阅读说明：本技术 动态等静压法改性聚四氟乙烯浸渍石墨方法 (Method for modifying polytetrafluoroethylene impregnated graphite by dynamic isostatic pressing method ) 是由 孟海波 杨颖� 于 2021-11-16 设计创作，主要内容包括：本发明公开了一种动态等静压法改性聚四氟乙烯浸渍石墨方法,该方法通过对改性四氟配方、浸渍次数、压力、时间、温度等参数的科学分析和比对试验,并对每组试件分别进行耐压和耐温测试,最终得出最佳试验结果。本发明方法改善了石墨换热块的应用性能和理化性能,提高石墨换热器耐压和耐温性能和耐腐蚀性能,从而提高石墨设备的技术含量和市场竞争力,提升产品品质,提高效益；通过对石墨制设备的原材料(颗粒度、密度)、浸渍树脂种类、浸渍工艺、热固化工艺等进行研究；开发一种能适用于高温、高压和强腐蚀性工况的不透性石墨复合材料,以提高石墨设备的使用工况和使用寿命。(The invention discloses a method for impregnating graphite with modified polytetrafluoroethylene by a dynamic isostatic pressing method, which comprises the steps of scientifically analyzing and comparing parameters such as a formula of modified polytetrafluoroethylene, impregnation times, pressure, time, temperature and the like, and respectively testing the pressure resistance and the temperature resistance of each group of test pieces to finally obtain the optimal test result. The method improves the application performance and the physical and chemical properties of the graphite heat exchange block, and improves the pressure resistance, the temperature resistance and the corrosion resistance of the graphite heat exchanger, thereby improving the technical content and the market competitiveness of graphite equipment, improving the product quality and improving the benefit; the raw materials (granularity and density) of the graphite equipment, the type of impregnating resin, the impregnating process, the thermosetting process and the like are researched; the impermeable graphite composite material suitable for high-temperature, high-pressure and strong-corrosiveness working conditions is developed so as to improve the service condition and prolong the service life of graphite equipment.)

1. The method for modifying polytetrafluoroethylene impregnated graphite by a dynamic isostatic pressing method is characterized by comprising the following steps: the method comprises the following steps:

A. preparing impregnating resin, adding boron modified phenolic resin with the viscosity of 24 seconds measured by coating 4 cups and polytetrafluoroethylene emulsion with the solid content of 70% into a storage tank according to the volume ratio of 1:3, starting a heat preservation system of the tank body, controlling the temperature of the resin to be 15-20 ℃, and stirring and mixing for more than 2 hours for later use;

B. removing oil stains on the surface of the graphite heat exchange block with the granularity of 0.8-2 mm and cleaning the graphite heat exchange block;

C. sending the cleaned graphite heat exchange block into a heat treatment furnace for drying treatment, and recording the temperature and the time;

D. confirming the surface of the dried graphite heat exchange block, and blowing off graphite powder and impurities attached to the surface and in the pore passage of the graphite heat exchange block by using air, and if a problem is found, timely treating or replacing the graphite heat exchange block until the graphite heat exchange block is qualified;

E. naturally cooling the dried qualified graphite heat exchange block to 30-40 ℃, and weighing the weight;

F. the graphite heat exchange block, the upper sealing head of the pressure tank and the lower sealing head of the pressure tank are connected, sealed and assembled through bolts to form the pressure tank;

G. putting the pressure tank into the dipping kettle, connecting an upper seal head of the pressure tank with a pipeline of the pressure tank, fastening and sealing the dipping kettle, and finishing the preparation of the system device;

H. opening a vacuum pipeline, starting vacuumizing the impregnating kettle, simultaneously fastening the impregnating kettle once again, vacuumizing until the vacuum degree is more than or equal to-0.083 MPa after normal leakage test, keeping for 7.5 hours, and making a corresponding record;

I. opening a storage tank valve where the impregnating resin is located, pumping the prepared impregnating resin into an impregnating kettle, enabling the liquid level of the impregnating resin to be higher than that of a pressurization tank by more than 150mm, closing the valve after the liquid level of the resin reaches the immersion height, and closing a vacuum valve after keeping vacuumizing for 10 minutes;

