CN116272042A - A filter drying system for PSPI resin - Google Patents

A filter drying system for PSPI resin Download PDF

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Publication number
CN116272042A
CN116272042A CN202310343501.9A CN202310343501A CN116272042A CN 116272042 A CN116272042 A CN 116272042A CN 202310343501 A CN202310343501 A CN 202310343501A CN 116272042 A CN116272042 A CN 116272042A
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pipe
filter
valve
barrel
hose
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赵彦平
张圣成
王梅
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Mingshi New Materials Co ltd
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Mingshi New Materials Co ltd
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Priority to CN202310343501.9A priority Critical patent/CN116272042A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/01Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
    • B01D29/03Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting
    • B01D29/035Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting with curved filtering elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/62Regenerating the filter material in the filter
    • B01D29/70Regenerating the filter material in the filter by forces created by movement of the filter element
    • B01D29/72Regenerating the filter material in the filter by forces created by movement of the filter element involving vibrations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/76Handling the filter cake in the filter for purposes other than for regenerating
    • B01D29/78Handling the filter cake in the filter for purposes other than for regenerating for washing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/88Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices
    • B01D29/92Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices for discharging filtrate
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B1/00Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/28Moving screens not otherwise provided for, e.g. swinging, reciprocating, rocking, tilting or wobbling screens
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B1/00Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/46Constructional details of screens in general; Cleaning or heating of screens
    • B07B1/4609Constructional details of screens in general; Cleaning or heating of screens constructional details of screening surfaces or meshes
    • F26B21/50
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/02Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/06Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried
    • F26B3/08Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00Drying solid materials or objects by processes not involving the application of heat
    • F26B5/04Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Microbiology (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

The invention discloses a PSPI resin filtering and drying system, which comprises a barrel, wherein a filter vat is arranged in the barrel, a cavity is arranged between the filter vat and the inner wall of the barrel, a back blowing pipe, an exhaust pipe, a water inlet pipe and a feed pipe are arranged on a top plate of the barrel, a vacuum pipe and a drying air flow inlet pipe are arranged on the side wall of the barrel, and a liquid discharge pipe are arranged on a bottom plate of the barrel; the bottom of filter vat is equipped with bowl form filter, and the bottom of bowl form filter is connected with vibrating device, is equipped with powder trap, spray set and feed inlet on the roof of filter vat, and powder trap is connected with the exhaust tube respectively and blowback union coupling through giving vent to anger hose and blowback hose, and spray set passes through water inlet hose and water piping connection, and the feed inlet passes through feed hose and is connected with the inlet pipe. The PSPI resin filtering and drying system adopting the structure has the advantages of high filtering precision, good sealing performance, low loss, high yield, no slurry leakage of liquid, no blockage in filtering, high drying efficiency and small occupied space.

Description

一种PSPI树脂的过滤干燥系统A filter drying system for PSPI resin

技术领域technical field

本发明涉及PSPI树脂纯化干燥技术领域,特别是涉及一种PSPI树脂的过滤干燥系统。The invention relates to the technical field of PSPI resin purification and drying, in particular to a filter drying system for PSPI resin.

背景技术Background technique

光敏聚酰亚胺(PSPI)是一类在高分子链上兼有亚胺环以及光敏基因,集优异的热稳定性、良好的机械性能、化学和感光性能的有机材料,光敏聚酰亚胺属于聚酰亚胺中的高端产品。PSPI树脂作为半导体先进封装和光刻胶领域的卡脖子材料,国产化替代日趋重要。因其技术壁垒高,研发及中试放大研究投入大,产业化难度极高的特点,PSPI树脂的制备一直未得到有效突破,尤其在PSPI树脂的过滤、纯化以及干燥环节,困难重重,比如,堵塞、干燥时间久、工艺路线长导致系统占地面积大等。为解决上述问题需要提供一种新型的PSPI树脂的过滤干燥系统。Photosensitive polyimide (PSPI) is a kind of organic material with imide ring and photosensitive gene on the polymer chain, which has excellent thermal stability, good mechanical properties, chemical and photosensitive properties. Photosensitive polyimide It is a high-end product in polyimide. PSPI resin, as a bottleneck material in the field of semiconductor advanced packaging and photoresist, is becoming increasingly important for localization. Because of its high technical barriers, large investment in research and development and pilot scale-up research, and extremely difficult industrialization, the preparation of PSPI resin has not been effectively broken through, especially in the filtration, purification and drying of PSPI resin, which is full of difficulties, for example, Blockage, long drying time, long process route lead to large system footprint, etc. In order to solve the above problems, it is necessary to provide a novel filter drying system for PSPI resin.

