阅读说明：本技术 一种大量粉体助剂标液形式存储配送系统及其使用方法 (Large-amount powder auxiliary agent standard liquid type storage and distribution system and use method thereof ) 是由 陈队范 张琳 郭长青 郭颂 李国栋 刘霞 于 2020-07-30 设计创作，主要内容包括：本发明涉及一种大量粉体助剂标液形式存储配送系统及其使用方法,包括吨包上料装置、设置在吨包上料装置下方的化料缸以及与化料缸连通的若干个PE储料罐,所述化料缸内装有搅拌器和化料缸加热装置,化料缸上连通有化料缸进水管路,化料缸与PE储料罐通过进料管路连通,进料管路上装有进料管泵送装置,PE储料罐内装有储料罐保温装置,PE储料罐上连通有配送管路,本发明实现了工厂所需大剂量粉体助剂自动溶解、标液存储和实时输送、在线检测与控制、成产数据实时记录等功能,解决生产中由于称量不准、溶解不彻底、粉料飞扬等导致的产品质量问题,提高配送效率、提高生产效率,降低成本,提升产品品质,并改善工作环境,降低对操作人员的危害。(The invention relates to a large amount of powder auxiliary agent standard liquid type storage and distribution system and a using method thereof, the system comprises a ton bag feeding device, a material melting cylinder arranged below the ton bag feeding device and a plurality of PE storage tanks communicated with the material melting cylinder, wherein a stirrer and a material melting cylinder heating device are arranged in the material melting cylinder, the material melting cylinder is communicated with a material melting cylinder water inlet pipeline, the material melting cylinder is communicated with the PE storage tanks through a feeding pipeline, a feeding pipe pumping device is arranged on the feeding pipe, a storage tank heat preservation device is arranged in the PE storage tanks, and distribution pipelines are communicated with the PE storage tanks The production efficiency is improved, the cost is reduced, the product quality is improved, the working environment is improved, and the harm to operators is reduced.)

1. A storage and distribution system for a large amount of powder auxiliary agent standard liquid is characterized in that: the device comprises a ton bag feeding device (8), a material melting cylinder (6) arranged below the ton bag feeding device (8) and a plurality of PE storage tanks (1) communicated with the material melting cylinder (6), wherein a stirrer (18) and a material melting cylinder heating device (19) are arranged in the material melting cylinder (6), the material melting cylinder (6) is communicated with a material melting cylinder water inlet pipeline (20), the material melting cylinder (6) is communicated with the PE storage tanks (1) through a feeding pipeline (11), a feeding pipe pumping device is arranged on the feeding pipeline (11), a storage tank heat preservation device is arranged in the PE storage tanks (1), and the PE storage tanks (1) are communicated with a distribution pipeline (9).

2. The system for storing and dispensing a large amount of powder auxiliary agent standard solution according to claim 1, wherein: the ton bag feeding device (8) is communicated with the compressed air pipeline (16) and the soft water pipeline (17).

3. The system for storing and dispensing a large amount of powder auxiliary agent standard solution according to claim 1, wherein: the ton bag feeding device (8) comprises a barrel body (26), a filter screen (27) arranged inside the barrel body (26) and a pipe cap (28) arranged above an outlet at the lower end of the barrel body (26).

4. The system for storing and dispensing a large amount of powder auxiliary agent standard solution according to claim 1, wherein: and the feeding pipeline (11) is communicated with a material melting cylinder circulating pipeline positioned behind the feeding pipe pumping device, and the material melting cylinder circulating pipeline is communicated into the material melting cylinder (6).

5. The system for storing and dispensing a large amount of powder auxiliary agent standard solution according to claim 1, wherein: the material melting device is characterized by further comprising a heating water tank (5), wherein a water outlet of the heating water tank (5) is communicated with a material melting cylinder water inlet pipeline (20).

6. The system for storing and dispensing a large amount of powder auxiliary agent standard solution according to claim 1, wherein: the feeding pipeline (11) is communicated with a compressed air pipeline (16) and a soft water pipeline (17).

