CN111851117B - Production process of superfine glass fiber partition plate - Google Patents
Production process of superfine glass fiber partition plate Download PDFInfo
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- CN111851117B CN111851117B CN202010725244.1A CN202010725244A CN111851117B CN 111851117 B CN111851117 B CN 111851117B CN 202010725244 A CN202010725244 A CN 202010725244A CN 111851117 B CN111851117 B CN 111851117B
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F9/00—Complete machines for making continuous webs of paper
- D21F9/02—Complete machines for making continuous webs of paper of the Fourdrinier type
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F1/00—Wet end of machines for making continuous webs of paper
- D21F1/48—Suction apparatus
- D21F1/52—Suction boxes without rolls
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/36—Inorganic fibres or flakes
- D21H13/38—Inorganic fibres or flakes siliceous
- D21H13/40—Inorganic fibres or flakes siliceous vitreous, e.g. mineral wool, glass fibres
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/63—Inorganic compounds
- D21H17/65—Acid compounds
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H25/00—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
- D21H25/04—Physical treatment, e.g. heating, irradiating
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Abstract
The application relates to a production process of a superfine glass fiber partition plate, which comprises the following steps: s1: weighing raw materials, namely weighing preset purified water, glass fiber cotton, a fiber softening reinforcing agent and sulfuric acid; s2: stirring and settling, namely putting the raw materials into a stirring kettle for stirring, and conveying the raw materials to a settling pond after stirring to finally form slurry; s3: a step of feeding the slurry to a conveying net through a head box; s4: dewatering and forming, namely dewatering the slurry on the conveying net by using a dewatering device to form a fiber partition plate; s5: drying and cooling, namely conveying the fiber partition plate to a drying box for drying, and conveying the dried fiber partition plate to a cooling device for cooling; s6: and (6) rolling, namely rolling the cooled fiber partition plate by using a rolling machine. This application takes place to bond after having the dry rolling of reduction to guarantee product quality's effect.
Description
Technical Field
The application relates to the field of glass fiber production, in particular to a production process of an ultrafine glass fiber partition plate.
Background
At present, with the development of science and technology, in order to deal with the limitation that petrochemical energy is used as non-renewable energy, the electric automobile industry using lead-acid storage battery as power energy is in a period of vigorous development, the lead-acid storage battery is a battery with mature technology and safety and environmental protection, and a layer of fiber partition plate needs to be sandwiched between the positive plate and the negative plate of the lead-acid storage battery in the assembly production process, and the fiber partition plate can absorb a large amount of electrolyte, so that the fiber partition plate is an important component in the storage battery.
The Chinese patent with publication number CN103836306B in the prior art discloses a production process of a glass fiber ultra-low temperature heat insulation material, and discloses a production method of the glass fiber ultra-low temperature heat insulation material, which is characterized in that glass fiber cotton is used as a raw material, a softening reinforcing agent is added by utilizing the strength and scientific proportion of the glass fiber cotton, the glass fiber cotton is subjected to the process treatments of disintegration, pulping, fluffing, chopping and the like, the glass fiber cotton is subjected to strict metering, sufficient stirring and dispersion, the dehydration and forming are carried out by a wet process, and the glass fiber ultra-low temperature heat insulation material is obtained after drying, coiling, rewinding, slitting and compounding. The product of the glass fiber has low ration, excellent heat preservation effect and good air permeability.
In view of the above-mentioned related technologies, the inventor believes that after the glass fiber cotton is dried at a high temperature, the surface of the fiber cotton is melted and has viscosity, and the direct rolling at this time causes the glass fiber cotton to be bonded with each other, thereby affecting the product quality.
Disclosure of Invention
In order to reduce the bonding generated during the rolling of the fiber separator and ensure the product quality, the application provides a production process of the superfine glass fiber separator.