发明内容Contents of the invention

本发明的目的是提供一种PSPI树脂的过滤干燥系统,有效解决堵塞、干燥时间久的问题,提升工艺系统工作效率,还能够节省整个系统的占地面积,提升树脂纯化质量。The purpose of the present invention is to provide a filtration and drying system for PSPI resin, which can effectively solve the problems of clogging and long drying time, improve the working efficiency of the process system, save the floor area of the entire system, and improve the quality of resin purification.

为实现上述目的,本发明提供了一种PSPI树脂的过滤干燥系统,包括筒体,所述筒体内设有过滤桶,所述过滤桶与所述筒体的内壁之间设有空腔,所述筒体的顶板上设有反吹管、抽气管、进水管和进料管,所述筒体的侧壁上设有与所述空腔相连通的抽真空管和干燥气流进气管,所述筒体的底板上设有排液管和排料管,所述排液管与所述空腔相连通,所述排液管上设有排液阀、电导率仪和排水流量计,所述排料管与所述过滤桶的底部相连通,所述排料管上设有卸料阀;In order to achieve the above object, the invention provides a filter drying system of PSPI resin, comprising a cylinder, a filter bucket is provided in the cylinder, a cavity is provided between the filter bucket and the inner wall of the cylinder, so The top plate of the cylinder body is provided with a blowback pipe, an air extraction pipe, a water inlet pipe and a feed pipe, and the side wall of the cylinder body is provided with a vacuum pipe and a dry air inlet pipe connected with the cavity. The bottom plate of the body is provided with a discharge pipe and a discharge pipe, the discharge pipe is connected with the cavity, a discharge valve, a conductivity meter and a drainage flowmeter are arranged on the discharge pipe, and the discharge pipe The material pipe is connected with the bottom of the filter barrel, and the discharge pipe is provided with a discharge valve;

所述过滤桶的底部设有碗状过滤板,所述碗状过滤板上设有均匀分布的凸块,所述碗状过滤板的底部通过缓冲连接件与固定在所述空腔底部的振动装置连接,所述过滤桶的顶板上设有粉体捕集器、喷淋装置和进料口,所述喷淋装置位于所述过滤桶的顶板中部,所述粉体捕集器通过出气软管和反吹软管分别与所述抽气管连接和所述反吹管连接,所述喷淋装置通过进水软管与所述进水管连接,所述进料口通过进料软管与所述进料管连接。The bottom of the filter bucket is provided with a bowl-shaped filter plate, and the bowl-shaped filter plate is provided with evenly distributed bumps. The device is connected, the top plate of the filter barrel is provided with a powder trap, a spray device and a feed port, the spray device is located in the middle of the top plate of the filter barrel, and the powder trap passes through the air outlet soft The pipe and the blowback hose are respectively connected with the suction pipe and the blowback pipe, the spray device is connected with the water inlet pipe through the water inlet hose, and the feed port is connected with the water inlet pipe through the feed hose. Feed tube connection.

优选的,所述卸料阀位于所述排料管靠近所述过滤桶的一端,且所述卸料阀为上展阀。Preferably, the discharge valve is located at one end of the discharge pipe close to the filter barrel, and the discharge valve is an upward opening valve.

优选的,所述反吹管上设有进气阀,所述抽气管上设有出气阀,所述进水管上设有进水阀,所述进料管上设有进料阀,所述抽真空管上设有控制阀,所述干燥气流进气管上设有干燥阀。Preferably, an air intake valve is provided on the back blowing pipe, an air outlet valve is provided on the air extraction pipe, a water inlet valve is provided on the water inlet pipe, a feed valve is provided on the feed pipe, and a feed valve is provided on the suction pipe. A control valve is arranged on the vacuum pipe, and a drying valve is arranged on the dry air inlet pipe.

