger seals are as follows:

① st plunger main seal and 1 st flushing liquid system

The 1 st plunger main seal close to the main hydraulic cylinder has the task of separating a high-pressure medium from leaking and flowing to one side of the middle section of the plunger housing beyond the 1 st plunger main seal as far as possible, in order to prevent harmful substances (high-temperature liquid, solid slurry, corrosive or explosive or toxic components) in the main medium from entering the packing (sealing packing) part of the plunger front sleeve, the packing housing, the plunger housing and the plunger sealing member, prevent the high-temperature medium from entering the plunger front sleeve, the packing housing from contacting the plunger, the plunger housing and the plunger sealing member to generate ultralimit thermal deformation, prevent solid particles from entering the packing part of the plunger sealing to accelerate the abrasion of the packing, prevent the corrosive medium from corroding the contacted part, or prevent the harmful components from entering the middle section and the front section of the plunger assembly U100 to leak into the environment or contact with a human body, arranging a No. 1 flushing fluid system at the front end (the end close to a main pump cylinder) of a No. 1 plunger main seal, and forming flushing fluid (isolating fluid) flowing towards the main pump cylinder between a plunger and a plunger assembly in a high-pressure working cavity of the plunger assembly to prevent a main medium in the main cylinder from flowing into a stuffing sealing part of the plunger assembly, so that a plunger sealing member is effectively isolated from a main pumping medium during the normal working period of a pump set, and for a coal slurry pump, the method is usually to intermittently inject and intermittently discharge or continuously inject and continuously discharge the No. 1 flushing fluid;

the working mode of the flushing liquid can be continuous injection and continuous discharge, namely, full flushing;

the working mode of the flushing liquid can be intermittent injection and intermittent discharge, the working mode can be any effective working mode, and the common working mode is plunger return flushing;

a1 st flushing liquid flushing chamber is called as a1 st flushing chamber;

② No. 2 plunger primary seal and No. 2 flushing oil system

Between the 1 st plunger main seal (high pressure packing seal) and the 2 nd plunger main seal (low pressure packing seal), a low pressure flushing cavity (called as 2 nd flushing cavity) with proper pressure is arranged to prevent the medium from the high pressure side of the 1 st plunger main seal from leaking and flowing to the 2 nd plunger main seal and further leaking to the plunger seal at the outer side, therefore, the operating pressure of the 2 nd flushing cavity is lower than that of the low pressure sealing cavity, and a small amount of sealing oil can flow to the 2 nd flushing cavity through the gap between the 2 nd plunger main seal and the plunger;

when the pump set normally works, the 2 nd flushing oil enters the 2 nd flushing cavity through the 2 nd flushing oil injection hole to maintain the operating pressure of 1.00-1.10 MPa (G), then the 2 nd flushing oil flowing through the 2 nd flushing cavity is discharged out of a plunger housing (stuffing housing) through the 2 nd flushing oil discharge hole, and the possible series flow 1 st flushing oil from the 1 st flushing cavity and series flow sealing oil from the sealing cavity are carried out of the 2 nd flushing cavity together;

③ outside plunger seal and low pressure seal oil system

The function of the outside plunger sealing packing is to seal the plunger, prevent the medium from the sealing cavity side from leaking to the outside and polluting the environment, and simultaneously prevent the lubricating oil from the power end from invading and polluting the plunger box (packing box) and the plunger surface;

when the pump package normally worked, low pressure seal oil got into the seal chamber through the seal oil filling hole and maintains operating pressure for example 1.10 ~ 1.20MPa (G) (be a little higher than 2 nd washing chamber operating pressure), then most seal oil discharge hole discharge plunger box's packing box through the seal oil, because seal chamber operating pressure is higher than 2 nd washing chamber operating pressure, have a small amount of seal oil to reveal, flow to 2 nd washing chamber through the clearance between 2 nd plunger main seal and the plunger.

In the plunger type reciprocating pump of the plunger assembly with the conventional structure for conveying coal oil slurry and using flushing oil, shown in fig. 1 and 2, a1 st flushing liquid is regularly added into a stuffing box of a plunger box according to a return flushing mode, passes through a plunger front sleeve and then enters a main liquid cylinder of the pump, and a flow path of the 1 st flushing liquid discharged out of the main liquid cylinder belongs to a U-shaped flow.

In fig. 1 and 2, 7 is a lens pad, 8 is a flange cover, 9 is a stud a, 10 is a nut a, 12 is a truss, 13 is a heat insulation board, 14 is a screw, 15 is a pump body component (main liquid cylinder), 16 is a pin, 171 is a feeding check valve (171-1 is a valve body, 171-2 valve seat, 171-3 is a valve ball guide sleeve, 171-4 valve ball), 172 is a discharging check valve (172-1 is a valve body, 172-2 valve seat, 172-3 is a valve ball guide sleeve, 172-4 valve ball), 18 is a nut B, 19 is a stud B, 20 is a discharging pipe, 21 is a pin, 22 is a stud, 23 is a nut, 24 is a lens pad, 25 is a support stud, 26 is a nut, 27 is a stud heat insulation board, 28 is a round nut, 29 is a nut protective sleeve, 30 is a long nut sleeve, 31 is a stud C, 32 is a nut C, 33 is a liquid guide pipe, 34 is, 35 is a heat insulation gasket, 36 is a pressing block, 37 is a lens pad, 38 is a threaded flange, 39 is a stud, 40 is a nut, 41 is a different-neck flange, 42 is a stud, 43 is a nut, 44 is a sealing gasket, 45 is an elbow flange, 111 is a plunger, 115 is a stuffing box of the stuffing box, 119 is a plunger front sleeve of the stuffing box, 151 is a 2 nd flushing oil inlet, 152 is a 2 nd flushing oil outlet, 191 is a1 st flushing liquid injection through hole, 251 is a sealing oil inlet, 252 is a sealing oil outlet, 701 is a steam inlet, 702 is a steam outlet, R100 is a first packing (a 1 st plunger main sealing packing), R200 is a second packing (a 2 nd plunger main sealing packing), R300 is a third packing (an outer plunger packing), and R700 is a steam heat insulation jacket.

In fig. 2, the following part numbers are indicated:

① N01 is an outer plunger packing gland (third packing gland), the outer part of the outer plunger packing gland N01 is an outer end N01c with screw thread, N01c is matched with a matching screw thread section on the inner side of the outer end part of an outer plunger packing box (third packing box) N06 to complete assembly, fastening, connection and positioning, and meanwhile, the outer plunger packing (third packing) N03 is a compression part to realize reasonable pre-pressure and compression deformation on the 3 rd packing N03, so that the 3 rd packing N03 is tightly matched with the plunger 111;

② N02 is an outer side backing ring of an outer side plunger packing (third packing);

③ N03 is an outer plunger packing (third packing);

④ N04 is an outside plunger packing (third packing) inside long distance backing ring;

⑤ N05 is static sealing ring;

⑥ N06 is an outer plunger packing box (third packing box) (middle packing gland, i.e. 2 nd plunger main seal packing gland);

⑦ N07 is an intermediate filler (second filler) outer backing ring;

⑧ N08 is an intermediate filler (second filler);

⑨ N09 is an intermediate filler (second filler) inside backing ring;

⑩ N10 is a pressing piece of intermediate filler (second filler) and is a pressing piece with threads, the pressing piece is matched with a matched thread section on the inner side of the outer end of the stuffing box 115 to complete assembly, fastening, connection and positioning, and meanwhile, the pressing piece of the intermediate filler (second filler) N08 realizes reasonable pre-pressure and pressing deformation on the 2 nd filler N08, so that the 2 nd filler N08 is tightly matched with the plunger 111;

n51 is the outside long distance backing ring of the 1 st plunger main sealing packing;

n52 is the 1 st plunger main sealing packing;

n53 right side fastener for the 1 st plunger main seal packing1, a flushing fluid guide sleeve;

n531 is an opening arranged on the right flushing guide sleeve of the 1 st plunger main seal packing and communicated with the 1 st flushing liquid port 191;

n54 is the positioning part and the pre-tightening part of the flushing guide sleeve at the front end of the 1 st plunger main sealing packing.

The plunger type reciprocating pump shown in fig. 1 can be used for conveying coal slurry of a coal hydrogenation direct liquefaction device, and the working modes of the feeding stroke (the return stroke of the plunger 111) and the discharging stroke (the process of the plunger 111) of a main medium of a main liquid cylinder are as follows:

① when the main cylinder 15 is in the feeding stroke of pumping the target liquid (such as coal slurry), the plunger 111 is in the return process, the plunger 111 is far away from the main cylinder 15, the liquid level of the main medium (such as coal slurry) pumped in the main cylinder 15 rises, normally the main medium (such as coal slurry) is not allowed to exceed the main cylinder and enter the plunger front sleeve 119 and the stuffing box 115, thus causing the isolation failure;

② when the main cylinder 15 is IN the process of discharging the pumped target liquid (such as coal slurry), the plunger 111 is IN the process, the plunger 111 is close to or enters the main cylinder 15, the liquid level of the pumped main medium (such as coal slurry) IN the main cylinder 15 drops, flows into the interior of the liquid guide pipe 33 through the side opening at the lower part of the liquid guide pipe 33, rises along the inner cylinder chamber 33IN-V and finally discharges the main cylinder outlet check valve, the pumped main medium which is discharged from the main cylinder outlet check valve and possibly carries the 1 st flushing liquid (which IN the long term must carry the 1 st flushing liquid), so that the pumped main medium and the 1 st flushing liquid which enter the pump chamber are discharged out of the main cylinder 15.

For the end position of the plunger process, the built-in auxiliary PUMP 7PUMP at the front section of the plunger assembly U100 is bounded by an inlet and an outlet N6 (the inlet and the outlet can be shared) of the heat-conducting liquid of an auxiliary PUMP front cavity, and the space which is communicated with N6 and can be repeatedly filled and occupied by the heat-conducting liquid at one side of the auxiliary PUMP front cavity is called a motion cavity of the auxiliary PUMP front cavity, which is called as an auxiliary PUMP front motion cavity V6 for short; the auxiliary pump forward moving cavity V6 generally comprises a liquid suction and discharge cavity of the auxiliary pump forward moving cavity and a relative stagnation cavity of the auxiliary pump forward moving cavity. For the plunger process termination position, the space from the position N6 to the position of the auxiliary pump cavity plug surface on the side of the auxiliary pump front cavity belongs to the detention zone of the auxiliary pump front cavity; when the 1 st plunger main seal front end of the plunger assembly U100 uses the isolation flushing liquid, the auxiliary pump front moving cavity is also the flow channel cavity of the isolation flushing liquid naturally.

The liquid region where the plunger is relatively stationary with respect to the auxiliary pump region or the plunger housing with respect to the auxiliary pump region is referred to as a stagnant region, however, the liquid region where the plunger is relatively stationary with respect to the auxiliary pump region may be dynamic with respect to the plunger housing of the auxiliary pump region, and the stagnant region is also referred to as a semi-stagnant region in the present invention, and has a certain heat conduction function.

For the end position of the plunger process, the front part of the front moving cavity of the auxiliary pump of the plunger assembly U100 is a plunger space communicated with the main hydraulic cylinder, a reciprocating motion space filled with liquid in the space, and a discharge channel of isolation flushing liquid which can be used.