The application provides a superfine glass fiber baffle production technology, adopts following technical scheme:
a production process of an ultrafine glass fiber separator comprises the following steps: s1: weighing raw materials, namely weighing preset purified water, glass fiber cotton, a fiber softening reinforcing agent and sulfuric acid; s2: stirring and settling, namely putting the raw materials into a stirring kettle for stirring, and conveying the raw materials to a settling pond after stirring to finally form slurry; s3: a net, wherein the slurry flows to a conveying net through a head box; s4: dewatering and forming, namely dewatering the slurry on the conveying net by using a dewatering device to form a fiber partition plate; s5: drying and cooling, namely conveying the fiber partition plate to a drying box for drying, and conveying the dried fiber partition plate to a cooling device for cooling; s6: and (4) rolling, namely rolling the cooled fiber separator by using a rolling machine.
Through adopting above-mentioned technical scheme, after thick liquid dehydration shaping forms the fibre baffle, can dry to the fibre baffle once more through the stoving case to guarantee the inside dry shaping of fibre baffle, can directly get into cooling device after the stoving completion, thereby can cool off the fibre baffle, reduce the melting of cellucotton, and hinder bonding each other between the fibre baffle, and then be favorable to reducing and lead to the fact destruction to the fibre baffle, guaranteed product quality.
Preferably, dewatering device includes the box that absorbs water, vacuum pump, absorbs water pipe and outlet pipe, the box that absorbs water is the cuboid form box body of top trompil, the box that absorbs water is located the below of carrying the net, the one end that absorbs water the pipe with the air inlet intercommunication of vacuum pump, the other end with the box inner chamber intercommunication that absorbs water, the one end of outlet pipe with the gas outlet intercommunication of vacuum pump, the other end with cooling device's water inlet intercommunication.
Through adopting above-mentioned technical scheme, the water that breaks away from the fibre baffle can let in among the cooling device to can cool off the fibre baffle after the high temperature drying, and then can realize the reutilization to the water that breaks away from, reduce the water waste.
Preferably, the water outlet pipe is connected with a filter box.
Through adopting above-mentioned technical scheme, utilize the filter cartridge to filter the water that breaks away from out from the fibre baffle, and then can reduce impurity and get into cooling device, reduce and cause the jam to cooling device, be favorable to guaranteeing cooling device's hydrologic cycle.
Preferably, the cooling device comprises a first cooling pipe, a water pipe and a water storage tank, the first cooling pipe is wound on the conveying net, the fiber partition plate penetrates through the first cooling pipe, the first cooling pipe is communicated with one end of the water pipe, the other end of the water pipe is communicated with the water storage tank, a water outlet of the water storage tank is communicated with a material inlet of the stirring kettle, and a water outlet of the water storage tank is connected with a first valve.
By adopting the technical scheme, the first cooling pipe wound on the conveying net can form a cooling pipeline, so that the fiber partition plate can be quickly cooled after entering the cooling pipeline; in addition, the cooling water in the first cooling pipe finally enters the water storage tank, and the water in the water storage tank is used for making slurry, so that the waste of the cooling water can be reduced, and the environment-friendly effect is achieved.
Preferably, the cooling device further comprises a second cooling pipe, the second cooling pipe is wound on the conveying net and is arranged in a staggered mode with the first cooling pipe, high-pressure cooling water is connected to a water inlet of the second cooling pipe, and a water outlet of the second cooling pipe is communicated with the water conveying pipe.
Through adopting above-mentioned technical scheme, the cooling tube two is crisscross to be set up on cooling tube one to let in high-pressure cooling water in cooling tube two, can further improve cooling device's cooling effect, further realized the rapid cooling of fibre baffle.
Preferably, the water inlet of the second cooling pipe and the water inlet of the first cooling pipe are respectively located at two ends of the conveying net.
Through adopting above-mentioned technical scheme, because the heat that is close to stoving case one end is more, cooling water can absorb a large amount of heats behind stoving case one end of flowing through, lead to the cooling effect that cooling tube kept away from stoving case one end to reduce easily, and set up the water inlet of cooling tube two and the water inlet of cooling tube one to be located the both ends of carrying the net respectively, can make the cooling tube who keeps away from stoving case one end still can input the cooling water that does not absorb the heat, and then can improve the cooling effect that cooling device kept away from stoving case one end.
Preferably, a heat insulation plate is arranged between the first cooling pipe and the drying box.
Through adopting above-mentioned technical scheme, utilize the heat insulating board can reduce heat transfer to cooling device in the drying cabinet, and then can reduce the cooling effect that causes the influence to cooling device.