优选的,所述碗状过滤板包括一体式连接的碗底过滤板和碗壁过滤板,所述碗底过滤板和所述碗壁过滤板之间的夹角为75°。Preferably, the bowl-shaped filter plate includes a bowl bottom filter plate and a bowl wall filter plate integrally connected, and the included angle between the bowl bottom filter plate and the bowl wall filter plate is 75°.

优选的,所述凸块为铆钉状凸块。Preferably, the bumps are rivet-shaped bumps.

优选的,所述出气软管、所述进水软管和所述进料软管靠近所述过滤桶的一端均设有止逆阀。Preferably, one end of the air outlet hose, the water inlet hose and the feed hose near the filter barrel is provided with a check valve.

优选的,所述排料管的内直径等于所述碗底过滤板的直径。Preferably, the inner diameter of the discharge pipe is equal to the diameter of the filter plate at the bottom of the bowl.

因此,本发明采用上述结构的PSPI树脂的过滤干燥系统,具有如下有益效果:Therefore, the present invention adopts the filter drying system of the PSPI resin of above-mentioned structure, has following beneficial effect:

1.有效解决过滤堵塞问题:采用独特的碗状过滤板设计,形成有效过滤面积,有效避免树脂在过滤板上的残留;过滤桶底部通过缓冲连接件固定于震动装置上,该震动装置具有控制启停开关,启动后,过滤桶可实现振动,树脂进而松散,释放被堵塞的空隙,保持空隙过滤能力。1. Effectively solve the problem of filter clogging: the unique design of bowl-shaped filter plate forms an effective filter area and effectively avoids the residue of resin on the filter plate; the bottom of the filter barrel is fixed on the vibrating device through a buffer connector. Start-stop switch, after starting, the filter barrel can vibrate, the resin will be loosened, and the clogged gap will be released to maintain the filtration capacity of the gap.

2.有效提高过滤干燥效率;系统顶部具有抽气管,实现抽真空干燥以提高干燥效率;对于易板结树脂,通过底部底部干燥气流进气管通入一定温度的气体,流化干燥树脂,带走树脂水分,明显提高干燥效率;系统顶部抽气管与粉体捕集器连接,防止抽气管堵塞的同时防止物料的流失,提高干燥收率。2. Effectively improve the efficiency of filtration and drying; the top of the system has an exhaust pipe to achieve vacuum drying to improve drying efficiency; for resins that are easy to harden, a certain temperature gas is introduced through the bottom dry air inlet pipe at the bottom to fluidize and dry the resin and take away the resin Moisture can significantly improve the drying efficiency; the exhaust pipe at the top of the system is connected to the powder collector to prevent the blockage of the exhaust pipe and prevent the loss of materials and improve the drying yield.

3.有效解决树脂干燥过程结团现象:过滤板上设有铆钉状凸块,它能够及时将形成的团状树脂进行碰撞粉粹,提高干燥效果;振动装置也能在一定程度上起到粉碎树脂结团现象,可以根据情况选择性的在干燥环节使用。3. Effectively solve the agglomeration phenomenon in the resin drying process: there are rivet-like bumps on the filter plate, which can collide and pulverize the formed agglomerate resin in time to improve the drying effect; the vibration device can also be crushed to a certain extent The phenomenon of resin agglomeration can be selectively used in the drying process according to the situation.

4.该系统能够将多种功能集成在一套设备上实现,有效解决了工艺路线复杂、生产效率低、物料转移风险高、外来杂质引入,尤其解决了空间占用大的弊端。4. The system can integrate multiple functions on a set of equipment, which effectively solves the problems of complex process routes, low production efficiency, high risk of material transfer, and introduction of foreign impurities, especially the large space occupation.

下面通过附图和实施例,对本发明的技术方案做进一步的详细描述。The technical solutions of the present invention will be described in further detail below with reference to the accompanying drawings and embodiments.