For the auxiliary pump at the front section of the plunger assembly U100, regarding the end position of the return stroke of the plunger, a heat-conducting liquid inlet/outlet N1 (an outlet and an inlet can be shared) of an inner cavity of the auxiliary pump is taken as a boundary, and a space which is communicated with N1 and can be repeatedly filled and occupied by the heat-conducting liquid at one side of the inner cavity of the auxiliary pump is called a motion cavity of the inner cavity of the auxiliary pump, namely an inner dynamic cavity V1 of the auxiliary pump for short; the auxiliary pump internal dynamic cavity generally comprises a liquid suction and discharge cavity of the auxiliary pump internal dynamic cavity and a relative stagnation cavity of the auxiliary pump internal dynamic cavity. For the return stroke end position of the plunger, the space on the side of N1 far away from the plug of the auxiliary pump cavity belongs to a residual cavity of the inner cavity of the auxiliary pump, namely the residual cavity of the auxiliary pump; when the 1 st plunger main seal front end of the plunger assembly U100 uses the isolation flushing liquid, the auxiliary pump residual cavity is also the flow channel cavity of the isolation flushing liquid.

The structure, design principles and operation of the plunger assembly U100 of the present invention are described below in conjunction with fig. 3.

Fig. 3 is a schematic structural diagram of a plunger return end state of the reciprocating plunger assembly of the first technical solution of the reciprocating plunger assembly of the present invention, wherein the front section of the plunger assembly is internally provided with a heat-conducting reciprocating pump.

Fig. 4 is a detail view of the front end structure of the plunger assembly of fig. 3.

Fig. 5 is a detailed view of a portion of the built-in thermally conductive reciprocating pump of fig. 4.

In the first technical scheme of the reciprocating plunger assembly of the plunger assembly front-section built-in heat-conducting reciprocating PUMP of the invention shown in fig. 3, the main difference from the technical scheme of the plunger assembly shown in fig. 2 is that the internal structure of the plunger front sleeve 119 (namely the plunger housing front section) shown in fig. 2 is changed, the external structure of the plunger front section 111 is changed to form the built-in heat-conducting reciprocating PUMP 7PUMP, liquid in the liquid suction and discharge cavity V1 in the auxiliary PUMP inner cavity is sucked and discharged by virtue of the process and return stroke reciprocating motion of the plunger 111 with the one-way stroke of L, liquid sucked in the liquid suction and discharge cavity V1 of the auxiliary PUMP inner cavity is heat-conducting liquid cooled by the heat transmitter HX, liquid discharged by V1 is heat-heated liquid by the cavity wall of V1 (the plunger outer surface of the auxiliary PUMP inner cavity and the plunger housing inner surface), and liquid sucked in and discharged by virtue of the process and return stroke of the plunger 111 of L1 is heat-conducting liquid suction and discharge cavity V6, liquid in the liquid suction and discharge cavity V6 of the auxiliary PUMP front cavity is heated liquid heat-conducting cavity (plunger housing inner surface of the plunger piston 3526 and plunger housing V3526).

The 1 st technical solution of the present invention shown in fig. 3 is also different from the conventional technical solution shown in fig. 1 in that: the steam inlet 701, the steam outlet 702 and the steam heat-preserving jacket R700 in the technical scheme shown in the figure 1 are all eliminated. Of course, the steam inlet 701, the steam outlet 702 and the steam heat-preserving jacket R700 can be reserved according to actual needs.

As shown in fig. 3, the main cavity plug ZQS of the auxiliary pump acts to suck and discharge liquid in the auxiliary pump cavity and the auxiliary pump front cavity, and the auxiliary pump cavity and the auxiliary pump front cavity operate synchronously in time sequence but have opposite liquid inlet and liquid discharge actions, that is, the auxiliary pump front cavity feeds liquid when the auxiliary pump cavity discharges liquid, the auxiliary pump front cavity discharges liquid when the auxiliary pump cavity feeds liquid, and the two cavities of the auxiliary pump are in a dynamic communicating vessel relationship.

As shown in fig. 3, the auxiliary pump internal dynamic chamber is also referred to as an auxiliary pump intrinsic volume chamber because the volume of the auxiliary pump internal dynamic chamber V1 determines the liquid suction amount or the liquid discharge amount of a single stroke of the auxiliary pump.

As shown in fig. 3, under the design principle of the reciprocating plunger assembly that the length of the plunger is shortened as much as possible and the dynamic stability of the plunger assembly is improved, the cavity wall area of the intrinsic volume cavity V1 cannot be increased at will (normally, it should be shortened as much as possible), so theoretically, the heat conduction area needs to be increased as much as possible in the auxiliary pump front-acting cavity V6, and the cavity wall area of the auxiliary pump front-acting cavity V6 generally determines the main heat exchange area of the auxiliary pump in a single stroke of the auxiliary pump; when the heat conduction area of the auxiliary pump front dynamic cavity V6 is far larger than that of the auxiliary pump front dynamic cavity V6, the auxiliary pump front dynamic cavity V6 can also be called an auxiliary pump main heat exchange cavity.

As shown in fig. 3, the auxiliary pump internal dynamic chamber V1 is referred to as an auxiliary pump intrinsic volume chamber, and during a single movement of the plunger 111, the auxiliary pump intrinsic volume chamber determines the volume of the intake liquid or the discharge liquid of the auxiliary pump internal dynamic chamber, that is, the overflow rate of the heat exchanger HX, and thus, it essentially determines the heat transfer rate of the internal heat transfer reciprocating pump system.

As shown in fig. 3, the auxiliary pump intrinsic volume chamber V1 requires increasing the volume of V1 in order to increase the overflow of heat exchanger HX, and under the condition of constant reciprocation frequency and constant stroke length of plunger 111, the radial cross-sectional area S1 of the V1 gap must be increased, i.e., the gap width H1 must be increased, or the gap height H1 of the built-in heat transfer reciprocating pump must be determined according to the heat exchange load of heat exchanger HX. The auxiliary pump intrinsic volume chamber V1 shown in fig. 3 is a ring column type gap with a radial cross-sectional area S1 ═ pi (r + H1)2-πr2. R is the auxiliary pump lumen plunger rod radius and (r + H1) is the auxiliary pump lumen main plunger ZQS radius.

As shown in fig. 5, r is the auxiliary pump lumen plunger rod radius, H1 is the auxiliary pump lumen main plug ZQS height, and P is the auxiliary pump main plug ZQS width.

Under the condition of not changing the motion frequency and the stroke of the plunger, the main design principle of the invention is to enlarge the heat exchange area as much as possible and improve the heat exchange efficiency, so that the auxiliary pump front dynamic cavity V6 can be provided with a gap H6 with a smaller gap distance than H1 on the premise of ensuring the fluid to reciprocate smoothly (the pressure difference between V1 and V6 is smaller).

In fig. 3, the front moving cavity V6 of the auxiliary pump is a ring column type gap, and the radial sectional area S1 ═ pi (r + H1)2-π(r+H1-H6)2

Thus, a single stroke L1 of the auxiliary pump intrinsic volume V1 will cause a liquid motion with a stroke (S1/S6) ×L 1 in the auxiliary pump forward chamber V6, for example, the design S1/S6 is 2, so that the axial length of the space occupied by the heat transfer liquid in V6 is about 2 ×L 1, and obviously, the dynamic chamber wall area of the auxiliary pump forward chamber V6 is about 2 times the dynamic chamber wall area of the auxiliary pump intrinsic volume V1.

In order to further improve the heat exchange efficiency, a semi-retention area with a proper length is arranged between the surface of the main cavity plug ZQS on the inner cavity side of the auxiliary pump and the communication pipe N1 of the heat exchanger HX, and between the surface of the main cavity plug ZQS on the front cavity side of the auxiliary pump and the communication pipe N6 of the heat exchanger HX by utilizing the dynamic relation between the static plunger function and the dynamic auxiliary pump liquid cavity at the front section of the plunger assembly U100; the semi-detention area is relative to the auxiliary pump cavity plug and the auxiliary pump plunger, however, the liquid in the semi-detention area is inevitably in contact with the inner surface of the plunger to generate heat conduction along with the reciprocating motion process of the auxiliary pump cavity plug, and meanwhile, heat is transferred through the plunger and the plunger, so that the semi-detention area also has certain heat exchange capacity and has the function of increasing the heat conduction area, and the semi-detention area is called as an extended heat conduction area (extended heat conduction cavity). As shown in fig. 3, the auxiliary pump front chamber and the auxiliary pump rear chamber are each provided with a half-stagnation region having a heat exchange function.

In the process of reciprocating motion relative to the static plunger box, part of the heat exchange surface of the dynamic auxiliary PUMP liquid cavity (the plunger surface of the auxiliary PUMP internal dynamic cavity and the auxiliary PUMP front dynamic cavity) of the built-in heat-conducting reciprocating PUMP 7PUMP can extend into the space outside the auxiliary PUMP internal dynamic cavity and the auxiliary PUMP front dynamic cavity to exchange heat with liquid materials, so that a secondary expansion heat-conducting area is formed.

As shown in fig. 3, the outer surface of part of the plunger rod of the auxiliary pump intrinsic volume chamber V1 can extend into the residual chamber V0 area of the auxiliary pump inner chamber during the plunger return process to exchange heat with the liquid material; during the process of the plunger, part of the outer surface of the plunger rod of the front moving cavity V6 of the auxiliary pump extends into the area V9 to exchange heat with liquid material to form a secondary expansion heat conduction area.

As described above, the heat exchange area of the heat-conducting reciprocating PUMP 7PUMP provided in the front section of the plunger assembly according to the present invention is large, and thus heat exchange can be performed efficiently.

As described above, the technical solution of the present invention has the characteristics of large flow rate of the heat transfer liquid and large heat transfer area, and therefore, the objective of the present invention of significantly expanding the temperature difference between the packing seal operation temperature and the main medium operation temperature of the main liquid cylinder can be achieved.

Regarding the relative position of the auxiliary pump chamber connection pipe N1 and the auxiliary pump chamber plug, in the plunger return end state, the auxiliary pump chamber plug should be positioned between the openings N1 and N2 and as close as possible to the opening N1.

In the position of the sub pump front chamber connection pipe N6 and the position of the sub pump chamber plug relative to each other, the sub pump plunger should be positioned between the ports N1 and N2 and as close as possible to the port N2 in the plunger stroke end state.

The distance between the openings N1 and N2 is at least equal to or more than (L1 + P), P is the width of the main cavity plug ZQS, preferably equal to or less than L1 × (S1/S6), the phenomenon that the opening N6 sucks in a heat medium is avoided, the opening N6 sucks in a circulating heat-conducting medium as much as possible is ensured, and the distance between the N1 and the N2 can be more than L1 × (S1/S6) according to needs, but the volume of a semi-stagnation area is theoretically increased, and the overall length of the plug is prolonged.

As shown in fig. 3, when the return stroke of the plunger 111 is terminated, the gap space between the auxiliary pump main chamber plug ZQS and the opening N1 becomes a semi-stagnation area of the auxiliary pump inner chamber.

As shown in fig. 3, when the return stroke of the plunger 111 is terminated, the volume of the suction and discharge liquid chamber V1 of the auxiliary pump internal dynamic chamber is theoretically zero, that is, the heat transfer liquid in the suction and discharge liquid chamber V1 of the auxiliary pump internal dynamic chamber is completely discharged V1 through the opening N1 to the heat exchanger HX.

Regarding the flow path of the heat transfer fluid during the return process of the plunger 111, as shown in fig. 3, the heat transfer fluid in the auxiliary pump inner cavity V1 is pushed by the auxiliary pump main cavity plug ZQS to discharge V1 through the openings N1 and N11, and enters the heat exchanger HX through the pipe P108 to release the heat absorbed by the V1 after being merged by the pipe P101 and the pipe P102, and at the same time, the cooled heat transfer fluid discharged by the heat exchanger HX is transported through the pipe P608, and is divided into 2 paths through the pipe P601 and the pipe P202, and is returned to the auxiliary pump front cavity V6 through the openings N6 and N61 respectively to absorb the heat, and V6 is the space occupied by the fluid entering the auxiliary pump front cavity through the opening N6 and having a volume equal to that of L1 × S ×, fig. 3 shows the flow direction of the fluid, and a portion of the fluid after leaving the opening N × moves to the left side along the return of the auxiliary pump main cavity plug × (i.e., a portion of the gap N moves to the right side of the opening N × (i.e., the gap is equal to the left side of the virtual space of the opening × in the front opening N ×, and thus the virtual space of the front opening N × in the condition that the front opening N × and the virtual space of the front opening N × is formed under the virtual space of the front opening ×.