Preferably, the cooling device with be provided with between the rolling machine and air-dry the device, air-dry the device including be located the support frame and the rigid coupling of fibre baffle both sides in the fan of support frame one end, the fan is located the intermediate position of a fibre baffle side, just the wind direction of fan with the length direction of fibre baffle is perpendicular.
Through adopting above-mentioned technical scheme, because the fibre baffle behind cooling device, there is the cooling water of drippage among the cooling device on the fibre baffle, and the fibre baffle is when air-drying the device through the process, and the fan on the air-dry device can be bloied the fibre baffle, and then can take away the moisture on the fibre baffle, guarantees the drying of fibre baffle.
Preferably, the air-drying device further comprises four compression rollers rotatably arranged on the support frame, the four compression rollers are positioned on two sides of the fan in pairs, and the fiber partition plate penetrates through the compression rollers on two sides of the fan.
Through adopting above-mentioned technical scheme, utilize the compression roller can compress tightly the fibre baffle that the device was air-dried to the way, and then can reduce and blow because of the fan and cause the removal to the fibre baffle, guarantee that the fibre baffle carries in order.
In summary, the present application includes at least one of the following beneficial technical effects:
the fiber separators are cooled after being dried at high temperature, so that the mutual adhesion among the fiber separators can be prevented, the damage to the fiber separators can be reduced, and the product quality is ensured;
the water separated from the fiber partition plate is introduced into the cooling device, and the fiber partition plate dried at high temperature is cooled, so that the separated water can be reused, and the waste of water resources is reduced;
through setting up cooling tube two, set up cooling tube two crisscross on cooling tube one to let in high-pressure cooling water in cooling tube two, can improve cooling device's cooling effect, further realized the rapid cooling of fibre baffle.
Drawings
FIG. 1 is a flow chart of a process for producing a fibrous insulation board according to an embodiment of the present invention.
FIG. 2 is a schematic view showing the overall structure of a dehydration device and a cooling device according to an embodiment of the present invention.
Fig. 3 is a partial schematic view of the structure of fig. 1, mainly illustrating the configuration of the cooling device and the seasoning device.
Description of the reference numerals: 101. a fibrous separator; 11. stirring the mixture in a kettle; 12. a sedimentation tank; 121. a pumping pump; 13. a head box; 14. a conveying net; 15. a dewatering device; 151. a water absorption box; 152. a vacuum pump; 153. a suction pipe; 154. a water outlet pipe; 1541. a filter cartridge; 16. a drying box; 161. a heat insulation plate; 17. a cooling device; 171. a first cooling pipe; 172. a water delivery pipe; 173. a water storage tank; 1731. a valve; 174. a second cooling pipe; 18. a winding machine; 19. an air drying device; 191. a support frame; 192. a fan; 193. and (4) pressing the rolls.
Detailed Description
The present application is described in further detail below with reference to figures 1-3.
The embodiment of the application discloses a production process of a superfine glass fiber separator. Referring to fig. 1, a process for manufacturing a microglass fiber separator includes:
s1: weighing raw materials, and weighing preset purified water, glass fiber cotton, a fiber softening reinforcing agent and sulfuric acid.
S2: stirring and settling, namely putting the raw materials into a stirring kettle 11 for stirring, and conveying the stirred raw materials to a settling pond 12 to finally form slurry; in the specific embodiment, the pH value of the stirred tank 11 is 3.5, and the concentration is 3%.
S3: the wire is moved on to the wire, and the slurry is passed through the head box 13 to the transfer wire 14, and the slurry can be uniformly fed into the transfer wire 14 by the head box 13.
S4: dewatering forming, in which the slurry on the conveying net 14 is dewatered by a dewatering device 15 to form a fiber separator 101; the dewatering device 15 can extract water from the homogeneous slurry on the transfer wire 14, so that the slurry is formed into a solid state.
S5: drying and cooling, namely conveying the fiber separator 101 to a drying box 16 for drying, and conveying the dried fiber separator to a cooling device 17 for cooling; the drying box 16 may dry the moisture inside the fiber separator 101 to ensure the dryness of the fiber separator 101.