附图说明Description of drawings

图1是本发明PSPI树脂的过滤干燥系统实施例的示意图。Figure 1 is a schematic diagram of an embodiment of a filter drying system for PSPI resin of the present invention.

附图标记reference sign

1、筒体;2、过滤桶;3、空腔;4、反吹管;5、抽气管;6、进水管;7、进料管;8、进气阀;9、出气阀;10、进水阀;11、进料阀;12、抽真空管;13、干燥气流进气管;14、控制阀;15、干燥阀;16、排液管;17、排料管;18、排液阀;19、电导率仪;20、排水流量计;21、卸料阀;22、碗状过滤板;23、铆钉状凸块;24、缓冲连接件;25、振动装置;26、粉体捕集器;27、喷淋装置;28、出气软管;29、反吹软管;30、进水软管;31、进料软管;32、止逆阀。1. Cylinder body; 2. Filter barrel; 3. Cavity; 4. Blowback pipe; 5. Exhaust pipe; 6. Water inlet pipe; 7. Feed pipe; 8. Inlet valve; 9. Outlet valve; Water valve; 11, feed valve; 12, vacuum tube; 13, dry air inlet pipe; 14, control valve; 15, drying valve; 16, drain pipe; 17, discharge pipe; 18, drain valve; 19 , conductivity meter; 20, drainage flow meter; 21, discharge valve; 22, bowl-shaped filter plate; 23, rivet-shaped bump; 24, buffer connector; 25, vibration device; 26, powder trap; 27. Spraying device; 28. Air outlet hose; 29. Blowback hose; 30. Water inlet hose; 31. Feed hose; 32. Check valve.

具体实施方式Detailed ways

下面结合附图对本发明的实施方式做进一步的说明。Embodiments of the present invention will be further described below in conjunction with the accompanying drawings.

如图所示,一种PSPI树脂的过滤干燥系统,包括筒体1,筒体1内设有过滤桶2,过滤桶2与筒体1的内壁之间设有空腔3。筒体1的顶板上设有反吹管4、抽气管5、进水管6和进料管7,反吹管4上设有进气阀8,抽气管5上设有出气阀9,进水管6上设有进水阀10,进料管7上设有进料阀11。筒体1的侧壁上设有与空腔3相连通的抽真空管12和干燥气流进气管13,抽真空管12上设有控制阀14,抽真空管12能够对筒体1进行抽真空,此时过滤桶2内PSPI树脂吸附的液体因压差作用与PSPI树脂分离,快速通过空腔3排出筒体1,增加干燥效率。干燥气流进气管13上设有干燥阀15,干燥阀15能控制干燥气流进气管13的启闭。As shown in the figure, a filtering and drying system for PSPI resin includes a cylinder body 1, a filter bucket 2 is arranged inside the cylinder body 1, and a cavity 3 is arranged between the filter bucket 2 and the inner wall of the cylinder body 1. The top plate of the cylinder body 1 is provided with a blowback pipe 4, an air extraction pipe 5, a water inlet pipe 6 and a feed pipe 7, an air inlet valve 8 is arranged on the blowback pipe 4, an air outlet valve 9 is arranged on the air extraction pipe 5, and an air outlet valve 9 is arranged on the water inlet pipe 6. A water inlet valve 10 is provided, and a feed valve 11 is provided on the feed pipe 7 . The side wall of the cylinder 1 is provided with a vacuum tube 12 connected with the cavity 3 and a dry air inlet tube 13. The vacuum tube 12 is provided with a control valve 14, and the vacuum tube 12 can vacuum the cylinder 1. At this time The liquid absorbed by the PSPI resin in the filter barrel 2 is separated from the PSPI resin due to the pressure difference, and is quickly discharged from the barrel 1 through the cavity 3 to increase the drying efficiency. The dry air inlet pipe 13 is provided with a dry valve 15 which can control the opening and closing of the dry air inlet pipe 13 .