J. opening a pressure system of an air compressor, pressurizing the impregnating kettle at a constant speed, starting a high-pressure circulating pump to pump impregnating resin in the impregnating kettle into an upper end enclosure of the pressure tank, enabling the impregnating resin to flow into a lower end enclosure of the pressure tank through a longitudinal hole of the graphite heat exchange block, and then flowing back to the impregnating kettle from an outlet of the lower end enclosure, wherein the pressure-applying speed of the impregnating kettle is 0.1MPa/h, and the pressure-maintaining is started when the pressure is up to 2 MPa; controlling the pressure of a high-pressure circulating pump to rise at a constant speed and always keep the pressure greater than 1MPa of the impregnation kettle, finally pressurizing to 3MPa, starting the circulating flow in a pressure maintaining state, realizing the dynamic impregnation operation by an isostatic pressing method, and keeping for 20 hours;

K. simultaneously decompressing the impregnation kettle and the pressure tank at a constant speed, and continuously keeping the dynamic one-way impregnation operation under pressure for 8 hours until the pressure of the impregnation kettle is 0MPa and the pressure of the pressure tank is 1MPa, and closing the high-pressure circulating pump;

l, opening an air compressor pressurization system to pressurize the impregnation kettle, opening a valve on a storage tank connected with the impregnation kettle, pressing the impregnating resin back into the storage tank, and closing the valve on the storage tank connected with the impregnation kettle after the impregnating resin is completely discharged;

m, then closing an air compressor pressurization system, releasing pressure and exhausting air from the impregnation kettle, carrying out primary air exchange after the air is exhausted, and then opening the impregnation kettle;

n, taking out the impregnated graphite heat exchange block, placing the graphite heat exchange block on a collection tank for overflowing and spitting the resin on the surface for 5 hours, scraping the redundant resin on the surface of the graphite heat exchange block after the overflow is finished, and weighing the wet weight of the test block;

o. then putting the graphite heat exchange block into a drying room, pressurizing to 0.6MPa to heat up the drying room, heating from normal temperature to 220 ℃, keeping the temperature for 1 hour, filling records every 30 minutes in the heating process, observing the change of pressure and temperature at any time, if overtemperature and overpressure are found, immediately opening a valve to exhaust gas so as to keep the pressure and temperature in the drying room stable, strictly prohibiting the operation of overtemperature and overpressure, stopping heating after the temperature rise is finished, releasing pressure and exhausting gas, naturally cooling to room temperature, performing air replacement for 2 times before opening the drying room, finally opening the drying room, taking out the graphite heat exchange block, cleaning resin powder on the surface of the graphite heat exchange block, weighing the quality of the graphite block, and finishing one impregnation and drying heat treatment operation;

repeating the dipping and drying heat treatment operation for 2 periods, then filling the graphite heat exchange block subjected to dipping and drying into a heat treatment tank, and preparing for heat treatment plasticizing operation;

and Q, sealing the heat treatment tank filled with the graphite heat exchange block, pressurizing to 0.6MPa, keeping the pressure, heating according to a heat treatment temperature rise curve after normal pressure test, raising the temperature to 380 ℃ from the normal temperature, preserving the heat for 3 hours, naturally cooling to below 70 ℃, performing air replacement in the tank twice before opening the tank, and finally opening the tank to take out the graphite heat exchange block of the graphite composite material impregnated with the modified polytetrafluoroethylene.

2. The dynamic isostatic pressing method for modifying polytetrafluoroethylene-impregnated graphite according to claim 1, wherein: and in the step B, cleaning the graphite blocks with the granularity of 0.8-2 mm by using gasoline to remove oil stains on the surface of the material, and then washing the graphite blocks by using clean water.

3. The dynamic isostatic pressing method for modifying polytetrafluoroethylene-impregnated graphite according to claim 1, wherein: and step C, hoisting the graphite heat exchange block by using a hoisting basket when the graphite heat exchange block is sent into the drying equipment, and carefully preventing the block materials from colliding during hoisting, lightly taking and lightly placing the block materials, and recording the temperature and the time.

4. The dynamic isostatic pressing method for modifying polytetrafluoroethylene-impregnated graphite according to claim 1, wherein: in the step C, the drying treatment is drying for 3 hours at the temperature of 120 ℃.

5. The dynamic isostatic pressing method for modifying polytetrafluoroethylene-impregnated graphite according to claim 1, wherein: in the step K, the pressure relief speed is 0.1 MPa/h.