S6: and (4) winding, namely winding the cooled fiber separator 101 by using a winder 18.
As shown in fig. 2, the headbox 13 is positioned above the conveying wire 14, and the discharge opening of the headbox 13 is oriented in the same direction as the conveying direction of the conveying wire 14. The sedimentation tank 12 is located at one end of the feed inlet of the head box 13, the discharge port of the sedimentation tank 12 is communicated with the feed inlet of the head box 13 through a pipeline, the discharge port of the sedimentation tank 12 is provided with a pumping pump 121, and the slurry in the sedimentation tank 12 can be pumped into the head box 13 by the pumping pump 121. The dewatering device 15 is located below the conveying wire 14 and the dewatering device 15 is close to the discharge opening of the headbox 13. The drying box 16 is installed on the conveying net 14, the drying box 16 is positioned at one end of the dewatering device 15 far away from the head box 13, and the fiber partition board 101 dewatered and formed by the dewatering device 15 is dried by the drying box 16. The cooling device 17 is located at the end of the drying box 16 remote from the dewatering device 15, and the fiber separator 101 is cooled by the cooling device 17 in the drying box 16. A winder 18 is located at the tail of the transport web 14, with which winder 18 the formed fibre spacers 101 can be wound.
As shown in fig. 2, the dewatering device 15 includes three water-absorbing boxes 151, a vacuum pump 152, a water-absorbing pipe 153 and a water outlet pipe 154, the water-absorbing boxes 151 are rectangular and have a plurality of uniformly distributed holes on the top surface, the water-absorbing boxes 151 are located below the conveying net 14 for conveying the slurry, the length direction of the water-absorbing boxes 151 is perpendicular to the length direction of the conveying net 14, and the water-absorbing boxes 151 are uniformly distributed along the length direction of the conveying net 14; one end of the water suction pipe 153 is communicated with an air inlet pipe of the vacuum pump 152, and the other end thereof is divided into a plurality of branch pipes which are respectively communicated with the end parts of the water suction boxes 151; one end of the water outlet pipe 154 is communicated with the air outlet of the vacuum pump 152, the other end is communicated with the water inlet of the cooling device 17, and in addition, the water outlet pipe 154 is connected with a filter box 1541.
When the slurry passes above the water absorption box 151, the water absorption box 151 can extract water from the slurry on the conveying net 14 due to the vacuum pump 152 vacuumizing the water absorption box 151, so that the slurry can be solidified and the fiber separator 101 is formed; in addition, the extracted water is filtered by the filter cartridge 1541 to remove impurities from the water, and the filtered water is sent to the cooling device 17.
As shown in fig. 1 and 2, the cooling device 17 includes a first cooling pipe 171, a water pipe 172, a water storage 173, and a second cooling pipe 174. The first cooling tube 171 is coiled in a circle of the conveying net 14, the coiling direction of the first cooling tube 171 is consistent with the length direction of the first conveying net 14, a water inlet of the first cooling tube 171 is close to the drying box 16 and is communicated with a water outlet pipe 154 in the dewatering device 15, a water outlet of the first cooling tube 171 is communicated with a water conveying pipe 172, one end, far away from the first cooling tube 171, of the water conveying pipe 172 is communicated with a water storage tank 173, the water storage tank 173 is located on one side of the stirring kettle 11, the pipeline between the water storage tank 173 and the stirring kettle 11 is communicated, and the water outlet of the water storage tank 173 is connected with a valve 1731. The second cooling pipe 174 is wound around the circumference of the conveying net 14 and is arranged in a staggered manner with the first cooling pipe 171, high-pressure cooling water is connected to a water inlet of the second cooling pipe 174, the water inlet of the second cooling pipe 174 is positioned at one end far away from the drying box 16, a water outlet of the second cooling pipe 174 is close to the drying box 16 and is communicated with the water conveying pipe 172, and the water outlet of the second cooling pipe 174 is arranged at one end far away from the drying box 16, so that cooling water which does not absorb heat can still be input into a cooling pipeline far away from one end of the drying box 16, and the cooling effect of the cooling device 17 far away from one end of the drying box 16 can be improved; in addition, a heat insulation plate 161 is arranged between the water inlet of the first cooling pipe 171 and the drying box 16, and heat transfer in the drying box 16 to the cooling device 17 can be reduced by using the partition plate, so that influence on the cooling effect of the cooling device 17 can be reduced.