筒体1的底板上设有排液管16和排料管17,排液管16与空腔3相连通,排液管16能够将空腔3内的液体排出。排液管16上设有排液阀18、电导率仪19和排水流量计20,通过排液阀18、电导率仪19和排水流量计20上的数值显示判断排液阀18的启闭。排料管17与过滤桶2的底部相连通,排料管17上设有卸料阀21,卸料阀21位于排料管17靠近过滤桶2的一端,且卸料阀21为上展阀,上展阀能够防止小部分浆料进入排料管17内进而影响干燥效果。排料管17的内直径等于碗底过滤板的直径,防止物料在碗底过滤板上堆积。A discharge pipe 16 and a discharge pipe 17 are arranged on the bottom plate of the cylinder body 1 , the liquid discharge pipe 16 communicates with the cavity 3 , and the liquid discharge pipe 16 can discharge the liquid in the cavity 3 . The discharge pipe 16 is provided with a discharge valve 18 , a conductivity meter 19 and a drainage flowmeter 20 , and the opening and closing of the discharge valve 18 is judged by the numerical display on the discharge valve 18 , the conductivity meter 19 and the drainage flowmeter 20 . The discharge pipe 17 communicates with the bottom of the filter barrel 2, and the discharge pipe 17 is provided with a discharge valve 21. The discharge valve 21 is located at the end of the discharge pipe 17 close to the filter barrel 2, and the discharge valve 21 is an upward opening valve. , The upper opening valve can prevent a small part of the slurry from entering the discharge pipe 17 to affect the drying effect. The inner diameter of discharge pipe 17 is equal to the diameter of the filter plate at the bottom of the bowl, preventing material from accumulating on the filter plate at the bottom of the bowl.

过滤桶2的底部设有碗状过滤板22,碗状过滤板22包括一体式连接的碗底过滤板和碗壁过滤板,碗底过滤板和碗壁过滤板之间的夹角为75°,碗底过滤板能够形成有效过滤面积,有效避免液体在过滤板上的残留。碗状过滤板22上设有均匀分布的凸块,凸块为铆钉状凸块23,铆钉状凸块23能够及时将形成的团状树脂进行碰撞粉粹,提高干燥效果。The bottom of the filter barrel 2 is provided with a bowl-shaped filter plate 22, and the bowl-shaped filter plate 22 includes an integrally connected bowl bottom filter plate and a bowl wall filter plate, and the included angle between the bowl bottom filter plate and the bowl wall filter plate is 75° , The filter plate at the bottom of the bowl can form an effective filtering area, effectively avoiding liquid residue on the filter plate. The bowl-shaped filter plate 22 is provided with evenly distributed bumps, and the bumps are rivet-shaped bumps 23, which can collide and pulverize the formed mass resin in time to improve the drying effect.

碗状过滤板22的底部通过缓冲连接件24与固定在空腔3底部的振动装置25连接,震动装置为过滤桶2提供震动能源,增加过滤效率,同时增加团状树脂的碰撞粉碎效果。过滤桶2的顶板上设有粉体捕集器26、喷淋装置27和进料口,喷淋装置27位于过滤桶2的顶板中部。粉体捕集器26通过出气软管28和反吹软管29分别与抽气管5连接和反吹管4连接,粉体捕集器26能够对干燥过程中被气流吹起的PSPI树脂进行收集,反吹软管29能够将粉体捕集器26收集的PSPI树脂吹落回过滤桶2,防止PSPI树脂流失的同时能够防止粉体捕集器26发生堵塞。喷淋装置27通过进水软管30与进水管6连接,进料口通过进料软管31与进料管7连接。出气软管28、进水软管30和进料软管31靠近过滤桶2的一端均设有止逆阀32,止逆阀32防止PSPI树脂被气流吹起时进入出气软管28、进水软管30和进料软管31进而造成管道堵塞。The bottom of the bowl-shaped filter plate 22 is connected to the vibrating device 25 fixed at the bottom of the cavity 3 through the buffer connector 24. The vibrating device provides vibration energy for the filter barrel 2 to increase the filtration efficiency and increase the impact and crushing effect of the lump resin. The top plate of the filter barrel 2 is provided with a powder trap 26 , a spray device 27 and a feeding port, and the spray device 27 is located in the middle of the top plate of the filter barrel 2 . The powder catcher 26 is connected to the suction pipe 5 and the blowback pipe 4 respectively through the air outlet hose 28 and the blowback hose 29. The powder catcher 26 can collect the PSPI resin blown by the airflow during the drying process, The blowback hose 29 can blow the PSPI resin collected by the powder trap 26 back to the filter barrel 2, preventing the loss of the PSPI resin and preventing the powder trap 26 from clogging. The spraying device 27 is connected with the water inlet pipe 6 through the water inlet hose 30 , and the feed port is connected with the feed pipe 7 through the feed hose 31 . The air outlet hose 28, the water inlet hose 30 and the feed hose 31 are all provided with a check valve 32 near the end of the filter barrel 2, and the check valve 32 prevents the PSPI resin from entering the outlet hose 28 and the water inlet when it is blown up by the air flow. The hose 30 and the feed hose 31 in turn cause a pipe blockage.