7. The system for storing and dispensing a large amount of powder auxiliary agent standard solution according to claim 1, wherein: the storage tank heat preservation device comprises an upper coil pipe fitting piece (14) and a lower coil pipe fitting piece (15), wherein the upper coil pipe fitting piece (14) and the lower coil pipe fitting piece (15) are spiral pipes with hot water communicated inside.

8. The system for storing and dispensing a large amount of powder auxiliary agent standard solution according to claim 1, wherein: the distribution pipeline (9) is provided with an end suction pump (2), the distribution pipeline (9) is communicated with a mixing pipeline (3) located behind the end suction pump (2), and the mixing pipeline (3) is communicated into the PE storage tank (1).

9. The system for storing and dispensing a large amount of powder auxiliary agent standard solution according to claim 1, wherein: the distribution pipeline (9) is communicated with a compressed air pipeline (16) and a soft water pipeline (17).

10. A use method of a large amount of powder auxiliary agent standard liquid type storage and distribution system is characterized by comprising the following steps:

a. adding a ton bag powder auxiliary agent into a material melting cylinder (6) through a ton bag feeding device (8), and cleaning the interior of the ton bag feeding device (8) through compressed air in a compressed air pipeline (16) and soft water in a soft water pipeline (17);

b. injecting hot water into the material melting cylinder (6) through a material melting cylinder water inlet pipeline (20), stirring the powder auxiliary agent in the dissolving process through a stirrer (18), and heating the powder auxiliary agent in the dissolving process through a material melting cylinder heating device (19);

c. the mixed solution in the feeding pipeline (11) is pumped back into the material melting cylinder (6) through the circulating pipeline of the material melting cylinder, so that the mixed solution in the material melting cylinder (6) circularly flows, and the solution is prevented from crystallizing;

d. injecting the mixed powder auxiliary agent in the material melting cylinder (6) into the PE storage tank (1) through the feeding pipeline (11), and cleaning the interior of the feeding pipeline (11) through compressed air in the compressed air pipeline (16) and soft water in the soft water pipeline (17);

e. keeping the temperature of the mixed solution in the PE storage tank (1) through a storage tank heat preservation device;

f. the mixed solution in the distribution pipeline (9) is pumped back into the PE storage tank (1) through the mixing pipeline (3), so that the mixed solution in the PE storage tank (1) flows circularly, and the solution is prevented from crystallizing;

g. the auxiliary agents stored in the PE storage tank (1) are distributed to all the machine stations through the distribution pipeline (9), and the interior of the distribution pipeline (9) is cleaned through compressed air in the compressed air pipeline (16) and soft water in the soft water pipeline (17).

Technical Field

The invention relates to the technical field of dyeing, in particular to the field of dyeing feeding, and specifically relates to a large amount of powder auxiliary agent standard liquid type storage and distribution system and a use method thereof.

Background

In most domestic factories, a large amount of powder auxiliaries are mostly added manually during dyeing. And (4) manually filling, adding according to the marked weight on the package, and manually weighing the excess part. The defects of high labor intensity of workers, large weighing error and the like inevitably exist in the manual filling process. The product quality problems caused by inaccurate weighing, incomplete dissolution, flying powder and the like due to human reasons are increased, the influence on the product quality and the production efficiency is caused, and the pollution to the working environment and the harm to operators are increased.

Disclosure of Invention

Aiming at the defects of the prior art, the invention provides a large amount of powder auxiliary agent standard liquid type storage and distribution system and a using method thereof, which can improve the distribution efficiency, improve the production efficiency, reduce the cost, improve the product quality, improve the working environment and reduce the harm to operators.

The invention is realized by the following technical scheme, and provides a large amount of powder auxiliary agent standard liquid type storage and distribution system which comprises a ton bag feeding device, a material melting cylinder arranged below the ton bag feeding device and a plurality of PE storage tanks communicated with the material melting cylinder, wherein a stirrer and a material melting cylinder heating device are arranged in the material melting cylinder, the material melting cylinder is communicated with a material melting cylinder water inlet pipeline, the material melting cylinder is communicated with the PE storage tanks through the material inlet pipeline, a material inlet pipe pumping device is arranged on the material inlet pipeline, a storage tank heat preservation device is arranged in the PE storage tank, and the PE storage tanks are communicated with a distribution pipeline.