Fig. 6 is a schematic structural view showing a plunger stroke end state of the reciprocating plunger assembly of the first embodiment of the reciprocating plunger assembly of the reciprocating pump with a heat conductive built in the front stage of the plunger assembly according to the present invention.

Fig. 7 is a detail view of the front end structure of the plunger assembly of fig. 6.

As shown in fig. 6, regarding the flow path of the heat transfer liquid during the plunger process, under the suction of the low pressure region formed after the movement of the auxiliary pump main cavity plug ZQS (or under the pushing of the higher pressure of the liquid suction and discharge cavity V6 of the auxiliary pump front dynamic cavity), the liquid in the heat transfer device HX after being cooled down enters the liquid suction and discharge cavity V1 of the auxiliary pump internal dynamic cavity through the opening N1 to absorb heat (the volume increases along with the temperature rise), and moves to the right along with the auxiliary pump main cavity plug ZQS; meanwhile, the heat transfer liquid (heat absorption heat transfer liquid) in the area on the left side of the opening N6 in the liquid suction and discharge cavity V6 of the auxiliary pump front driving cavity moves to the right and enters the heat exchanger HX through the opening N6, and the liquid (heat absorption liquid) in the area on the right side of the opening N6 in the liquid suction and discharge cavity V6 of the auxiliary pump front driving cavity moves to the left under the pushing of the medium pressure of the main pump cylinder and enters the heat exchanger HX through the opening N6 to release the heat absorbed by V6 (the volume is reduced along with the temperature reduction). Thus, at the end of the plunger stroke, the right (front) interface of the virtual V6, which is theoretically located at the inner port of the opening N6 on the plunger casing, i.e., all V6, has the heat transfer fluid discharged from V6. As shown in fig. 6, the volume of the heat transfer liquid that is discharged from the V6 space through the opening N6 into the heat exchanger HX is reduced during the cooling process in the heat exchanger HX.

As shown in fig. 6, when the plunger 111 is advanced, the gap space between the auxiliary pump main chamber plug ZQS and the opening N6 becomes a semi-stagnant zone of the auxiliary pump front chamber.

As shown in fig. 6, when the stroke of the plunger 111 is terminated, the volume of the liquid suction and discharge chamber V6 of the auxiliary pump forward chamber is theoretically zero, that is, the heat transfer liquid in the liquid suction and discharge chamber V6 of the auxiliary pump forward chamber is completely discharged V6 through the opening N6 to the heat exchanger HX.

Fig. 8 is a schematic structural view of a plunger return end state of the reciprocating plunger assembly of the 2 nd technical means of the reciprocating plunger assembly of the heat-conducting reciprocating pump with a built-in front section of the plunger assembly of the present invention.

Fig. 9 is a detail view of the forward end of the plunger assembly of fig. 8.

In the 2 nd solution of the reciprocating plunger assembly of the heat-conducting reciprocating pump with the built-in front plunger assembly section of the invention shown in fig. 8, the main difference from the solution of the plunger assembly shown in fig. 3 is that: the auxiliary pump follow-up cavity has the advantages that the follow-up cavity plug AQS is additionally arranged, the auxiliary pump follow-up cavity which is constant in volume and cavity area and exists between the auxiliary pump main cavity plug ZQS and the auxiliary pump follow-up cavity plug AQS (also called as an auxiliary pump auxiliary cavity plug) is additionally arranged, and the auxiliary pump follow-up cavity generally has heat conduction capability and can also be called as an auxiliary pump follow-up heat conduction cavity; the follow-up heat conducting cavity is used as a continuous heat conducting section in series connection, so that the heat conducting area can be increased.

As shown in fig. 8, in the functional spatial relationship between the following heat conduction cavity and other auxiliary pump cavities (auxiliary pump cavity and auxiliary pump front cavity), it is equivalent to insert a "following heat conduction cavity" functional unit at the right side of the auxiliary pump main cavity plug ZQS in fig. 3, or to insert a "following heat conduction cavity" functional unit before the auxiliary pump front cavity, so that the following heat conduction cavity naturally has the function of a communication channel, and the spatial series relationship between the auxiliary pump cavity, the following heat conduction cavity and the auxiliary pump front cavity is formed.

As shown in fig. 8, the functional space relationship between the servo heat-conducting cavity and the auxiliary pump cavity can also be explained as the functional improvement of a cavity plug body of AN auxiliary pump cavity plug QS with a longer width, which is equivalent to that AN annular cylindrical groove is dug on the side wall of the cavity plug body of the auxiliary pump cavity plug QS, then a class 2 interface AN1, AN11, AN2 and AN21 are arranged on the side surface of a plunger box corresponding to the groove, the interfaces AN1 and AN11 are communicated with the inner cavity of the auxiliary pump, and the interfaces AN2 and AN21 are communicated with the front cavity of the auxiliary pump, and obviously, the servo heat-conducting cavity space between the 2 interfaces AN1 and AN2 is a heat-conducting liquid flow channel, so that the main cavity plug ZQS of the auxiliary pump and the auxiliary cavity plug AQS of the auxiliary pump can be regarded as a cavity plug group with the flow channel.

As shown in FIG. 8, opening AN1 is located between opening N1 and opening AN2, and opening AN2 is located between opening AN1 and the main cylinder. As shown in FIG. 8, opening AN11 is located between opening N11 and opening AN21, and opening AN21 is located between opening AN11 and the main cylinder.

Based on fig. 8, at least a part of the space between the openings AN1, AN2 of the auxiliary pump follower chamber can be filled with the heat transfer liquid.

Based on fig. 8, a part of the space between the openings AN1, AN2 of the auxiliary pump follower chamber, which is occupied by the heat transfer liquid repeatedly, is referred to as a suction and discharge liquid chamber AV of the auxiliary pump follower chamber.

As shown in fig. 8, the auxiliary pump follower cavity is 1 flow channel first, and the material flowing to and from the auxiliary pump follower cavity and the auxiliary pump inner cavity flows through the openings N1 (and N11), HX, AN1 (and AN 11).

As shown in fig. 8, the auxiliary pump following cavity is 1 flow channel first, and the material flowing to and from the auxiliary pump following cavity and the auxiliary pump front cavity flows through the opening AN2 (and AN21), the AHX1 (and AHX2) and the opening N6 (and N61).

As shown in fig. 8, AN auxiliary pump auxiliary cavity plug AQS is disposed in the plunger section of the auxiliary pump follow-up cavity between AN2 (and AN21) and the opening N6 (and N61), and during the movement of the auxiliary pump auxiliary cavity plug AQS, the heat-conducting liquid in the auxiliary pump follow-up cavity moves and contacts with the inner surface of the static plunger front sleeve to exchange heat.

As shown in fig. 8, during the return stroke of the plunger 111, the heat transfer liquid in the liquid suction and discharge chamber V1 of the dynamic chamber in the auxiliary pump is pushed by the auxiliary pump main chamber plug ZQS to be discharged from the V1 through the opening N1 (and N11), and enters the heat exchanger HX through the pipe P108 to release heat after being merged by the pipe P101 and the pipe P102; meanwhile, the cooled heat-conducting liquid discharged by the heat exchanger HX is conveyed through a pipeline PA108, and is respectively returned to the auxiliary pump follow-up cavity through openings AN1 and AN11 to absorb heat through 2 pipelines PA101 and PA 102; meanwhile, the heat-conducting liquid between the opening AN1 (AN 11) and the opening AN2 (AN 21) of the auxiliary pump follow-up cavity moves towards the right side; meanwhile, the heat-conducting liquid in the auxiliary pump follow-up cavity is discharged through AN opening AN2 (and AN21) and then enters a heat exchanger AHX1 (and AHX2) for heat exchange, and the heat-conducting liquid discharged from the heat exchanger AHX1 (and AHX2) after temperature reduction enters AN auxiliary pump front cavity through AN opening N6 (and N61) for heat exchange.

In the plunger assembly shown in fig. 8, when the return stroke of the plunger 111 is terminated, the clearance space between the auxiliary pump auxiliary chamber plug AQS and the opening AN2 (and AN21) forms a semi-stagnant area of the auxiliary pump follower chamber close to the auxiliary pump auxiliary chamber plug AQS, which is referred to herein as AN auxiliary stagnant area of the auxiliary pump follower chamber, and which is substantially stationary with respect to the auxiliary pump auxiliary chamber plug AQS and the auxiliary pump plunger.

In the plunger assembly shown in fig. 8, when the plunger 111 is stopped to return, the hot heat transfer fluid in the suction/discharge chamber AV of the auxiliary pump follower chamber is at least partially discharged to the heat exchanger AHX through the opening AN2 (and AN 21).

In the plunger assembly shown in fig. 8, during the process of the plunger 111, the heat transfer fluid in the front chamber of the auxiliary pump is discharged from the front chamber of the auxiliary pump through the opening N6 (and N61) and enters the heat exchanger AHX1 (and AHX2) for heat exchange; meanwhile, the cooled heat-conducting liquid discharged by the heat transmitter AHX1 (and AHX2) enters the auxiliary pump follow-up cavity through AN opening AN2 (and AN21) for heat exchange; meanwhile, the heat-conducting liquid between the opening AN1 (AN 11) and the opening AN2 (AN 21) of the auxiliary pump follow-up cavity moves towards the left side; meanwhile, the heat-conducting liquid in the auxiliary pump follow-up cavity is discharged through AN1 (and AN11), and enters a heat exchanger HX through a pipeline PA108 to release heat after being converged through a pipeline PA101 and a pipeline PA 102; meanwhile, the cooled heat-conducting liquid discharged by the heat exchanger HX is conveyed through a pipeline P108, and is returned to the dynamic cavity in the auxiliary pump through openings N1 and N11 respectively in 2 paths through a pipeline P101 and a pipeline P102 to absorb heat.

As shown in the plunger assembly of fig. 8, when the travel of the plunger 111 is terminated, the interstitial space between the auxiliary pump main plunger ZQS and the opening AN1 (and AN11) forms a semi-stagnant zone of the auxiliary pump follower chamber adjacent to the main plunger ZQS, referred to herein as the main stagnant zone of the auxiliary pump follower chamber, which is substantially stationary with respect to the main plunger ZQS and the auxiliary pump plunger.

In the plunger assembly shown in fig. 8, when the plunger 111 is stopped, the hot heat transfer fluid in the suction/discharge chamber AV of the auxiliary pump follower chamber is discharged at least partially through the opening AN1 (and AN11) to the heat exchanger HX.

As shown in fig. 8, since the volume of the heat transfer fluid in the area between the opening AN1 (and AN11) and the opening AN2 (and AN21) does not change, but flows back and forth with the back and forth movement of the plunger 111, it is a heat transfer fluid channel connecting the inner cavity of the auxiliary pump chamber plug set and the front cavity of the auxiliary pump chamber plug set.

As shown in fig. 8, when ZQS and AQS of the cavity plug group of the auxiliary pump act, three functions are formed for liquid suction and drainage of the cavity plug group inner cavity of the auxiliary pump, the auxiliary pump follow-up cavity and the auxiliary pump cavity plug group front cavity, the cavity plug group inner cavity of the auxiliary pump and the front cavity of the auxiliary pump cavity plug group are synchronous working cavities in time sequence, but liquid feeding and drainage actions are opposite, that is, liquid feeding of the cavity plug group front cavity of the auxiliary pump is performed when liquid is discharged from the cavity plug group inner cavity of the auxiliary pump, liquid feeding of the cavity plug group inner cavity of the auxiliary pump is performed when liquid is discharged from the cavity plug group front cavity of the auxiliary pump, and three cavities of the cavity plug group inner cavity of the auxiliary pump, the auxiliary pump follow-up cavity and the front cavity of the.