6. The dynamic isostatic pressing method for modifying polytetrafluoroethylene-impregnated graphite according to claim 1, wherein: in the step O, the drying temperature rise curve is as follows: uniformly heating the mixture for 1 hour at the normal temperature to 80 ℃, uniformly heating the mixture for 1 hour at the temperature of 80-140 ℃, uniformly heating the mixture for 1 hour at the temperature of 140-200 ℃, uniformly heating the mixture for 1 hour at the temperature of 200-220 ℃, heating the mixture to 220 ℃ according to a heating curve, and preserving the heat for 1 hour.

7. The dynamic isostatic pressing method for modifying polytetrafluoroethylene-impregnated graphite according to claim 1, wherein: and step O, performing air replacement for 2 times before opening the drying room, and in the air exchange process, introducing tail gas into a tail gas tower for treatment.

8. The dynamic isostatic pressing method for modifying polytetrafluoroethylene-impregnated graphite according to claim 1, wherein: in the step Q, the heat treatment temperature rise curve is as follows: uniformly heating the mixture for 1 hour at the normal temperature to 100 ℃, uniformly heating the mixture for 1 hour at the temperature of 100 ℃ to 160 ℃, uniformly heating the mixture for 1 hour at the temperature of 160 ℃ to 220 ℃, uniformly heating the mixture for 1 hour at the temperature of 220 ℃ to 270 ℃, uniformly heating the mixture for 1 hour at the temperature of 270 ℃ to 320 ℃, uniformly heating the mixture for 1 hour at the temperature of 320 ℃ to 380 ℃, and preserving the heat for 3 hours when the temperature is raised to 380 ℃.

9. The dynamic isostatic pressing method for modifying polytetrafluoroethylene-impregnated graphite according to claim 1, wherein: and step Q, performing air replacement in the tank twice before opening the tank, and introducing tail gas into a tail gas spray washing tower during air exchange.

10. The dynamic isostatic pressing method for modifying polytetrafluoroethylene-impregnated graphite according to claim 1, wherein: and after the step Q, performing a step R, performing a hydrostatic test of more than or equal to 0.8MPa on the finished heat exchange block for 1 hour, and recording the pressure test condition.

Technical Field

The invention relates to a method for preparing modified polytetrafluoroethylene impregnated graphite by a dynamic isostatic pressing method, belonging to the technical field of production of modified polytetrafluoroethylene impregnated graphite.

Background

Graphite is a material with certain gaps, and the gaps of the graphite material are filled by an impregnation process to prepare an impermeable graphite composite material which can be used for manufacturing chemical equipment such as a graphite heat exchanger. The graphite material has excellent heat conductivity, heat transfer coefficient of 104W/M ℃, which is inferior to copper and aluminum, long-term aerobic use temperature of 400 ℃, excellent corrosion resistance and easy processing and manufacturing.

The existing graphite material impregnant is mainly phenolic resin, furan resin, vinyl resin and the like, but the application range of the impermeable graphite composite material for impregnating the above resins is very small, and the impregnant cannot be applied at all under the conditions of strong alkali and strong oxidizing acid.

The long-term use temperature of the polytetrafluoroethylene is-200 ℃ to-260 ℃; has excellent chemical corrosion resistance, resists corrosion to all chemicals and is called as plastic king. Most raw materials are powdery resins or concentrated dispersions, have extremely high molecular weights, are thermoplastic polymers with high crystallinity, have high melt viscosity, and show the characteristics of non-Newtonian fluids. The existing polytetrafluoroethylene graphite impregnation process technology and equipment have the defects that the service pressure of the manufactured graphite heat exchanger is generally not more than 0.3MPa, the impermeability is poor, and the requirement of chemical production development cannot be met.

Therefore, how to organically combine two high-performance materials into a high-performance composite material becomes a technical problem which is constantly addressed by the chemical industry.

Disclosure of Invention

The invention aims to provide a method for modifying polytetrafluoroethylene impregnated graphite by a dynamic isostatic pressing method. The method improves the pressure resistance, temperature resistance and corrosion resistance of the graphite heat exchange block, thereby improving the technical content and market competitiveness of graphite equipment, improving the product quality and improving the benefit; through improving the raw materials (granularity and density), the types of impregnating resins, the impregnating process, the thermosetting process and the like of the graphite equipment, an impermeable graphite composite material which can be suitable for high-temperature, high-pressure and strong-corrosivity working conditions is developed so as to improve the service condition and the service life of the graphite equipment.