During ton package loading attachment in this scheme adds the change material jar with ton package powder auxiliary agent, pours into hot water into to change the material jar through changing the material jar inlet tube way to solution carries out hybrid heating through agitator and change material jar heating device, and solution after mixing is stored in carrying each PE storage tank through the feed line, and delivers to each board through the delivery pipeline.

As optimization, the ton bag feeding device is communicated with the compressed air pipeline and the soft water pipeline, and the interior of the ton bag feeding device is cleaned through compressed air in the compressed air pipeline and soft water in the soft water pipeline.

As optimization, ton package loading attachment includes the staving, sets up the filter screen and the pipe cap of setting in staving lower extreme export top in staving inside. The filter screen in this scheme filters the powder, prevents that bold impurity from getting into the material jar that changes, and the pipe cap setting is in staving lower extreme export top, and the powder disperses to open the back and gets into the lower extreme export, prevents that the powder from piling up in a large number the jam that causes at the lower extreme export.

And as optimization, the feeding pipe is communicated with a material melting cylinder circulation pipeline behind the feeding pipe pumping device, and the material melting cylinder circulation pipeline is communicated into the material melting cylinder. Through the mixed solution pump of the material melting cylinder circulation pipeline in the scheme, the mixed solution in the material feeding pipeline is pumped back to the material melting cylinder, so that the mixed solution in the material melting cylinder flows circularly, and the solution is prevented from crystallizing and precipitating.

As optimization, the device further comprises a heating water tank, and a water outlet of the heating water tank is communicated with a water inlet pipeline of the material melting cylinder. The heating water tank in the scheme is used for supplying hot water to the material melting cylinder.

Preferably, the feeding pipeline is communicated with the compressed air pipeline and the soft water pipeline. The interior of the feed line is purged by means of compressed air in the compressed air line and soft water in the soft water line.

As optimization, the storage tank heat preservation device comprises an upper coil pipe fitting and a lower coil pipe fitting, wherein the upper coil pipe fitting and the lower coil pipe fitting are spiral pipes with hot water flowing inside. The hanging wall union piece in this scheme and lower coiled pipe closes the piece and is inside to lead to there is hydrothermal spiral pipe, through the spiral pipe of hot-water flow through, realize the heat preservation function.

Preferably, the distribution pipeline is provided with an end suction pump, a mixing pipeline positioned behind the end suction pump is communicated with the distribution pipeline, and the mixing pipeline is communicated to the PE storage tank. The mixed solution pump in the distribution pipeline is sent back to the PE storage tank through the mixed pipeline, so that the mixed solution in the PE storage tank flows circularly, and the crystallization of the solution is prevented.

Preferably, the distribution pipeline is communicated with the compressed air pipeline and the soft water pipeline. The interior of the dispensing line is purged by compressed air in the compressed air line and soft water in the soft water line.

A use method of a large amount of powder auxiliary agent standard liquid type storage and distribution system comprises the following steps:

a. adding the ton bag powder auxiliary agent into a material melting cylinder through a ton bag feeding device, and cleaning the interior of the ton bag feeding device through compressed air in a compressed air pipeline and soft water in a soft water pipeline;

b. injecting hot water into the material dissolving cylinder through a water inlet pipe of the material dissolving cylinder, stirring the powder auxiliary agent in the dissolving process through a stirrer, and heating the powder auxiliary agent in the dissolving process through a heating device of the material dissolving cylinder;

c. the mixed solution in the feeding pipeline is pumped back into the material melting cylinder through the circulating pipeline of the material melting cylinder, so that the mixed solution in the material melting cylinder circularly flows, and the solution is prevented from crystallizing;