The auxiliary detention area of the auxiliary pump follow-up cavity and the main detention area of the auxiliary pump follow-up cavity are dynamic relative to the plunger function of the auxiliary pump area, belong to a semi-detention area and have a certain heat conduction function.

As shown in fig. 8, the volume of the gap section 900 may be any suitable value, and is generally capable of being filled and fully contacted by the heat transfer fluid discharged from the heat exchangers HX, AHX1 and AHX2, and is generally in the range of 0.9 to 2 times, preferably 0.5 to 1 times, the one-way liquid discharge amount L1 × S1 of the auxiliary pump intrinsic volume chamber V1.

In the plunger assembly shown in fig. 8, the liquid in the gap section 900 between the opening AN1 (and AN11) and the opening AN2 (and AN21) is in a flowing state during any stroke of the plunger, the gap section 900 is preferably completely replaced by the heat transfer liquid from the heat transfer devices HX and AHX and completely participates in heat exchange, and the volume of the gap section 900 is usually not more than 2 times of the single-pass liquid discharge amount L1 × S1 of the auxiliary pump intrinsic volume chamber V1.

In the plunger assembly shown in fig. 8, when the volume of the gap section 900 is 2 times of the one-way liquid discharge amount L1 × S1 of the auxiliary pump intrinsic volume chamber V1, the cold heat transfer liquid is fed from AN2 (and AN21) during 1 stroke of the plunger 111 to cool 50% of the AV wall surface on the right side of the gap section 900, and the cold heat transfer liquid is fed from AN1 (and AN11) during 1 return stroke of the plunger 111 to cool 50% of the AV wall surface on the left side of the gap section 900, according to the scheme, the effective heat exchange area provided by the gap section 900 is the largest, and although 1 plunger stroke can only replace 50% of the AV wall surface, in the long term, all AV chamber walls can be cooled.

As shown in fig. 8, the volume of the gap section 900 may be no more than 1 times of the one-way discharge capacity L1 × S1 of the auxiliary pump intrinsic volume chamber V1, so that the heat transfer fluid in the gap section 900 can be replaced by 100% for any 1 plunger stroke.

Fig. 10 is a schematic structural view showing a plunger return end state of the reciprocating plunger assembly of the 3 rd embodiment of the reciprocating plunger assembly of the reciprocating pump with a heat conductive built in the front stage of the plunger assembly according to the present invention.

In the 3 rd technical scheme of the reciprocating plunger assembly of the heat-conducting reciprocating pump with the built-in front plunger assembly section of the invention shown in the figure 10, the main difference with the technical scheme of the plunger assembly shown in the figure 9 is that: the internal structure of the right side (the side close to the main cylinder) of a plunger front sleeve 119 (namely, the front section of the plunger function) shown in fig. 9 is changed, the plunger front sleeve 119 is in a structure with unequal inner diameters, and the inner diameter of the left section of the plunger front sleeve 119 is large and the inner diameter of the right section of the plunger front sleeve 119 is small (a necking section 10007 is arranged on the structure); during the assembly of the plunger assembly, the plunger 111 can be inserted into the plunger front sleeve 119 only from the left side of the plunger front sleeve 119, or the plunger front sleeve 119 can be inserted into the plunger 111 only from the right side; the scheme has the effects of reducing the space volume of the plunger front sleeve 119 close to the end of the main liquid cylinder as much as possible, reducing the quantity of possibly existing media from the main liquid cylinder, and reducing the possibility or the pollution degree of heat-conducting liquid in a heat-conducting gap of the built-in heat-conducting reciprocating pump, which is polluted by the main media from the main liquid cylinder.

Fig. 11 is a schematic structural diagram of a plunger return end state of the reciprocating plunger assembly of the 4 th technical solution of the reciprocating plunger assembly of the heat-conducting reciprocating pump with a built-in front section of the plunger assembly of the present invention.

In the 4 th technical solution of the reciprocating plunger assembly of the heat-conducting reciprocating pump with the built-in front plunger assembly section of the invention shown in fig. 11, the main difference from the technical solution of the plunger assembly shown in fig. 9 is that: the internal structure of the left side (the side away from the main cylinder) of the plunger front sleeve 119 (i.e. the front section of the plunger function) shown in fig. 9 is changed, the plunger front sleeve 119 is of a structure with unequal inner diameters, the inner diameter of the left section of the plunger front sleeve 119 is small (a necking section 10003 exists in the structure), and the inner diameter of the right section is small; during the assembly of the plunger assembly, the plunger 111 can be inserted into the plunger front sleeve 119 from the right side only, or the plunger front sleeve 119 can be inserted into the plunger 111 from the left side only; the effect of this scheme is, the space volume that the one side was kept away from main hydraulic cylinder to minimize plunger front cover 119 does benefit to the entity thickness that reduces the joint portion of stuffing box 115 and plunger front cover 119, and the installation of being convenient for does benefit to and reduces plunger box weight. In fact, the structure of the stuffing box 115, the first pass of stuffing R100 and the left end (far from the main cylinder section) part of the plunger front sleeve 119 in fig. 11 can be completely the same as the structure of the stuffing box 115, the first pass of stuffing R100 and the left end (far from the main cylinder section) part of the plunger front sleeve 119 in fig. 1, so that the changes caused by the invention are only limited to the front section (near the main cylinder section) of the plunger front sleeve 119 and the front section of the main plunger.

In the structural schematic diagram of the 1 st technical solution of the present invention shown in fig. 3, a through-type gap QSJX exists between the auxiliary pump main cavity plug ZQS at the front section of the plunger 111 and the plunger front sleeve 119, so that it allows a small flow DR9 to exist for short-circuit flow of liquid between the auxiliary pump inner cavity and the auxiliary pump front cavity through the gap QSJX, in order to ensure that the heat transfer liquid of the auxiliary pump inner cavity mainly flows through the liquid driver HX, the width and length of the gap QSJX should be precisely set to ensure the flow-blocking capability of the gap QSJX, generally, during a single-pass movement of the plunger 111, the cumulative flow of the heat transfer liquid entering and exiting the auxiliary pump inner cavity through the openings N1 and N11 is marked as R16, and the flow-blocking coefficient K100 is (R16)/(DR9), the flow-blocking coefficient K100 is larger, the flow-blocking effect is better, but the requirements on the flow-blocking accuracy; the flow-blocking coefficient K100 is usually greater than or equal to 10, generally greater than or equal to 30, preferably greater than or equal to 50.

In the structure diagram of the 1 st technical solution of the present invention shown in fig. 3, a non-contact gap QSJX is formed between the auxiliary pump main cavity plug ZQS at the front section of the plunger 111 and the plunger front sleeve 119, because absolute isolation is not required between the auxiliary pump inner cavity and the auxiliary pump front cavity, a small amount of liquid leakage can be realized, and the structure is relatively simple and convenient to manufacture and assemble.

In the structure diagram of the first technical solution of the present invention shown in fig. 3, a non-contact gap QSJX is formed between the auxiliary pump main cavity plug ZQS at the front section of the plunger 111 and the plunger front sleeve 119, and a filler may be used in combination to serve as the filler outer edge ZQS-T L WY of the auxiliary pump main cavity plug ZQS, so that the sliding frictional contact relationship between the filler outer edge ZQS-T L WY of the auxiliary pump main cavity plug and the inner wall of the plunger front sleeve 119 is formed in the gap QSJX, but the structure is relatively complex and the manufacturing and assembling difficulty is relatively high.

The invention refers to the filler for isolating the inner cavity of the auxiliary pump and the front cavity of the auxiliary pump as the auxiliary pump cavity separating filler.

Fig. 12 is a schematic structural view showing a plunger return end state of the reciprocating plunger assembly of the 5 th embodiment of the reciprocating plunger assembly of the reciprocating pump with a heat conductive built in the front stage of the plunger assembly according to the present invention.

Fig. 13 is a detailed structural view of the auxiliary pump main cavity plug ZQS of fig. 12.

In the 5 th technical scheme of the reciprocating plunger assembly of the heat-conducting reciprocating pump with the built-in front plunger assembly section of the invention shown in the figure 12, the main difference from the technical scheme of the plunger assembly shown in the figure 5 is that the structure of the auxiliary pump main cavity plug ZQS shown in the figure 5 is changed, the filler outer edge ZQS-T L WY of the auxiliary pump main cavity plug ZQS is formed by combining the filler, and the sliding friction contact relation between the filler outer edge ZQS-T L WY of the auxiliary pump main cavity plug ZQS and the inner wall of the plunger front sleeve 119 is realized, so that the short-circuit flow between the auxiliary pump inner cavity and the auxiliary pump front cavity is almost not generated, namely the flow DR9 is basically zero.

The auxiliary pump main chamber plug ZQS, as shown in fig. 12, is comprised of the following:

① ZQS11 is a boss of the auxiliary pump main cavity plug ZQS integral with the plunger 111 for supporting the inboard backing ring ZQS 12;

② ZQS12 is an inner backing ring for supporting packing ring ZQS 13;

③ ZQS13 is a packing ring, which can be composed of 1 layer or 2 or more layers of packing ring, ZQS13 in FIG. 12 is composed of 1 layer of packing ring;

④ ZQS14 is an outer backing ring for transmitting pressure that compresses the support packing ring ZQS 13;

⑤ ZQS15 is an outer annular gland, which can be fixed ZQS15 on the plunger 111 by a set screw or a set pin, or ZQS15 can be fixed on the plunger 111 by a screw fit, for example, a female screw is processed on the inner side of the outer annular gland ZQS15, a matched male screw section is processed on the outer side of the corresponding section of the plunger 111 where the outer annular gland ZQS15 is installed, the outer annular gland ZQS15 is rotatably sleeved on the male screw section of the plunger 111 during installation, and finally ZQS15 is fixed on the plunger 111 by a set screw or a set pin.

Fig. 14 is a schematic structural view showing a plunger return end state of the reciprocating plunger assembly of the 6 th embodiment of the reciprocating plunger assembly of the reciprocating pump with a heat conductive built in the front stage of the plunger assembly according to the present invention.

Fig. 15 is a detailed structural view of the auxiliary pump main chamber plug ZQS of fig. 14.

In the 6 th technical solution of the reciprocating plunger assembly of the heat-conducting reciprocating pump built in the front section of the plunger assembly of the invention shown in fig. 14, the main difference from the technical solution of the plunger assembly shown in fig. 5 is that the structures of the auxiliary pump main cavity plug ZQS and the plunger front sleeve 119 shown in fig. 5 are changed, and the embedded short-circuit-proof filler ring assemblies ZQS-FD L T L of the plunger front sleeve 119 are combined and used with fillers, so that the sliding friction contact relationship between the auxiliary pump main cavity plug ZQS and the embedded short-circuit-proof filler ring assemblies ZQS-FD L T L of the plunger front sleeve 119 is realized, and the short-circuit flow between the auxiliary pump inner cavity and the auxiliary pump front cavity is hardly generated, namely the flow DR9 is basically zero.

The internally-embedded anti-short-circuit filler ring assembly ZQS-FD L T L of plunger front sleeve 119 shown in FIG. 14 is composed of the following parts:

① ZQS21 is an inner backing ring for supporting packing ring ZQS 22;

② ZQS22 is a packing ring, which can be composed of 1 layer or 2 or more layers of packing ring, ZQS22 in FIG. 14 is composed of 1 layer of packing ring;

③ ZQS23 is an outer backing ring for transmitting pressure that compresses the support packing ring ZQS 22;

④ ZQS24 is an external elastic gland, which can be ring-shaped disc spring or corrugated ring plate, and has certain elastic deformation ability to generate expected pressing force to the external pad ring ZQS23, and its shape can be elastically changed and can be completely restored to meet the requirements of installation and disassembly.