The technical scheme of the invention is as follows: the method for modifying polytetrafluoroethylene impregnated graphite by a dynamic isostatic pressing method comprises the following steps:

A. preparing impregnating resin, adding boron modified phenolic resin with the viscosity of 24 seconds measured by coating 4 cups and polytetrafluoroethylene emulsion with the solid content of 70% into a storage tank according to the volume ratio of 1:3, starting a heat preservation system of the tank body, controlling the temperature of the resin to be 15-20 ℃, and stirring and mixing for more than 2 hours for later use;

B. removing oil stains on the surface of the graphite heat exchange block with the granularity of 0.8-2 mm and cleaning the graphite heat exchange block;

C. sending the cleaned graphite heat exchange block into a heat treatment furnace for drying treatment, and recording the temperature and the time;

D. confirming the surface of the dried graphite heat exchange block, and blowing off graphite powder and impurities attached to the surface and in the pore passage of the graphite heat exchange block by using air, and if a problem is found, timely treating or replacing the graphite heat exchange block until the graphite heat exchange block is qualified;

E. naturally cooling the dried qualified graphite heat exchange block to 30-40 ℃, and weighing the weight;

F. the graphite heat exchange block, the upper sealing head of the pressure tank and the lower sealing head of the pressure tank are connected, sealed and assembled through bolts to form the pressure tank;

G. putting the pressure tank into the dipping kettle, connecting an upper seal head of the pressure tank with a pipeline of the pressure tank, fastening and sealing the dipping kettle, and finishing the preparation of the system device;

H. opening a vacuum pipeline, starting vacuumizing the impregnating kettle, simultaneously fastening the impregnating kettle once again, vacuumizing until the vacuum degree is more than or equal to-0.083 MPa after normal leakage test, keeping for 7.5 hours, and making a corresponding record;

I. opening a storage tank valve where the impregnating resin is located, pumping the prepared impregnating resin into an impregnating kettle, enabling the liquid level of the impregnating resin to be higher than that of a pressurization tank by more than 150mm, closing the valve after the liquid level of the resin reaches the immersion height, and closing a vacuum valve after keeping vacuumizing for 10 minutes;

J. opening a pressure system of an air compressor, pressurizing the impregnating kettle at a constant speed, starting a high-pressure circulating pump to pump impregnating resin in the impregnating kettle into an upper end enclosure of the pressure tank, enabling the impregnating resin to flow into a lower end enclosure of the pressure tank through a longitudinal hole of the graphite heat exchange block, and then flowing back to the impregnating kettle from an outlet of the lower end enclosure, wherein the pressure-applying speed of the impregnating kettle is 0.1MPa/h, and the pressure-maintaining is started when the pressure is up to 2 MPa; controlling the pressure of a high-pressure circulating pump to rise at a constant speed and always keep the pressure greater than 1MPa of the impregnation kettle, finally pressurizing to 3MPa, starting the circulating flow in a pressure maintaining state, realizing the dynamic impregnation operation by an isostatic pressing method, and keeping for 20 hours;

K. simultaneously decompressing the impregnation kettle and the pressure tank at a constant speed, and continuously keeping the dynamic one-way impregnation operation under pressure for 8 hours until the pressure of the impregnation kettle is 0MPa and the pressure of the pressure tank is 1MPa, and closing the high-pressure circulating pump;

l, opening an air compressor pressurization system to pressurize the impregnation kettle, opening a valve on a storage tank connected with the impregnation kettle, pressing the impregnating resin back into the storage tank, and closing the valve on the storage tank connected with the impregnation kettle after the impregnating resin is completely discharged;

m, then closing an air compressor pressurization system, releasing pressure and exhausting air from the impregnation kettle, carrying out primary air exchange after the air is exhausted, and then opening the impregnation kettle;

n, taking out the impregnated graphite heat exchange block, placing the graphite heat exchange block on a collection tank for overflowing and spitting the resin on the surface for 5 hours, scraping the redundant resin on the surface of the graphite heat exchange block after the overflow is finished, and weighing the wet weight of the test block;

o. then putting the graphite heat exchange block into a drying room, pressurizing to 0.6MPa to heat up the drying room, heating from normal temperature to 220 ℃, keeping the temperature for 1 hour, filling records every 30 minutes in the heating process, observing the change of pressure and temperature at any time, if overtemperature and overpressure are found, immediately opening a valve to exhaust gas so as to keep the pressure and temperature in the drying room stable, strictly prohibiting the operation of overtemperature and overpressure, stopping heating after the temperature rise is finished, releasing pressure and exhausting gas, naturally cooling to room temperature, performing air replacement for 2 times before opening the drying room, finally opening the drying room, taking out the graphite heat exchange block, cleaning resin powder on the surface of the graphite heat exchange block, weighing the quality of the graphite block, and finishing one impregnation and drying heat treatment operation;