d. injecting the mixed powder auxiliary agent in the material melting cylinder into a PE storage tank through a feeding pipeline, and cleaning the interior of the feeding pipeline through compressed air in a compressed air pipeline and soft water in a soft water pipeline;

e. keeping the temperature of the mixed solution in the PE storage tank through a storage tank heat preservation device;

f. the mixed solution in the distribution pipeline is pumped back into the PE storage tank through the mixing pipeline, so that the mixed solution in the PE storage tank flows circularly, and the solution is prevented from crystallizing;

g. the auxiliary agents stored in the PE storage tank are delivered to all the machines through the delivery pipeline, and the interior of the delivery pipeline is cleaned through compressed air in the compressed air pipeline and soft water in the soft water pipeline.

The invention has the beneficial effects that: the large-amount powder auxiliary agent standard liquid form storage and distribution system and the use method thereof realize the functions of automatic dissolution of large-amount powder auxiliary agent, standard liquid storage and real-time conveying, on-line detection and control, real-time recording of production data and the like required by a factory, solve the product quality problem caused by inaccurate weighing, incomplete dissolution, flying powder and the like in production, improve the distribution efficiency, improve the production efficiency, reduce the cost, improve the product quality, improve the working environment and reduce the harm to operators.

Drawings

FIG. 1 is a front view of the present invention;

FIG. 2 is a top view of the present invention;

FIG. 3 is a cross-sectional view taken along plane A-A of FIG. 1 in accordance with the present invention;

FIG. 4 is a front view of the PE storage tank of the present invention;

FIG. 5 is a front view of the ton bag loading apparatus of the present invention;

FIG. 6 is a front view of the material melting cylinder of the present invention;

FIG. 7 is a front view of the heating water tank of the present invention;

FIG. 8 is a schematic view of the PE storage tank dispensing of the present invention;

FIG. 9 is a schematic view of the interior of the ton bag feeding device according to the present invention;

shown in the figure:

1. PE storage tank, 2, end suction pump, 3, mixing pipeline, 4, sewage discharging system, 5, heating water tank, 6, material melting tank, 7, ton bag powder auxiliary agent, 8, ton bag feeding device, 9, distribution pipeline, 10, pipeline bracket, 11, feeding pipeline, 12, control cabinet, 13, pneumatic control device, 14, upper coil pipe assembly, 15, lower coil pipe assembly, 16, compressed air pipeline, 17, water softening pipeline, 18, stirrer, 19, material melting tank heating device, 20, material melting tank water inlet pipeline, 21, turbine flowmeter, 22, liquid level meter, 23, thermometer, 24, slag slurry pump, 25, storage tank liquid level meter, 26, barrel, 27, filter screen, 28, pipe cap, 29 and pneumatic film three-way confluence regulating valve.

Detailed Description

In order to clearly illustrate the technical features of the present solution, the present solution is explained below by way of specific embodiments.

The system can be used independently by one set and can also be used symmetrically by two sets; the system can be used independently or can be used online with an MES (manufacturing execution system) system. Two sets of symmetry are used in this embodiment.

As shown in fig. 1 to 9, the storage and distribution system for a large amount of powder additives in a standard liquid form comprises a ton bag feeding device 8, a material melting cylinder 6 arranged below the ton bag feeding device 8, and a plurality of PE storage tanks 1 communicated with the material melting cylinder 6, wherein a stirrer 18 and a material melting cylinder heating device 19 are arranged in the material melting cylinder 6, the material melting cylinder 6 is communicated with a material melting cylinder water inlet pipeline 20, the material melting cylinder 6 is communicated with the PE storage tanks 1 through a material inlet pipeline 11, a material inlet pipe pumping device is arranged on the material inlet pipeline 11, a storage tank heat preservation device is arranged in the PE storage tanks 1, and the PE storage tanks 1 are communicated with a distribution pipeline 9.