As shown in FIG. 3, the filler rim ZQS-T L WY of the auxiliary pump main cavity plug ZQS is required to be fixed on the metal body of the auxiliary pump main cavity plug ZQS to reciprocate with the plunger 111, and the structure of the filler rim ZQS-T L WY can be designed, manufactured and assembled simply because the pressure difference between the two sides of the filler rim ZQS-T L WY is small.

As shown in fig. 3, it should be noted that the packing outer rim ZQS-T L WY is a part of the cavity plug QS, and it does not belong to the plunger seal packing, because the auxiliary pump inner cavity, the auxiliary pump front cavity and the auxiliary pump following cavity which may be used are communicated together through the heat transmitter to form a communicating device, and a sealing relation for separating liquid from the auxiliary pump inner cavity and the auxiliary pump front cavity cannot be formed.

In the structure diagram of the 1 st technical solution of the present invention shown in fig. 3, the plunger 111 and the auxiliary pump main cavity plug ZQS are an integrated structure, and the plunger 111 and the auxiliary pump main cavity plug ZQS may be a combination of 2 or more structural members as required. For example, the auxiliary pump main cavity plug ZQS can be a solid ring ZQS-HJ composed of 2 or more parts and assembled on the main body of the plunger 111, the solid ring ZQS-HJ is embedded in the annular groove of the main body of the plunger 111 and fixed by a fastener, and the auxiliary pump main cavity plug ZQS with the structure can be randomly replaced or adjusted in shape.

In the structure schematic diagram of the 1 st technical scheme of the invention shown in fig. 3, a heat transmitter HX is arranged to perform time-sharing heat exchange on the heat-conducting liquid discharged from V1 and V6; of course, one heat transfer device HX1 can be arranged to exchange heat with the heat-conducting liquid in the auxiliary pump intrinsic volume chamber V1 only, and the other heat transfer device HX2 can be arranged to exchange heat with the heat-conducting liquid in the auxiliary pump main heat exchange chamber only, but a shared heat transfer device HX is proposed to exchange heat with the heat-conducting liquid discharged from the auxiliary pump intrinsic volume chambers V1 and V6 in a time-sharing mode, so that the total area and the occupied space volume of the heat transfer devices can be reduced.

In the structure diagram of the invention 1 shown in fig. 3, a packing for supporting the plunger may be provided between the front section of the plunger and the main cylinder, but the packing for supporting the plunger 111 is not a sealing packing for the plunger 111 because a liquid material flow passage is necessarily left.

In the structural schematic diagram of the 1 st technical solution of the present invention shown in fig. 3, one plunger assembly is provided with one heat transfer device HX, and for a multi-plunger reciprocating pump with the number of plungers PY, the heat transfer components HX of a plurality of plungers can be individually arranged or jointly arranged to reduce the number of heat transfer devices and save the occupied space.

The plunger assembly U100 of the present invention shown in fig. 3, 6, 8, 10, 11, 12 and 14 can be used to replace the plunger assembly of the plunger reciprocating pump shown in fig. 1, thereby forming a plunger reciprocating pump with a novel structure; in fig. 3, 6, 8, 10 and 11, except for the components of the plunger assembly of the present invention, the functions and structures of other components not shown are the same as or similar to those of the components shown in fig. 1, and of course, the relative positions of the components may need to be adjusted, which are within the conventional and well-known technologies.

The components or assemblies shown in figures 3, 6, 8, 10, 11, 12, 14 may be replaced by any other functionally equivalent structural element of any suitable form.

The specific mode of carrying out the invention can be any suitable mode and is not limited by the specific mode shown in the drawings; the individual functions shown in the figures may be combined with each other in a number of suitable arrangements.

The plunger assembly of the present invention, together with other functional components, may be formed as an integrated assembly.

The plunger 111 of the present invention, typically made of a corrosion-resistant, abrasion-resistant material, may be coated with an abrasion-resistant coating to extend its life.

The primary hydraulic cylinder used in conjunction with the plunger assembly of the present invention may be of any suitable construction.

The invention can be combined with other technical schemes for use, for example, the following patent applications can be combined for use to form a plunger reciprocating pump with complete functions:

① application No. 201811205520.0 patent application entitled "plunger reciprocating Pump";

② application No. 201811297707.8 patent application for plunger type reciprocating pump with heat insulation region between main liquid flow space in pump cylinder and pump cylinder;

③ patent application No. 201811373823.3 for invention, plunger stuffing box with 1 packing reciprocating seal at each end and plunger reciprocating pump;

④ application No. 201811374088.8 patent application for "plunger reciprocating seal with three packing seals and its plunger reciprocating pump";

⑤ application No. 201811374087.3 for "three-way packing type reciprocating seal with pressurized middle flushing cavity and its reciprocating pump";

⑥ application No. 201811403601.1 patent application for "plunger reciprocating seal and its reciprocating pump using four packing seals";

⑦ application No. 201811403055.1 entitled "plunger reciprocating seal with diamond coating on plunger face contacted by high pressure packing".

Compared with the traditional plunger assembly technical scheme without a built-in heat conduction reciprocating pump, the reciprocating plunger assembly with the built-in heat conduction reciprocating pump at the front section has the structural advantages that:

① the system or structure is simple, easy to design, manufacture and maintain, low investment, low energy consumption, and little influence on the dynamic balance of plunger pump;

②, the temperature difference DT can be flexibly controlled, the operation temperature of the 1 st main seal is reduced, the lubricating effect of the 1 st main seal is improved, the service life of the 1 st main seal is prolonged, and the outward leakage probability of the outer side end of the stuffing box is reduced;

③ the probability of contamination of the plunger housing with the primary hydraulic medium is reduced;

④ may increase the main cylinder operating temperature range;

⑤, the high-pressure flushing liquid consumption is reduced, and the volume efficiency of the plunger pump is improved;

⑥ it is beneficial to prolong the operation period of the plunger assembly, reduce the frequency of maintenance or part replacement and improve the operation rate of the equipment.

Detailed Description

The present invention is described in detail below.

The pressure in the present invention refers to absolute pressure.

The concentrations of the components described in the present invention, when not particularly specified, are weight concentrations, i.e., mass concentrations.

The solid-containing liquid material refers to a liquid material containing solid particles, such as raw material coal oil slurry in a coal hydrogenation direct liquefaction reaction process.

The invention relates to a plunger type reciprocating pump.A hydraulic end comprises a main hydraulic cylinder for sucking and discharging liquid materials and a plunger box matched with a plunger to do reciprocating motion; the plunger can be composed of a single part, or can be an assembly of 2 or more parts; the plunger gland assembly may include a plunger gland that uses a plunger seal packing and a plunger barrel that does not use a plunger seal packing.

The plunger type reciprocating pump is usually used for conveying high-temperature liquid or low-temperature liquid, is used for conveying slurry containing solid particles or/and liquid materials containing corrosive components or/and liquid materials containing explosive components or/and liquid materials containing toxic components or/and liquid materials containing radioactive components, and is used for medium-high pressure difference normal-temperature coal slurry pumps, medium-high pressure difference medium-temperature coal slurry pumps, medium-high pressure difference high-temperature coal slurry pumps and medium-high pressure difference high-temperature flushing oil pumps which are used in coal hydrogenation direct liquefaction devices, and the normal discharge pressure of the plunger type reciprocating pump is usually medium-high pressure (the pressure is 2.0-25.0 MPa).

The invention relates to a pumping target liquid material or a main medium of a main liquid cylinder, which refers to a process material conveyed by a plunger type reciprocating pump, and is different from a main body pumping material of injection liquid (sealing liquid and flushing liquid) of a plunger assembly, such as coal oil slurry conveyed by the plunger type reciprocating pump for conveying the coal oil slurry.

The invention relates to a plunger type reciprocating pump for conveying solid-containing slurry, which is typically applied to a plunger type reciprocating pump for conveying oil-coal slurry, wherein an isolating liquid or an isolating flushing liquid is used in a working mode, the isolating liquid can be injected for a long time or injected discontinuously for discharging or injected continuously for discharging, the discharged isolating flushing liquid can finally enter a pump cavity of a pump body and is discharged out of the pump cavity along with a pumping target liquid material, so as to prevent harmful substances (low-temperature liquid materials, high-temperature liquid, solid slurry, corrosive or explosive or toxic or radioactive components and the like) from entering a sealing packing (sealing filler) part of a plunger, or prevent high-temperature media or low-temperature media from entering the plunger box and contacting the plunger to cause the over-limit thermal deformation or cold deformation of the plunger box, or prevent solid particles from entering the sealing packing (sealing filler) part of the plunger to cause the intensified abrasion of the packing, or prevent corrosive medium from entering the plunger case to contact the plunger and generate corrosion, or prevent harmful component medium from entering the rear section of the plunger case to leak into the environment or contact human body. The working mode of the spacer fluid of the invention is usually intermittent injection and intermittent discharge or continuous injection and continuous discharge.

The working mode of the spacer fluid can be a working mode of continuous injection and continuous discharge, namely a working mode of full flushing of all strokes, for example, the working scheme of full flushing of all strokes for setting the spacer fluid during conveying the particle slurry in the prior art is adopted, the pressure of the flushing fluid is always higher than the pressure of a main hydraulic cylinder with the particle slurry, for example, 0.2-0.5 MPa, and the spacer fluid (flushing fluid) is added to the front end (one end close to the main hydraulic cylinder) of a high-pressure sealing box (a first plunger sealing filler close to the main hydraulic cylinder side) of a main pump plunger sealing box in all time periods of the strokes of sucking the particle slurry and discharging the particle slurry by the main pump, and the working mode has the following functions:

① preventing the particle slurry from entering the first plunger sealing box to destroy the sealing box, and preventing the particle slurry from entering the gap between the plunger and the plunger sleeve to abrade the surfaces of the plunger and the plunger sleeve;

② lubricating the sliding seal of the first plunger seal;

③ the first plunger seal is cooled.

The working mode of the isolation liquid full flushing in all strokes is a necessary injection step because the isolation liquid added can effectively play the roles of isolation, flushing, lubrication and cooling in the plunger return stroke (return stroke) (namely, in the liquid suction stroke of the main liquid cylinder); however, in the plunger forward stroke (stroke) (i.e., in the main cylinder drain stroke), the spacer fluid added does not have the above-described effective functions of spacing, flushing, lubricating, and cooling, and therefore, is an unnecessary injection step, resulting in a large spacer fluid flow rate. According to the working mode of the isolation liquid full-flushing in all strokes, generally, the flow of a prepared flushing liquid pump is 8-10% of the flow of a main pump, the pressure is controlled by adding a pore plate on a flushing pipeline, and if the flushing amount is less than 6%, the sealing failure of the pump is caused. Most particle slurry pumps do not limit the flushing amount, for example, the flow of chemical water slurry medium flushing liquid requires 8-10% of the flow of a main pump, and the flow of power plant ash coal slurry medium flushing liquid does not limit. The washing matching device in the prior art is simple, but the washing amount is large and is 8-10% of the flow of the main pump, so that the volumetric efficiency of the hydraulic cylinder is greatly reduced, and the washing matching device cannot be applied to certain processes requiring the limiting of the injected oil washing amount.

The working mode of the isolating liquid (isolating flushing liquid) can be a working mode of intermittent injection and intermittent discharge so as to reduce the flow of the isolating liquid, usually, a scheme of synchronously injecting the isolating liquid in a main pump plunger return stroke is adopted, when a main cylinder of a reciprocating plunger pump sucks slurry, the isolating liquid is injected into a plunger of a pump to move in a front space sealed by plunger packing in a1 st channel of a main pump, and when the main pump discharges the slurry, the isolating liquid is injected into the pump to move so as to suck the isolating liquid, the isolating liquid is not added into the plunger packing of the main pump in a sealing way, the isolating liquid amount can be reduced to be less than or equal to 3 percent of the flow of the main pump, when the working mode is applied to an oil-coal slurry pump of a direct coal hydrogenation liquefaction device, the using amount of the isolating liquid can be reduced, the load of the oil-coal slurry pump can be reduced, the increment of the device load (5 to 7 percent, has the effects of greatly reducing investment, reducing energy consumption and improving oil yield.