使用时,按照如下步骤利用本发明PSPI树脂的过滤干燥系统实现PSPI树脂浆料的过滤、纯化及干燥工艺:During use, utilize the filter drying system of PSPI resin of the present invention to realize the filtration, purification and drying process of PSPI resin slurry according to the following steps:

步骤1:添加PSPI树脂浆料:利用进料管7向过滤桶2中输送PSPI树脂浆料,树脂固体通过碗状过滤板22拦截留在过滤桶2内部,滤液通过碗状过滤板22空隙进入空腔3内并通过排液管16排出。Step 1: Add PSPI resin slurry: use the feed pipe 7 to transport the PSPI resin slurry to the filter tank 2, the resin solids are intercepted and left in the filter tank 2 through the bowl-shaped filter plate 22, and the filtrate enters through the gap of the bowl-shaped filter plate 22 The cavity 3 is discharged through the drain pipe 16.

步骤2:淋洗树脂固体:利用进水管6向过滤桶2中输送纯水,纯水通过喷淋装置27对被拦截下来的树脂固体进行淋洗。Step 2: rinse the resin solids: use the water inlet pipe 6 to deliver pure water to the filter barrel 2, and the pure water will rinse the intercepted resin solids through the spray device 27.

步骤3:浸泡树脂固体:待排液管16上的电导率仪19检测到的电导率达80-100us/cm后关闭排液阀18,转入浸泡,并对树脂固体浸泡4h后。Step 3: Soak the solid resin: when the conductivity detected by the conductivity meter 19 on the drain pipe 16 reaches 80-100us/cm, close the drain valve 18, switch to soaking, and soak the resin solid for 4 hours.

步骤4:排除滤液:开启排液阀18进行滤液的排放,同时进行如下操作以增加滤液的排放速度:开启控制阀14并利用抽真空管12对筒体1进行抽真空,抽真空进行1-5分钟后,碗状过滤板22的孔隙会被逐渐堵塞而使排水流量计20上显示的排水流量变小,此时启动振动装置25,通过缓冲连接件24将振动传导到过滤桶2上,直至排水流量计20上显示的排水流量为0时,关闭抽真空管12上的控制阀14停止抽真空,并打开干燥气流进气管13上的干燥阀15进行破真空,破真空1分钟后关停振动装置25。震动装置能够使孔隙内的树脂因振动产生位移,进而提升排液效率。Step 4: Remove the filtrate: open the drain valve 18 to discharge the filtrate, and at the same time perform the following operations to increase the discharge speed of the filtrate: open the control valve 14 and use the vacuum tube 12 to vacuum the cylinder 1, and perform 1-5 Minutes later, the pores of the bowl-shaped filter plate 22 will be gradually blocked and the drainage flow shown on the drainage flowmeter 20 will become smaller. At this time, the vibrating device 25 will be started, and the vibration will be transmitted to the filter bucket 2 by the buffer connector 24 until When the drainage flow rate displayed on the drainage flow meter 20 is 0, close the control valve 14 on the vacuum pumping pipe 12 to stop vacuuming, and open the drying valve 15 on the dry air inlet pipe 13 to break the vacuum, and stop the vibration after breaking the vacuum for 1 minute Device 25. The vibrating device can make the resin in the pores move due to vibration, thereby improving the drainage efficiency.