Ton package loading attachment 8 includes staving 26, sets up filter screen 27 and the pipe cap 28 of setting in staving 26 lower extreme export top in staving 26 inside, barrel 26 is the diameter in the middle of cylinder 26 and upper and lower opening all is less than barrel 26, and filter screen 27 sets up at barrel 26 inside and level, and the filter screen is circular and laminates with barrel 26 inner wall, and pipe cap 28 is big end down's toper, and pipe cap 28 passes through the support to be fixed inside barrel 26, and the lower extreme of pipe cap 28 is less than the lower extreme export of staving 26.

The ton package loading attachment 8 intercommunication compressed air pipeline 16 and soft water pipe way 17, compressed air pipeline 16 is the inside gas circuit of mill, and soft water pipe way 17 is the inside water pipe of mill, and staving 26 is inside to be equipped with a plurality of air jets that communicate with compressed air pipeline 16, still is equipped with a plurality of water jets that communicate with soft water pipe way 17.

The material melting cylinder 6 is arranged below the ton bag feeding device 8, the outlet below the ton bag feeding device 8 corresponds to the upper opening of the material melting cylinder 6, the material melting cylinder 6 is communicated with a material melting cylinder water inlet pipeline 20, a turbine flowmeter 21 is arranged on the material melting cylinder water inlet pipeline 20, the water inlet quantity inside the material melting cylinder 6 is calculated, the material melting cylinder water inlet pipeline 20 is divided into two paths to be connected to the material melting cylinder 6, one path directly flows into the material melting cylinder 6 from the top of the material melting cylinder 6, the other path is communicated to the side wall of the top of the material melting cylinder 6, the side wall of the top of the material melting cylinder 6 is provided with an annular nozzle, the other path is communicated to the annular nozzle, and therefore the inner wall of the material melting cylinder 6 is cleaned during water.

Still include heating water tank 5, heating water tank 5's delivery port and the feed cylinder water intake pipe 20 intercommunication of changing for to changing feed cylinder water intake pipe 20 and providing hot water, heating water tank 5 passes through steam heating, and 5 inside level gauges that are equipped with of heating water tank are used for detecting 5 inside water volumes of heating water tank, and the intaking of heating water tank 5 comes from two tunnel, comes from the hose all the way, and another way comes from the hot-water pool of mill.

A stirrer 18 and a melting cylinder heating device 19 are arranged in the melting cylinder 6, a stirring paddle of the stirrer 18 extends into the melting cylinder 6, and the melting cylinder heating device 19 is a spiral heating pipe with steam flowing inside. The material melting tank 6 is also provided with a liquid level meter 22 and a thermometer 23.

The material melting cylinder 6 is communicated with the PE storage tank 1 through a feeding pipeline 11, the feeding pipeline 11 is communicated to the bottom of the material melting cylinder 6, and a feeding pipe pumping device is arranged on the feeding pipeline 11, wherein the feeding pipe pumping device in the embodiment is a slurry pump 24.

And the feeding pipeline 11 is communicated with a material melting cylinder circulating pipeline positioned behind the feeding pipe pumping device, and the material melting cylinder circulating pipeline is communicated into the material melting cylinder 6.

The feeding pipeline 11 is communicated with a compressed air pipeline 16 and a soft water pipeline 17, wherein the compressed air pipeline 16 is directly communicated with the feeding pipeline 11, the soft water pipeline 17 is communicated to the material cylinder feeding pipeline 20 through a pneumatic membrane three-way confluence regulating valve 29 and then is connected to the feeding pipeline 11 through a connecting pipeline, the pneumatic membrane three-way confluence regulating valve 29 is arranged in front of the turbine flowmeter 21, and water in the material cylinder feeding pipeline 20 is switched to come from the heating water tank 5 or come from the soft water pipeline 17 through the pneumatic membrane three-way confluence regulating valve 29.

Contain three PE storage tanks 1 in this embodiment, feed line 11 and the top intercommunication of three PE storage tanks 1 to through which PE storage tank of PE tee junction confluence regulating valve control with the mixed solution injection, be equipped with storage tank heat preservation device in the storage tank 1.