In order to reduce the consumption of the isolating liquid, the invention generally adopts a working method of injecting the isolating liquid synchronously with the return stroke of a main pump plunger, correspondingly configures an isolating liquid injection system (comprising a synchronous isolating liquid injection pump), and needs to arrange an isolating liquid injection interface on a plunger stuffing box assembly, namely a plunger stuffing box cylinder or/and a plunger sleeve, and the isolating liquid washes a plunger and flows into a flow channel or a flow channel cavity of a pump cavity.

The invention relates to a plunger type reciprocating pump for isolating a working medium by using an isolation liquid to a plunger stuffing box, and discloses a working method for injecting the isolation liquid synchronously with the return stroke of a plunger of a main pump, wherein when the plunger type reciprocating pump is applied to a three-plunger type reciprocating pump, three plungers of the main pump are hermetically matched with one three-plunger type isolation liquid injection pump, a plunger cylinder of each isolation liquid injection pump corresponds to one plunger seal of a slurry pump, two pumps adopt one shaft, and the crank throw phase difference between one plunger of the isolation liquid injection pump and a corresponding plunger crankshaft of the reciprocating pump is 180 degrees.

The plunger type reciprocating pump for conveying the oil coal slurry generally refers to a plunger type reciprocating pump for conveying the oil coal slurry by using an isolation liquid, and the structure of the plunger type reciprocating pump essentially belongs to an isolation type reciprocating pump; when the isolating liquid is continuously or regularly and discontinuously injected, the isolating liquid can be conveyed by using an isolating liquid injection reciprocating pump (such as a metering reciprocating pump) driven by a main driving machine (such as a main motor) and driven by a main pump power end, so that the coordination and consistency of actions can be ensured.

The normally working plunger type reciprocating pump set at least comprises a driving end (power end) and a hydraulic end, wherein the driving end possibly comprises a connected prime motor (which can be a motor, a variable frequency motor, a diesel engine, a hydraulic motor, a steam engine and the like), a coupler and a protective cover thereof, a speed changer, a gear box, a crankshaft, a connecting rod, a crosshead and a pull rod, and the hydraulic end can comprise a plunger working assembly (comprising a plunger, a stuffing box and a plunger front sleeve), a main hydraulic cylinder, a liquid inlet one-way valve, a liquid discharge one-way valve and a liquid guide pipe according to requirements.

The main objective of the present invention is to provide structural improvement to the front section of the plunger assembly, therefore, the main technical solution of the present invention is to provide the structure, assembly scheme, system working method, design principle of the front section of the plunger assembly, and to explain the operation scheme and operation effect.

The reciprocating plunger assembly and the reciprocating pump thereof with the heat-conducting reciprocating pump arranged in the front section of the plunger assembly are suitable for conveying high-temperature liquid or low-temperature liquid, and are suitable for conveying slurry containing solid particles or/and liquid materials containing corrosive components or/and liquid materials containing explosive components or/and liquid materials containing toxic components or/and liquid materials containing radioactive components, such as a high-pressure-difference medium-temperature coal slurry pump, a high-pressure-difference high-temperature coal slurry pump and a high-pressure-difference high-temperature flushing oil pump which are used in a direct coal hydrogenation liquefaction device.

The reciprocating plunger assembly with the heat-conducting reciprocating pump arranged in the front section of the plunger assembly and the reciprocating pump of the reciprocating plunger assembly can be used for a high-pressure-difference high-temperature pipeline used for a direct coal hydrogenation liquefaction device or a flushing oil pump used for flushing an instrument and a high-pressure-difference high-temperature coal slurry pump, and is particularly suitable for a high-pressure coal oil slurry feeding pump used in CT L in the direct coal hydrogenation liquefaction process.

The reciprocating plunger assembly of the heat-conducting reciprocating pump and the reciprocating pump thereof are arranged in the front section of the plunger assembly, and related pipeline systems can be provided with flow measuring elements such as a flowmeter and pressure measuring elements such as a pressure gauge.

In order to ensure the dynamic balance stability of the pump set and the stability of discharge flow, the reciprocating plunger assembly and the reciprocating pump of the heat-conducting reciprocating pump are arranged in the front section of the plunger assembly, and pump types such as 1 plunger, 3 plungers, 5 plungers and the like are usually selected according to the total flow of conveyed solid-containing liquid materials, and pump types such as 2 plungers, 4 plungers, 6 plungers and the like which are even number plungers are usually not selected. Therefore, the solid-containing liquid material reciprocating pump can be a single-plunger reciprocating pump, can be a multi-plunger reciprocating pump, and can select 3-plunger, 5-plunger, 7-plunger and other pump types.

The installation mode of the reciprocating pump formed by the reciprocating plunger assembly of the heat-conducting reciprocating pump arranged in the front section of the plunger assembly is used, the main liquid cylinder body or the pump cavity is usually arranged vertically, and the plunger rod and the plunger box are usually arranged horizontally.

The reciprocating plunger component of the heat-conducting reciprocating pump and the reciprocating pump thereof are arranged in the front section of the plunger component, and the driving equipment can be any suitable form of prime mover, such as an electric motor, a variable frequency motor, a steam turbine and the like, and the electric motor is usually selected; because the reciprocating frequency of the reciprocating pump is usually very low, when the driving system uses the motor, a gearbox or a speed changer is usually matched to be used so as to adapt to the requirement of the reciprocating pump on low reciprocating frequency; in order to increase the flexibility and the adjusting range of flow adjustment, a variable frequency motor can be used, a matched frequency converter is needed at the moment, and 2 sets of frequency converters (1 set for 1 device) can be prepared at the same time in order to improve the safety of a frequency conversion system.

According to the reciprocating plunger assembly with the heat-conducting reciprocating pump arranged in the front section of the plunger assembly and the reciprocating pump thereof, a flushing oil system of a chamber between plunger seals is usually arranged according to needs, wherein the flushing oil system of the chamber between an outer plunger seal and an outer plunger main seal is also called a sealing flushing oil system, and flushing oil or sealing flushing oil is injected into the chamber between the plunger seals to lubricate a contact surface between the seal and the plunger and take away solid particles (so as to prevent the solid particles from accumulating) possibly brought by a sealing filler.

According to the reciprocating plunger assembly with the heat-conducting reciprocating pump arranged in the front section of the plunger assembly and the reciprocating pump of the reciprocating plunger assembly, an isolating liquid injection system is usually arranged according to needs, and most or all of the isolating liquid finally enters a main hydraulic cylinder and is discharged out of the main hydraulic cylinder along with a pumped target liquid material; the spacer fluid is typically a solids-free cleaning fluid that is not detrimental to the operation of the process fluid, such as a cleaning fluid that is processed in conjunction with the process fluid.

The reciprocating plunger assembly with the heat-conducting reciprocating pump arranged in the front section of the plunger assembly and the reciprocating pump of the reciprocating plunger assembly can form a skid-mounted structure according to needs, are convenient to install and are beneficial to enhancing the dynamic stability.

The plunger packing seal material of the plunger assembly may be selected from any suitable material, such as a sealing material that is resistant to corrosion and abrasion by the components of the target fluid being pumped.

The material of the mating member (such as an elastic backing ring, a metal ring, a guide sleeve, etc., and the elastic backing ring may be a disc spring) of the high-pressure packing seal of the plunger assembly may be selected from any suitable material, such as a sealing material capable of resisting corrosion and abrasion of the pumping target liquid component, which is generally a steel material, and particularly may be an alloy material with a high heat transfer coefficient.

The plunger assembly can be any suitable structure in structural form, and the convenience of manufacturing, installation, overhauling and replacement is fully considered.

When the plunger assembly comprises the stuffing box and the plunger front sleeve, the plunger assembly and the plunger can be assembled from one side of the stuffing box in advance and then assembled from one side of the plunger front sleeve, or can be assembled from one side of the plunger front sleeve in advance and then assembled from one side of the stuffing box.

The plunger stuffing box assembly of the present invention may be combined with other parts.

The working mode of the spacer fluid of the plunger assembly can be one-time injection for long-term use, or intermittent injection and intermittent discharge or continuous injection and continuous discharge, and the spacer fluid can finally enter the pump cavity of the pump body and be discharged out of the pump cavity along with working media.

The working mode of flushing liquid in the cavity between the plunger seals of the plunger assembly can be a working mode of intermittent injection and intermittent discharge, and can be a working mode of continuous injection and continuous discharge.

Based on the plunger assembly with the characteristic structure, an improved plunger type reciprocating pump can be manufactured.

The normally working plunger type reciprocating pump set of the invention at least comprises a driving end and a hydraulic end, wherein the hydraulic end usually comprises a plunger assembly U100 (comprising a plunger and a plunger box), and the related technology which can be used for reference of the pump set of the invention is described below by combining the functional requirements and the structure of the plunger assembly U100.

The following describes the prior art of plunger type reciprocating pump and its system, and the structural features and the improved experience of these pump components are all the references of the reciprocating plunger assembly of the present invention and its non-characteristic part of the reciprocating pump with heat-conducting reciprocating pump in the front section of the plunger assembly.

The structural characteristics and the improvement of the feeding port collecting pipe in the production and use process of the coal slurry feeding pump SHFB of Shenhua Ordos coal oil separation company are described below. The working method of the U-shaped flow path of the coal slurry feeding pump SHFB of the Shenhua Ordos coal oil separation company and the discharged liquid of the separating liquid in the pump cavity.

China Shenhua Ordos coal oil preparation company has a unique commercial 100-million ton/year coal hydrogenation direct liquefaction device, a high-pressure oil coal slurry feeding pump is a high-pressure plunger type reciprocating pump, the structure and the function of the device are recorded on pages 232 to 233 of document A02 direct coal liquefaction process and engineering (published time 2015 year 02 month), the function of the device is to pressurize oil coal slurry containing 50 wt% of solid particles to about 20MPa, then the oil coal slurry enters a coal slurry heating furnace for heating, then the oil coal slurry enters a coal liquefaction reactor for hydrogenation reaction, the device is one of core devices of the coal liquefaction device, and the manufacturer is the Uraca URACA pump company of Germany.

Table 1 shows the main parameters of the coal slurry feed pump SHFB of the shenhua redes coal oil separation company.

TABLE 1 main parameters of SHFB for coal slurry feeding pump of Shenhua Ordos coal oil separation company

Item Principal parameters
Pump type 5 plunger horizontal pump P5-96
Flow (normal/maximum flow), m3/h 85.3/93.8
Suction pressure (maximum/minimum), MPa 0.458/0.41
Outlet pressure (max/min), MPa 20.11/20.04
Inlet-outlet pressure difference (maximum/minimum), MPa 19.63/19.58
Net suction head (NPSHQ), m 44
Working medium Coal oil slurry: 47.2 wt% solids +52.8 wt% liquids
Viscosity (Normal/minimum/maximum), Pa/s 0.034/0.013/0.081
Medium temperature (normal/maximum), deg.C 168.6/290
Pump speed (Normal/maximum), r/min 74/81
Linear speed of plunger (Normal/maximum), m/s 0.66/0.73
Stroke, mm 270
Diameter of plunger, mm 150
Plunger thrust, t 41
Main motor parameter 710KW,1500r/min

The coal slurry feeding pump SHFB is a horizontally arranged five-cylinder single-action fixed-displacement reciprocating plunger pump, and uses a reciprocating pump with 5 plunger pistons and 5 liquid suction and discharge cavities; the lower part of the liquid suction and discharge cavity is provided with a feeding one-way valve in the form of a ball valve and is connected with a feeding branch pipe and a feeding collecting pipe outside the pump body through a feeding interface; the upper part of the liquid suction and discharge cavity is provided with a ball valve type discharge one-way valve which is connected with a discharge branch pipe and a discharge collecting pipe outside the pump body through a discharge interface.