repeating the dipping and drying heat treatment operation for 2 periods, then filling the graphite heat exchange block subjected to dipping and drying into a heat treatment tank, and preparing for heat treatment plasticizing operation;

and Q, sealing the heat treatment tank filled with the graphite heat exchange block, pressurizing to 0.6MPa, keeping the pressure, heating according to a heat treatment temperature rise curve after normal pressure test, raising the temperature to 380 ℃ from the normal temperature, preserving the heat for 3 hours, naturally cooling to below 70 ℃, performing air replacement in the tank twice before opening the tank, and finally opening the tank to take out the graphite heat exchange block of the graphite composite material impregnated with the modified polytetrafluoroethylene.

In the step B, graphite blocks with the granularity of 0.8-2 mm are cleaned by gasoline to remove oil stains on the surface of the material, and then the graphite blocks are washed clean by clean water.

In the step C, the graphite heat exchange block is hoisted by using a hoisting basket when being sent into drying equipment, the block is prevented from collision during hoisting, the block is lightly taken and lightly placed, and the temperature and the time are recorded.

In the method for modifying polytetrafluoroethylene impregnated graphite by dynamic isostatic pressing, in the step C, the drying treatment is drying at 120 ℃ for 3 hours.

In the method for modifying polytetrafluoroethylene impregnated graphite by the dynamic isostatic pressing method, in the step K, the pressure relief speed is 0.1 MPa/h.

In the above method for modifying polytetrafluoroethylene impregnated graphite by dynamic isostatic pressing, in step O, the drying and temperature-raising curve is: uniformly heating the mixture for 1 hour at the normal temperature to 80 ℃, uniformly heating the mixture for 1 hour at the temperature of 80-140 ℃, uniformly heating the mixture for 1 hour at the temperature of 140-200 ℃, uniformly heating the mixture for 1 hour at the temperature of 200-220 ℃, heating the mixture to 220 ℃ according to a heating curve, and preserving the heat for 1 hour.

In the method for modifying polytetrafluoroethylene impregnated graphite by using the dynamic isostatic pressing method, in the step O, air replacement is carried out for 2 times before opening a drying room, and in the air exchange process, tail gas is introduced into a tail gas tower for treatment.

In the method for modifying polytetrafluoroethylene impregnated graphite by dynamic isostatic pressing, in step Q, the heat treatment temperature rise curve is as follows: uniformly heating the mixture for 1 hour at the normal temperature to 100 ℃, uniformly heating the mixture for 1 hour at the temperature of 100 ℃ to 160 ℃, uniformly heating the mixture for 1 hour at the temperature of 160 ℃ to 220 ℃, uniformly heating the mixture for 1 hour at the temperature of 220 ℃ to 270 ℃, uniformly heating the mixture for 1 hour at the temperature of 270 ℃ to 320 ℃, uniformly heating the mixture for 1 hour at the temperature of 320 ℃ to 380 ℃, and preserving the heat for 3 hours when the temperature is raised to 380 ℃.

In the method for modifying polytetrafluoroethylene impregnated graphite by dynamic isostatic pressing, in step Q, air replacement in the tank is performed twice before the tank is opened, and the tail gas is introduced into the tail gas spray washing tower during air exchange.

In the method for modifying polytetrafluoroethylene impregnated graphite by using the dynamic isostatic pressing method, after the step Q, the step R is carried out, a hydrostatic test of more than or equal to 0.8MPa is carried out on the finished heat exchange block, the time is 1 hour, and the pressure test condition is recorded.

The invention has the beneficial effects that: compared with the prior art, the invention has the following advantages:

1. because the modified polytetrafluoroethylene impregnating resin is suspension, sedimentation and delamination are easy to occur, and the method can ensure that the modified resin is always uniformly mixed.

2. Resin circulation flow scouring of the dynamic isostatic pressing method dipping operation of the high-pressure circulating pump takes away solid sediments retained on the dipping section of the graphite heat exchange block in time, avoids forming a filter membrane effect, opens an inlet of a graphite gap channel, and provides convenience for subsequent resin, particularly solid-containing resin, to smoothly enter a graphite gap.