Storage tank heat preservation device includes that hanging wall pipe closes piece 14 and lower coiled pipe closes piece 15, and hanging wall pipe closes piece 14 and lower coiled pipe closes piece 15 and is inside logical hydrothermal spiral pipe, and hanging wall pipe closes piece 14 and lower coiled pipe closes piece 15 all communicates with the hot-water tank, realizes the heat preservation function through the hot water in the hot-water tank, and the hot-water tank is the central hot-water tank in the mill, is responsible for providing hot water for each equipment in mill.

Still be equipped with storage tank level gauge 25 on PE storage tank 1, storage tank level gauge 25 is arranged in detecting the liquid height in PE storage tank 1.

The PE storage tank 1 is communicated with a distribution pipeline 9, the distribution pipeline 9 is communicated to the bottom of the PE storage tank 1, an end suction pump 2 is arranged on the distribution pipeline 9, a mixing pipeline 3 located behind the end suction pump 2 is communicated with the distribution pipeline 9, and the mixing pipeline 3 is communicated into the PE storage tank 1.

The dispensing line 9 communicates with a compressed air line 16 and a flexible water line 17 for flushing the dispensing line 9.

In the dyeing process, when a machine station has a feeding requirement, a distribution system is called, and the materials are distributed to the corresponding machine station through the end suction pump 2 and the distribution pipeline 9.

The sewage treatment system comprises a sewage pool arranged at the bottom and a sewage pump arranged in the sewage pool, and sewage in each part of the sewage treatment system enters the sewage pool and is discharged through the sewage pump.

A pipe support 10 is also included for supporting the various pipes. A control cabinet 12 for mounting electrical components and an air control device 13 for mounting pneumatic control components are also included.

The use method of the invention comprises the following steps: the method comprises the following steps:

place ton package powder auxiliary agent 7 to ton package loading attachment 8 top through the driving, through ton package loading attachment 8 with ton package powder auxiliary agent add in the material jar 6 to wash ton package loading attachment 8 inside through the compressed air in compressed air pipeline 16 and the soft water in the soft water pipeline 17, take out the inboard residual powder of ton package loading attachment 8.

Hot water with a certain proportion is injected into the material melting cylinder 6 through a material melting cylinder water inlet pipeline 20, the water inlet amount is controlled by a turbine flowmeter 21, the powder auxiliary agent in the dissolving process is stirred through a stirrer 18, and the powder auxiliary agent in the dissolving process is heated through a material melting cylinder heating device 19.

The mixed solution in the feeding pipeline 11 is pumped back into the material melting cylinder 6 through the material melting cylinder circulating pipeline, so that the mixed solution in the material melting cylinder 6 circularly flows, and the solution is prevented from crystallizing.

The powder auxiliary agent mixed in the material melting cylinder 6 is injected into the PE storage tank 1 through the feeding pipeline 11, and the interior of the feeding pipeline 11 is cleaned through compressed air in the compressed air pipeline 16 and soft water in the soft water pipeline 17.

Keeping the temperature of the mixed solution in the PE storage tank 1 through a storage tank heat preservation device;

the mixed solution in the distribution pipeline 9 is pumped back into the PE storage tank 1 through the mixing pipeline 3, so that the mixed solution in the PE storage tank 1 circularly flows, and the solution is prevented from crystallizing; when the additive solution in the PE storage tank 1 is lower than the liquid level meter 25, the supplement of the liquid additive is prompted.

The auxiliary agent stored in the PE storage tank 1 is delivered to each machine station through the delivery pipeline 9, and the interior of the delivery pipeline 9 is cleaned through the compressed air in the compressed air pipeline 16 and the soft water in the soft water pipeline 17.

Of course, the above description is not limited to the above examples, and the undescribed technical features of the present invention can be implemented by or using the prior art, and will not be described herein again; the above embodiments and drawings are only for illustrating the technical solutions of the present invention and not for limiting the present invention, and the present invention has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that changes, modifications, additions or substitutions within the spirit and scope of the present invention may be made by those skilled in the art without departing from the spirit of the present invention, and shall also fall within the scope of the claims of the present invention.