The coal slurry feeding pump SHFB mainly comprises a power end, a hydraulic end (comprising a plunger injection oil pump, a plunger flushing oil pump and an inlet/outlet voltage stabilizer), a control system (comprising a field instrument, a transmitter and a controller), and the like; the power end comprises a motor (comprising a VFD frequency converter) and a transmission chain (comprising a gear reducer and a coupling).

The coal slurry feeding pump SHFB of Shenhua Ordos coal oil separation company converts the rotation motion of a motor into the reciprocating motion of a crosshead and a plunger piston arranged on the crosshead. The power end comprises components such as a crankshaft/a main shaft bushing, a connecting rod/a crosshead and the like. The crankshaft has five cranks and is supported by four babbit metal bearing bushes.

The coal slurry feeding pump SHFB of Shenhua Ordos coal oil separation company, the hydraulic end includes the exit and entrance liquid discharge valve component, the packing and the plunger piston. The outlet and the inlet adopt ball valves, and the diameter of the ball is phi 140 mm. The plunger material is 2Cr13+ special coating. The plunger sealing box (stuffing box) adopts a structural form of synchronous injection, flushing and sealing, and the stuffing box is a double stuffing box of a metal throttling ring and a special PTFE (polytetrafluoroethylene) stuffing ring. The injection oil is injected into the high-pressure filler through a synchronously driven shaft head injection pump, the tail end filler (the filler box filler at the outermost side far away from the main hydraulic cylinder) is cooled and lubricated by adopting sealing oil, and the flushing oil is injected between the low-pressure filler and the high-pressure filler to play a role in lubricating and taking away solid particles possibly brought by the high-pressure filler.

The Shenhua Ordos coal oil separation company reforms the feeding expansion joint branch pipe of the main oil cylinder of the oil coal slurry from the upper part of the feeding collecting pipe (the arrangement scheme before reforming) into the feeding expansion joint branch pipe of the main oil cylinder of the oil coal slurry from the lower part of the feeding collecting pipe (the arrangement scheme after reforming) according to the operation experience of the coal slurry feeding pump SHFB in the production of the device, thereby basically eliminating the flowing dead zone of the coal slurry, basically eliminating the phenomenon of uneven abrasion of a suction inlet ball valve and a valve seat in operation, prolonging the service life of a pump and a pump inlet valve, improving the safety of the pump, reducing the maintenance cost, relating to the reasons of abrasion of the suction ball valve and the valve seat of the high-pressure reciprocating pump of the oil coal slurry caused by the leading-out scheme of the feeding expansion joint branch pipe of the pump cylinder from the upper part of the feeding collecting pipe before reforming, and a shallow coal liquefaction feeding ball valve suction abrasion and improvement measure published on pages 72 and 73 of the 11 th page of Negmeng petrochemical engineering 2013, a profile is given.

The application date is that chinese patent Z L201520443034.8 of 2015, 06 and 25 records other technical information including functional requirements and structures of plunger working components (including plungers, stuffing boxes and plunger front sleeves) besides plunger stuffing box components, which is information that can be used for reference or reference by the plunger reciprocating pump and the system thereof of the present invention.

The characteristic parts of the present invention are described below.

The invention discloses a reciprocating plunger assembly of a heat-conducting reciprocating pump arranged in the front section of the plunger assembly, which is characterized in that:

a reciprocating plunger assembly U100, at least comprising a plunger U110, a plunger housing U130, and a plunger seal U120 installed in the plunger housing;

the plunger U110 is placed in the inner cavity of the plunger U130 and used for reciprocating motion;

the end face of the plunger letter U130, which is in contact with the main hydraulic cylinder, is the front end face of the plunger letter U130, and the end face of the plunger letter U130, which is far away from the main hydraulic cylinder, is the rear end face of the plunger letter U130;

the reciprocating plunger assembly U100 at least uses 2 plunger seals, the plunger seal closest to the rear end face of the plunger box U130 is an outer plunger seal U129, the other plunger seals belong to plunger main seals, and the plunger main seal closest to the outer plunger seal U129 is also called as the outer plunger main seal;

when 2 or more plunger main seals are used in the reciprocating plunger assembly U100, the numbers are sequentially numbered from near to far according to the distance from the front end face of the plunger letter U130, the plunger main seal closest to the front end face of the plunger letter U130 is a1 st plunger main seal U121, and the other plunger main seals are a 2 nd plunger main seal U122, a 3 rd plunger main seal U123 and the like;

the part of the plunger letter U130 between the front end face of the plunger letter U130 and the 1 st plunger main seal U121 is called as the front section of the plunger letter U130;

the part of the plunger letter U130 between the rear end face of the plunger letter U130 and the main seal of the plunger at the outer side is called the rear section of the plunger letter U130;

when the reciprocating plunger assembly U100 uses 2 or more plunger main seals, the plunger letter U130 part between the 1 st plunger main seal U121 and the plunger main seal at the outer side is called the middle section of the plunger letter U130;

a plunger pocket U130 containing at least the plunger packing pocket fitted with or contacting the plunger seal U120 and possibly a plunger barrel not fitted with the plunger seal U120, the plunger barrel adjacent to the main cylinder being referred to as a plunger front barrel;

the reciprocating plunger assembly U100 is characterized by also comprising a built-in auxiliary heat exchange reciprocating PUMP 7PUMP (auxiliary PUMP);

the auxiliary pump is composed and works according to the following principle:

① plunger function U130 front section and reciprocating between the plunger U110 front section, constituting built-in auxiliary pump fluid chamber FQ, plunger U110 front section reciprocating through FQ position set up auxiliary pump fluid chamber plug QS which pushes auxiliary pump fluid chamber FQ fluid movement;

when the plunger U110 reciprocates, the auxiliary pump cavity plug QS is driven to reciprocate to push heat-conducting liquid in the auxiliary pump liquid cavity FQ to reciprocate, and the auxiliary pump cavity plug QS plays a role of a reciprocating pump plunger;

an auxiliary pump liquid cavity FQ is divided into an auxiliary pump inner cavity and an auxiliary pump front cavity by taking an auxiliary pump cavity plug QS as a boundary;

the part of an auxiliary pump liquid cavity FQ far away from the front end surface of the plunger piston U130 by taking an auxiliary pump cavity plug QS as a boundary is an auxiliary pump inner cavity,

the part of an auxiliary pump liquid cavity FQ close to the front end surface of the plunger U130 is an auxiliary pump front cavity by taking an auxiliary pump cavity plug QS as a boundary,

in the reciprocating process of the plunger U110, the liquid suction and discharge space of the inner cavity of the auxiliary pump is called as an inner dynamic cavity of the auxiliary pump, and the volume of the inner dynamic cavity of the auxiliary pump is a dynamic variable quantity;

in the reciprocating process of the plunger U110, the liquid suction and discharge space of the front cavity of the auxiliary pump is called as a front moving cavity of the auxiliary pump, and the volume of the front moving cavity of the auxiliary pump is a dynamic variable quantity;

the auxiliary pump inner cavity is communicated with the auxiliary pump front cavity through a channel and a heat transfer element HX, and the auxiliary pump inner cavity is communicated with the auxiliary pump front cavity through a communicating vessel;

②, the heat transfer element HX is used for receiving the heat-conducting liquid discharged from the auxiliary pump liquid cavity FQ, transferring heat to the heat-conducting liquid to change the temperature of the heat-conducting liquid, returning the heat-conducting liquid after the temperature change of the heat transfer to the auxiliary pump liquid cavity FQ, and heating the wall surface of the auxiliary pump liquid cavity FQ;

③ the heat-conducting liquid in the auxiliary pump fluid cavity FQ reciprocates along with the reciprocating motion of the auxiliary pump cavity plug QS, contacts with the wall of the auxiliary pump fluid cavity FQ to perform reciprocating flow contact heat conduction on the inner surface of the front section of the plunger U130 and the outer surface of the front section of the plunger, the wall of the auxiliary pump fluid cavity FQ is also a heat-conducting surface, and the auxiliary pump fluid cavity FQ is also called as an auxiliary pump heat-conducting cavity;

when the main plunger U110 moves forwards, the main plunger U110 moves forwards close to the main hydraulic cylinder, heat-conducting liquid is discharged from the front movable cavity of the auxiliary pump through the interface N6X and enters the heat transfer element HX, and the heat-conducting liquid with changed temperature discharged from the heat transfer element HX is used as forward cold flow to return to the inner movable cavity of the auxiliary pump through the interface N1X;

when the main plunger U110 makes a return movement, the main plunger U110 makes a return movement away from the main hydraulic cylinder, the heat-conducting liquid is discharged from the internal movable cavity of the auxiliary pump through the interface N1X and enters the heat transfer element HX, and the heat-conducting liquid with the temperature changed and discharged from the heat transfer element HX is returned to the front movable cavity of the auxiliary pump as a reverse cold flow through the interface N6X.

The invention, in general, is in the form of an auxiliary pump plug QS selected from 1 or a combination of several of the following:

① the outer side surface is a smooth cylinder;

②, a cylinder with 1 or 2 or more inner grooves is arranged outside;

③ cylindrical body with internal screw thread on its outer side;

④ is provided with a cylinder communicating the minute passages of the sub pump rear chamber and the sub pump front chamber.

In the invention, the inner cavity form of the front section of the plunger letter U110 is selected from 1 or a combination of several of the following types:

① equal diameter channels with the same inner diameter;

② the inner diameter of the side close to the main cylinder is smaller than that of the side far from the main cylinder;

③ is larger than the main cylinder on the side away from the main cylinder.

According to the invention, the heat transfer element HX is, in general, in the form of 1 or a combination of several selected from the group consisting of:

① independent of the heat transfer element of the plunger barrel;

② converge on the heat transfer element of the plunger barrel.

According to the invention, the heat transfer element HX is, in general, in the form of 1 or a combination of several selected from the group consisting of:

① the heat pipe is a smooth pipe, the guide vane liquid flows in the heat exchange pipe;

② the heat exchange tube is a screw tube, the guide vane liquid flows in the heat exchange tube, the inner side and/or outer side of the heat exchange tube is provided with screw thread;

③ the heat exchange tube is the finned tube, and guide vane liquid flows in the heat exchange tube, and the finned tube is arranged to the heat exchange tube inboard and/or the outside.

In the present invention, the heat transfer member HX is a heat transfer member independent of the plunger sleeve, and the relationship between the elevation of the center of the heat transfer member HX and the elevation of the center of the plunger housing U130 is selected from 1 of the following:

① are equal in height;

②, the central elevation of the heat transfer element HX is lower than the central elevation of the plunger letter U130;

③ the height of the center of the heat transfer element HX is higher than the height of the center of the plunger letter U130.

In the present invention, in general, the heat transfer member HX, and the heat transfer medium used for heat transfer with the heat transfer fluid are selected from 1 of the following:

① gas, possibly air;

② liquid, which may be water or oil;

③ gas-liquid mixture.

In the invention, in general, the ratio K700 of the volume infusion amount 7PUMP-RW of the built-in auxiliary heat exchange reciprocating PUMP 7PUMP to the volume infusion amount U100-RW of the main hydraulic cylinder driven by the reciprocating plunger assembly U100 is (7PUMP-RW)/(U100-RW), and K700 is selected from 1 of the following types:

① is less than 0.1;

②0.1~0.3;

③0.3~1.0;

④ is greater than 1.0.

According to the invention, generally, the cavity wall area of the front dynamic cavity of the auxiliary pump is K300 times of the cavity wall area of the internal dynamic cavity of the auxiliary pump, and K300 is selected from 1 of the following types:

①0.5~1.0;

②1.0~3.0;

③ is greater than 3.0.