3. The pressure difference between the pressurizing kettle and the dipping kettle forms a larger dipping driving force which is 33.3 percent larger than that of the single isostatic pressing dipping; the one-way driving force is arranged on the tube pass of the heat exchange block, namely the anticorrosive material side, so that the impregnation filling of the anticorrosive side is more compact, and a better anticorrosive protective film and pressure resistance can be formed.

4. And by using isostatic pressing impregnation, the whole impregnation pressure is ensured to be larger and more uniform.

5. The modified polytetrafluoroethylene impregnating resin has a three-dimensional reticular skeleton structure which is randomly arranged after the thermosetting phenolic resin is cured, provides an anchoring foundation for a tetrafluoro condensate, overcomes the defect of poor combination effect of tetrafluoro and graphite caused by the non-adhesiveness of tetrafluoro, and provides a welding and heat treatment process technology for organically combining two high-performance materials into a high-performance composite material.

6. The technology of the invention improves the service life of the equipment: by improving the raw materials, impregnant, impregnation heat treatment process, impregnation process device, equipment structure and the like, the developed impermeable graphite composite material can be suitable for the working conditions of high temperature, high pressure and strong corrosive media, so that the service life of graphite equipment is prolonged by more than 2 times compared with domestic similar equipment.

Drawings

FIG. 1 is a schematic structural diagram of the related apparatus of the present invention.

Detailed Description

The invention is further illustrated by the following figures and examples, which are not to be construed as limiting the invention.

The embodiment of the invention comprises the following steps: the method for modifying polytetrafluoroethylene impregnated graphite by a dynamic isostatic pressing method comprises the following steps:

A. preparing impregnating resin, adding boron modified phenolic resin with the viscosity of 24 seconds measured by coating 4 cups and polytetrafluoroethylene emulsion with the solid content of 70% into a storage tank according to the volume ratio of 1:3, starting a heat preservation system of the storage tank, controlling the temperature of the resin to be 15-20 ℃, and stirring and mixing for more than 2 hours for later use;

B. cleaning the graphite heat exchange block with the granularity of 0.8-2 mm by using gasoline to remove oil stains on the surface of the graphite heat exchange block, and then washing the graphite heat exchange block clean by using clean water;

C. and (3) feeding the cleaned graphite heat exchange block into a heat treatment furnace for drying treatment, and drying for 3 hours at the temperature of 120 ℃. When the graphite heat exchange block is sent into drying equipment, a hanging basket is used for hanging, iron wire perforation hanging is strictly forbidden, when in hanging, the block materials are prevented from colliding, the block materials are lightly taken and lightly placed, and temperature and time records are made;

D. confirming the surface of the dried graphite heat exchange block, and blowing off graphite powder and impurities attached to the surface and in the pore passage of the graphite heat exchange block by using air, and if a problem is found, timely treating or replacing the graphite heat exchange block until the graphite heat exchange block is qualified;

E. naturally cooling the dried qualified graphite heat exchange block to 30-40 ℃, and then weighing the weight;

F. and the graphite heat exchange block, the upper sealing head of the pressure tank and the lower sealing head of the pressure tank are hermetically assembled through bolts. The pressure tank is composed of a graphite heat exchange block, a pressure tank upper end enclosure, a pressure tank lower end enclosure and a fastening sealing assembly;

G. putting the pressure tank into the dipping kettle, connecting the pressure tank with a pipeline of the pressure tank, extending the pipeline of the pressure tank out of the dipping kettle to be connected with the outlet end of the high-pressure circulating pump, fastening and sealing the dipping kettle, and finishing the preparation of the system device;

H. opening a vacuum pipeline, vacuumizing the impregnation kettle, fastening the impregnation kettle once again (to ensure that air leakage cannot occur), vacuumizing until the vacuum degree is more than or equal to-0.083 MPa after normal leakage test, keeping for 7.5 hours, and making a corresponding record;

I. opening a valve on a pipeline between the storage tank and the impregnation kettle, and pumping the prepared impregnation resin into the impregnation kettle to enable the liquid level of the impregnation resin to be higher than the pressure tank by more than 150 mm; after the liquid level of the resin reaches the immersion height, closing the valve, keeping the vacuum for 10 minutes to extract air carried in the resin, and then closing a vacuum valve on a vacuum pipeline;