步骤5:干燥:维持干燥气流进气管13上干燥阀15打开的状态,同时打开抽气管5上的出气阀9,保持过滤桶2内负压状态,通过干燥气流进气管13进入过滤桶2内部的气体具有一定的温度,能够快速干燥树脂。干燥过程中,树脂固体会发生抱团现象成球状,当球状树脂固体碰触到铆钉状凸块23时球状树脂固体破裂,达到加快干燥的效果;当树脂固体水分含量小于一定程度时,树脂固体会被底部的吹扫气流吹起来,为避免这个过程树脂固体的损失,粉体捕集器26将发挥树脂粉体捕集作用,抽气管5发生堵塞时关闭出气阀9并打开反吹管4上的进气阀8及时将捕集的树脂进行吹扫,保证捕集器的工作效率。Step 5: Drying: keep the drying valve 15 on the dry air inlet pipe 13 open, and open the air outlet valve 9 on the exhaust pipe 5 at the same time to keep the negative pressure in the filter bucket 2, and enter the inside of the filter bucket 2 through the dry air inlet pipe 13 The gas has a certain temperature and can quickly dry the resin. During the drying process, the resin solid will clump into a ball, and when the spherical resin solid touches the rivet-shaped bump 23, the spherical resin solid will break, so as to achieve the effect of accelerating drying; when the moisture content of the resin solid is less than a certain level, the resin solid will Blown up by the purge airflow at the bottom, in order to avoid the loss of resin solids in this process, the powder trap 26 will play a role in trapping resin powder. The intake valve 8 blows out the trapped resin in time to ensure the working efficiency of the trap.

步骤6:树脂固体装袋打包:首先利用卸料阀21的开启和关闭进行树脂固体的取样,树脂固体水分符合规定数值后,关闭干燥气流进气管13上的干燥阀15、抽气管5上的出气阀9和反吹管4上的进气阀8,打开卸料阀21进行树脂固体的出料、装袋和打包。Step 6: Resin solids are bagged and packaged: first use the opening and closing of the unloading valve 21 to sample the resin solids. After the moisture content of the resin solids meets the specified value, close the drying valve 15 on the air intake pipe 13 of the dry air flow and the air extraction pipe 5. The gas outlet valve 9 and the inlet valve 8 on the blowback pipe 4 open the unloading valve 21 to carry out the discharging, bagging and packing of the resin solid.

因此,本发明采用上述结构的PSPI树脂的过滤干燥系统,有效解决堵塞、干燥时间久的问题,提升工艺系统工作效率,还能够节省整个系统的占地面积,提升树脂纯化质量。Therefore, the present invention adopts the PSPI resin filtration and drying system with the above-mentioned structure, effectively solves the problems of clogging and long drying time, improves the working efficiency of the process system, saves the floor space of the entire system, and improves the quality of resin purification.

最后应说明的是:以上实施例仅用以说明本发明的技术方案而非对其进行限制,尽管参照较佳实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对本发明的技术方案进行修改或者等同替换,而这些修改或者等同替换亦不能使修改后的技术方案脱离本发明技术方案的精神和范围。Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention and not to limit them. Although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that: it still Modifications or equivalent replacements can be made to the technical solutions of the present invention, and these modifications or equivalent replacements cannot make the modified technical solutions deviate from the spirit and scope of the technical solutions of the present invention.

Claims (7)