In the invention, the reciprocating plunger assembly U100 can be provided with 2 plunger seals, and the functions of the reciprocating plunger assembly U are as follows:

① outside plunger seal, preventing the liquid in the space between 2 plunger seals from leaking to the outside environment;

② plunger primary seal, preventing leakage of primary cylinder media into the space between the 2 plunger seals.

In the invention, the reciprocating plunger assembly U100 can be provided with 3 plunger seals, and the functions of the reciprocating plunger assembly U are as follows:

① outside plunger seal, preventing the liquid in the space between the outside plunger seal and the outside plunger main seal from leaking to the outside environment;

② the 2 nd or outer plunger primary seal prevents liquid in the space between the 2 nd and 1 st plunger primary seals from leaking into the space between the outer and 2 nd plunger primary seals;

③ plunger primary seal 1, prevents leakage of primary cylinder media into the space between plunger primary seal 1 and plunger primary seal 2.

In the invention, the reciprocating plunger assembly U100 can be provided with 4 plunger seals, and the functions of the reciprocating plunger assembly U are as follows:

① outside plunger seal, preventing the liquid in the space between the outside plunger seal and the outside plunger main seal from leaking to the outside environment;

② the 3 rd plunger main seal, i.e. the outer plunger main seal, prevents the liquid in the space between the 3 rd plunger main seal and the 2 nd plunger main seal from leaking into the space between the outer plunger main seal and the 3 rd plunger main seal;

③ plunger primary seal 2, preventing liquid in the space between the plunger primary seal 2 and the plunger primary seal 1 from leaking into the space between the plunger primary seal 2 and the plunger primary seal 3;

④ plunger primary seal 1, prevents leakage of primary cylinder media into the space between plunger primary seal 1 and plunger primary seal 2.

The present invention, generally, a reciprocating plunger assembly U100, provides at least 2 plunger seals;

and the sealing liquid is continuously or discontinuously replaced in the gap between the outer plunger seal and the outer plunger main seal, so that the liquid material passing through the outer plunger main seal is prevented from polluting the outer plunger seal.

The present invention, generally, a reciprocating plunger assembly U100, provides at least 2 plunger seals;

at plunger letter U130 anterior segment, use and keep apart the flush fluid, continuous or be interrupted the injection plunger letter U130 anterior segment, the isolation flush fluid of injection finally enters into main hydraulic cylinder, prevents that the liquid material that comes from main hydraulic cylinder from polluting plunger letter U130 anterior segment and then polluting the 1 st plunger main seal.

According to the invention, the reciprocating plunger assembly U100 can be provided with at least 3 plunger seals, namely at least 2 plunger main seals;

in the gap JX-23 between any 2 plunger main seals, continuous or intermittent replacement of flushing liquid is used to prevent liquid material from the space near the main cylinder side from penetrating the plunger main seal into the gap JX-23 to cause pollution.

The present invention, generally, a reciprocating plunger assembly U100, provides at least 2 plunger seals;

an isolation flushing liquid is continuously or discontinuously injected into the front section of the plunger letter U130 at the front section of the plunger letter U130, and the injected isolation flushing liquid finally enters the main hydraulic cylinder to prevent liquid materials from the main hydraulic cylinder from polluting the front section of the plunger letter U130 and further polluting the 1 st plunger main seal;

the working mode of the isolation flushing liquid can be selected from 1 of the following modes:

①, the plunger U110 moves to the whole distance to separate and flush based on the reciprocating motion of the plunger U110;

② the return process of the plunger U110 is isolated and washed by taking the reciprocating motion of the plunger U110 as the reference;

the isolation flushing liquid adopts a working mode of plunger return synchronous injection, when the plunger U110 is in a return stroke, the main hydraulic cylinder sucks liquid materials, and the plunger of the injection pump for isolating the flushing liquid acts to flush the isolation liquid cavity at the front section of the plunger of the reciprocating plunger assembly U100; when the plunger U110 is in a forward stroke, the main cylinder discharges liquid materials, the plunger of the injection pump for isolating flushing liquid acts to suck the isolating liquid, and the front section of the plunger U130 of the reciprocating plunger assembly U100 is not flushed.

The invention, in general, is a plunger U130, in a form selected from 1 of:

① are one-piece components;

② is the assembly of the anterior segment of plunger case and the posterior segment of plunger case of 2 separate parts, the anterior segment of plunger case is a part, the posterior segment U131 of plunger case is another part;

③ is an assembly of multiple separate parts;

when the plunger assembly U130 comprises 2 or more plunger assembly sections, the complete plunger assembly U130 is formed after assembly.

In the invention, generally, the plunger letter U130 is an assembly of a plunger letter front section and a plunger letter rear section which are 2 split parts, wherein the plunger letter front section is one part, and the plunger letter rear section is the other part;

a reciprocating plunger assembly U100 provided with at least 2 plunger U110 seals;

at least 1 plunger U110 seal is arranged at the rear section of the plunger box, and at most all the plunger U110 seals are arranged.

In the invention, generally, the plunger letter U130 is an assembly of a plunger letter front section and a plunger letter rear section which are 2 split parts, wherein the plunger letter front section is one part, and the plunger letter rear section is the other part;

a reciprocating plunger assembly U100 provided with at least 2 plunger U110 seals;

at least 1 plunger U110 seal can be arranged at the front section of the plunger box.

According to the reciprocating plunger assembly U100, an auxiliary pump follow-up cavity can be arranged, and an auxiliary pump main cavity plug ZQS and an auxiliary pump auxiliary cavity plug FQS are arranged;

the auxiliary pump follow-up cavity is communicated with the inner cavity of the auxiliary pump through a passage AN1 and a heat transfer element HX which can be used, and the auxiliary pump follow-up cavity is communicated with the front cavity of the auxiliary pump through a passage AN2 and a heat transfer element AHX which can be used;

the auxiliary pump is provided with at least one heat transfer component which is a heat transfer component HX and/or a heat transfer component AHX;

the auxiliary pump follow-up cavity, the auxiliary pump inner cavity and the auxiliary pump front cavity are in a communicating vessel relationship.

In general, the relationship between the reciprocating plunger assembly U100, the auxiliary pump chamber plug QS and the plunger box, 1 of the following is selected for the present invention:

① the auxiliary pump cavity plug QS is not in contact with the plunger cage, and a gap exists;

② contact between the auxiliary pump cavity plug QS and the plunger box, the contact part is the auxiliary pump cavity separating filler which is installed on the plunger U110;

③ the auxiliary pump chamber plug QS is in contact with the plunger housing at the contact portion where the auxiliary pump chamber partition packing is mounted on the plunger housing U130.

In the present invention, in general, the absolute value of the difference between the operating temperature T2 of the plunger main seal closest to the main cylinder, i.e., the 1 st plunger main seal, and the main cylinder operating temperature T1 of the reciprocating plunger assembly U100 is selected from 1 of the following:

①30~60℃;

②60~90℃;

③90~150℃;

④150~200℃;

⑤ is greater than 200 ℃.

In the invention, the reciprocating plunger assembly U100 can be provided with a heat exchange jacket on the cylinder body of the plunger assembly U130, and the medium flowing in the heat exchange jacket and the working mode are selected from 1 or the combination of several of the following types:

① the heat-extracting medium with cooling effect is gas phase and/or liquid phase;

② the heating medium for heating is gas phase and/or liquid phase;

③ the heat-extracting medium with cooling and temperature control functions is in gas phase and/or liquid phase;

④ are used for heating medium with temperature control function, and are in gas phase and/or liquid phase.

The main cylinder K10, typically the pump cylinder K10 of a plunger reciprocating pump apomp, is used in conjunction with the reciprocating plunger assembly U100 of the present invention.

The plunger type reciprocating pump APUMP system can use 1 or 2 or more pump cylinders with single pump cavities.

The plunger type reciprocating pump APUMP system of the invention uses an integrated pump cylinder body which can have 1 or 2 or more pump chambers.

The pumping target liquid material of the plunger type reciprocating pump APUMP can be selected from 1 or more of the following materials:

① high temperature liquid material;

② low temperature liquid material;

③ high-pressure liquid material;

④ high temperature and high pressure liquid material;

⑤ high temperature and high pressure solid-liquid containing material;

⑥ liquid material containing easily coagulating component;

⑦ liquid material containing volatile component;

⑧ contains a solid slurry;

⑨ liquid material containing corrosive components;

⑩ liquid material containing explosive component;

liquid material containing toxic components;

a liquid material containing radioactive components.

The working mode of the injection liquid added into the stuffing box or the plunger sleeve of the plunger type reciprocating pump APUMP is selected from 1 or more of the following types:

① can be used for long term after being injected once;

② intermittent injection and discharge are performed, and the injected liquid finally enters the pump cavity of the pump body and is discharged out of the pump cavity along with the pumped target liquid;

③ the injection is continuously discharged, and the discharged injection liquid finally enters the pump cavity of the pump body and is discharged out of the pump cavity along with the pumping target liquid.

In the present invention, the operating conditions of the plunger type reciprocating pump APUMP are, in general: the temperature is 150-400 ℃, the inlet pressure is 0.3-1.0 MPa, the outlet pressure is 2.0-30.0 MPa, the weight concentration of solid particles is 0-55%, and the volume flow rate of liquid material at the inlet of the pump cavity is 0.1-150 m3/h。

The plunger type reciprocating pump APUMP can be an oil coal slurry booster pump in the direct coal hydrogenation liquefaction reaction process or the kerosene co-refining hydrogenation reaction process, and the operation conditions are as follows: the temperature is 150-350 ℃, the inlet pressure is 0.3-1.0 MPa, the outlet pressure is 2.0-30.0 MPa, the weight concentration of solid particles is 25-60%, and the volume flow rate of liquid material at the inlet of the pump cavity is 0.1-200 m3/h。

The plunger type reciprocating pump APUMP can be an oil coal slurry booster pump in the direct coal hydrogenation liquefaction reaction process or the kerosene co-refining hydrogenation reaction process, and the operation conditions are as follows: the temperature is 150-350 ℃, the inlet pressure is 0.3-1.0 MPa, the outlet pressure is 5.0-30.0 MPa, the weight concentration of solid particles is 40-55%, and the volume flow rate of liquid material at the inlet of the pump cavity is 10-150 m3/h。

The plunger type reciprocating pump APUMP can be an oil coal slurry booster pump in the coal hydrogenation direct liquefaction reaction process or the kerosene co-refining hydrogenation reaction process, and the quantities of working fluids of a plunger, a packing box and a plunger outer sleeve are as follows: the hourly volume flow of the injected liquid is 0.5-5% of the volume flow of the pumping target liquid of the plunger type reciprocating pump APUMP.

Generally, the plunger type reciprocating pump APUMP of the invention is arranged in the following way: the axis of the plunger (111) is arranged horizontally, the pump cylinder K10 is arranged vertically, the used divider XKP is arranged vertically, and the used liquid guide tube (33) is arranged vertically.

Generally, at the drive end of the plunger type reciprocating pump APUMP system of the invention, the prime mover is selected from 1 of the following:

① a motor;

② variable frequency motor;

③ diesel engines;

④ a hydraulic motor;

⑤ steamer.

Generally, the driving end of the plunger type reciprocating pump APUMP system uses a speed changer to convert high-speed motion of a prime motor into low-speed motion, and then drives a hydraulic end to work.

In general, the plunger type reciprocating pump APUMP system of the present invention comprises 1 or 2 or more pump cylinders, 1 or 2 or more plunger assemblies are used together, and 2 or more plunger assemblies use a heat transfer device HX and use the same heat transfer medium.

In general, the plunger type reciprocating pump APUMP and the system thereof form an integrated skid-mounted structure by part or all of components.

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