J. opening a pressurizing system of an air compressor, pressurizing the impregnating kettle at a constant speed, starting a high-pressure circulating pump to pump impregnating resin in the impregnating kettle into an upper end enclosure of the pressurizing tank through a pipeline of the pressurizing tank, flowing into a lower end enclosure of the pressurizing tank through a longitudinal hole of a graphite heat exchange block, flowing back into the impregnating kettle from an outlet of the lower end enclosure of the pressurizing tank, keeping the pressure of the impregnating kettle at 0.1MPa/h, and finally pressurizing to 2 MPa; controlling the pressure of the high-pressure circulating pump to rise at a constant speed, keeping the pressure to be 1MPa higher than that of the impregnation kettle all the time, and finally pressurizing to 3 MPa; starting circulating flow under the pressure maintaining state, realizing dynamic isostatic pressing impregnation operation, and keeping for 20 hours;

K. simultaneously carrying out uniform pressure relief on the impregnation kettle and the pressure tank at a pressure relief speed of 0.1MPa per hour until the pressure of the impregnation kettle is 0MPa and the pressure of the pressure tank is 1MPa, continuously maintaining the dynamic one-way impregnation operation under pressure for 8 hours, and then closing the circulating pump;

l, opening an air compressor pressurization system for pressurization, and opening a valve on a resin storage tank connected with a pipeline of the impregnation kettle; pressing the resin back into the storage tank, draining the impregnating resin, and closing a valve on a pipeline of the storage tank connected with the impregnating kettle;

m, closing the air compressor pressurization system, releasing pressure and exhausting air from the impregnation kettle, performing primary air exchange after the air is exhausted, and then opening the impregnation kettle;

and N, taking out the impregnated graphite heat exchange block, and placing the graphite heat exchange block on a collection tank for overflowing and spitting the surface resin for 5 hours. After the overflow is finished, scraping redundant resin on the surface of the graphite block, and weighing the wet weight of the test block;

and O, then filling the graphite heat exchange block into a drying room, pressurizing to 0.6MPa, and heating the drying room, wherein the drying temperature rise curve is as follows: uniformly heating from normal temperature to 80 ℃ for 1 hour, uniformly heating from 80 ℃ to 140 ℃ for 1 hour, uniformly heating from 140 ℃ to 200 ℃ for 1 hour, uniformly heating from 200 ℃ to 220 ℃ for 1 hour, heating to 220 ℃ according to a heating curve, and preserving heat for 1 hour. And (3) filling a record every 30 minutes in the temperature rising process, and observing the change of pressure and temperature at any time, wherein if overtemperature and overpressure are found, a valve needs to be opened immediately for exhausting so as to keep the pressure and temperature in the drying room stable, and the overtemperature and overpressure operation is strictly forbidden. And stopping heating after the temperature rise is finished, releasing pressure and exhausting, naturally cooling to room temperature, performing air replacement for 2 times before opening the drying room, and introducing tail gas into a tail gas tower for treatment in the ventilation process. Finally, opening the drying room, taking out the graphite heat exchange block, cleaning resin powder on the surface of the graphite heat exchange block, and weighing the mass of the graphite heat exchange block to finish one-time impregnation and drying heat treatment operation;

p, repeating the dipping and drying heat treatment operation for 2 periods, then filling the graphite heat exchange block subjected to dipping and drying into a heat treatment tank, and preparing for heat treatment plasticizing operation;

and Q, sealing the heat treatment tank filled with the graphite heat exchange block, pressurizing to 0.6MPa, keeping the pressure, and heating according to a heat treatment temperature rise curve after normal pressure test. Heat treatment temperature rise curve: uniformly heating from normal temperature to 100 ℃ for 1 hour, uniformly heating from 100 ℃ to 160 ℃ for 1 hour, uniformly heating from 160 ℃ to 220 ℃ for 1 hour, uniformly heating from 220 ℃ to 270 ℃ for 1 hour, uniformly heating from 270 ℃ to 320 ℃ for 1 hour, uniformly heating from 320 ℃ to 380 ℃ for 1 hour, keeping the temperature for 3 hours when the temperature is raised to 380 ℃, and then naturally cooling to below 70 ℃. And (3) performing air replacement in the tank twice before opening the tank, introducing tail gas into a tail gas spraying and washing tower during air exchange, and finally opening the tank to take out the graphite heat exchange block made of the modified polytetrafluoroethylene-impregnated graphite composite material.

And R, carrying out a hydrostatic test of more than or equal to 0.8MPa on the finished graphite heat exchange block for 1 hour, and recording the pressure test condition.