1. A filter-drying system for PSPI resin, characterized in that: the filter comprises a barrel, wherein a filter vat is arranged in the barrel, a cavity is formed between the filter vat and the inner wall of the barrel, a top plate of the barrel is provided with a back blowing pipe, an exhaust pipe, a water inlet pipe and a feed pipe, a side wall of the barrel is provided with an vacuumizing pipe and a drying air flow inlet pipe which are communicated with the cavity, a bottom plate of the barrel is provided with a liquid discharge pipe and a liquid discharge pipe, the liquid discharge pipe is communicated with the cavity, the liquid discharge pipe is provided with a liquid discharge valve, a conductivity meter and a water discharge flowmeter, the liquid discharge pipe is communicated with the bottom of the filter vat, and the liquid discharge pipe is provided with a discharge valve;
the bottom of filter vat is equipped with bowl form filter, be equipped with evenly distributed's lug on the bowl form filter, the bottom of bowl form filter is passed through the buffer connection spare and is fixed vibrating device in cavity bottom is connected, be equipped with powder trap, spray set and feed inlet on the roof of filter vat, spray set is located the roof middle part of filter vat, powder trap pass through give vent to anger hose and blowback hose respectively with the exhaust tube is connected with the blowback union coupling, spray set pass through the water inlet hose with advance water piping connection, the feed inlet pass through the feed hose with the feed pipe is connected.
2. The filter-drying system for PSPI resin according to claim 1, wherein: the discharge valve is located the row material pipe is close to the one end of filter vat, just the discharge valve is the exhibition valve.
3. The filter-drying system for PSPI resin according to claim 2, wherein: the back-blowing pipe is provided with an air inlet valve, the exhaust pipe is provided with an air outlet valve, the water inlet pipe is provided with a water inlet valve, the water inlet pipe is provided with a feed valve, the exhaust pipe is provided with a control valve, and the dry air inlet pipe is provided with a dry valve.
4. A PSPI resin filter drying system according to claim 3, wherein: the bowl-shaped filter plate comprises a bowl bottom filter plate and a bowl wall filter plate which are connected integrally, and an included angle between the bowl bottom filter plate and the bowl wall filter plate is 75 degrees.
5. The filter-drying system for PSPI resin according to claim 4, wherein: the lug is a rivet-shaped lug.
6. The filter-drying system for PSPI resin according to claim 5, wherein: and one end of the air outlet hose, the water inlet hose and one end of the feeding hose, which is close to the filter vat, are provided with check valves.
7. The filter-drying system for PSPI resin according to claim 6, wherein: the inner diameter of the discharge pipe is equal to the diameter of the bowl bottom filter plate.
CN202310343501.9A 2023-03-29 2023-03-29 A filter drying system for PSPI resin Pending CN116272042A (en)

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Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002320803A (en) * 2001-04-26 2002-11-05 Shionogi & Co Ltd Filtration and drying equipment
CN201014900Y (en) * 2007-03-09 2008-01-30 吕江强 Filtration washing vibration drying machines
CN101121089A (en) * 2007-05-21 2008-02-13 吴江市天地人真空炉业有限公司 Air-extracting and filtering device of vacuum unit
CN101995154A (en) * 2010-11-19 2011-03-30 太仓正信干燥设备科技有限公司 Bar type catcher and single-cone dryer with same
CN104906854A (en) * 2015-06-19 2015-09-16 临海市华海制药设备有限公司 Efficient press filter and filter method thereof
CN210602592U (en) * 2019-07-01 2020-05-22 福建康百赛新材料有限公司 Chemical fiber vacuum drying equipment
CN114798404A (en) * 2022-05-18 2022-07-29 西安科技大学 Building mortar preparation auxiliary device
CN115770430A (en) * 2022-12-07 2023-03-10 山东中京生物科技有限公司 Extraction element of refined chenodeoxycholic acid

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002320803A (en) * 2001-04-26 2002-11-05 Shionogi & Co Ltd Filtration and drying equipment
CN201014900Y (en) * 2007-03-09 2008-01-30 吕江强 Filtration washing vibration drying machines
CN101121089A (en) * 2007-05-21 2008-02-13 吴江市天地人真空炉业有限公司 Air-extracting and filtering device of vacuum unit
CN101995154A (en) * 2010-11-19 2011-03-30 太仓正信干燥设备科技有限公司 Bar type catcher and single-cone dryer with same
CN104906854A (en) * 2015-06-19 2015-09-16 临海市华海制药设备有限公司 Efficient press filter and filter method thereof
CN210602592U (en) * 2019-07-01 2020-05-22 福建康百赛新材料有限公司 Chemical fiber vacuum drying equipment
CN114798404A (en) * 2022-05-18 2022-07-29 西安科技大学 Building mortar preparation auxiliary device
CN115770430A (en) * 2022-12-07 2023-03-10 山东中京生物科技有限公司 Extraction element of refined chenodeoxycholic acid

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