After the fiber separator 101 is dried at a high temperature, a cooling pipeline is formed by the first cooling pipe 171 and the second cooling pipe 174, so that the fiber separator 101 can be cooled, the mutual adhesion among the fiber separators 101 can be prevented, the damage to the fiber separator 101 can be reduced, and the product quality is ensured; in addition, the cooling water in the first cooling pipe 171 and the second cooling pipe 174 finally enters the water storage tank 173, and the water in the water storage tank 173 is used for making slurry, so that the waste of the cooling water can be reduced, and the effect of environmental protection is achieved.
As shown in fig. 3, a seasoning device 19 is provided between the cooling device 17 and the winder 18, and the seasoning device 19 includes a support frame 191, a fan 192, and a pressing roller 193. The support frame 191 is positioned at the tail part of the conveying net 14, and the support frames 191 are arranged on both sides of the fiber partition board 101; the fan 192 is fixedly connected to the end of the supporting frame 191, the fan 192 is located on one side of the fiber partition board 101, and the blowing direction of the fan 192 is perpendicular to the length direction of the fiber partition board 101; the number of the compression rollers 193 is four, the four compression rollers 193 are all rotatably arranged on the support frame 191, the four compression rollers 193 are arranged on two sides of the fan 192 in pairs, and the two compression rollers 193 on the same side of the fan 192 are close to each other and are positioned on the upper side surface and the lower side surface of the fiber partition board 101.
After the fiber separator 101 passes through the cooling device 17, cooling water dripping from the cooling device 17 is generated on the fiber separator 101, and when the fiber separator 101 passes through the air drying device 19, the fan 192 on the air drying device 19 blows air to the fiber separator 101, so that moisture on the fiber separator 101 can be taken away, and the fiber separator 101 is ensured to be dry; in addition, the pressing roller 193 can be used for pressing the fiber separator 101 of the air drying device 19, so that the movement of the fiber separator 101 caused by the blowing of the fan 192 can be reduced, and the orderly conveying of the fiber separator 101 is ensured.
The implementation principle of the production process of the superfine glass fiber separator in the embodiment of the application is as follows: after thick liquid dehydration shaping formed fibre baffle 101, can dry fibre baffle 101 once more through stoving case 16 to guarantee the inside dry shaping of fibre baffle 101, can get into cooling device 17 after the stoving is accomplished, because fibre baffle 101 is behind high temperature drying, the fibre cotton on surface has viscidity, cool off fibre baffle 101 this moment, can hinder bonding each other between the fibre baffle 101, and then be favorable to reducing and lead to the fact destruction to fibre baffle 101, guaranteed product quality.
The above are preferred embodiments of the present application, and the scope of protection of the present application is not limited thereto, so: all equivalent changes made according to the structure, shape and principle of the present application shall be covered by the protection scope of the present application.
Claims (4)
1. A production process of an ultrafine glass fiber separator is characterized by comprising the following steps:
s1: weighing raw materials, namely weighing preset purified water, glass fiber cotton, a fiber softening reinforcing agent and sulfuric acid;
s2: stirring and settling, namely putting the raw materials into a stirring kettle (11) for stirring, and conveying the raw materials to a settling pond (12) after stirring to finally form slurry;
s3: an upper wire, through which the stock solution flows onto a transport wire (14) through a headbox (13);
s4: dewatering forming, wherein the slurry on the conveying net (14) is dewatered by a dewatering device (15) to form a fiber separator (101);
s5: drying and cooling, namely conveying the fiber partition plate (101) to a drying box (16) for drying, and conveying the dried fiber partition plate to a cooling device (17) for cooling;
s6: winding, namely winding the cooled fiber separator (101) by using a winding machine (18);
the cooling device (17) comprises a first cooling pipe (171), a water conveying pipe (172) and a water storage tank (173), the first cooling pipe (171) is wound on the conveying net (14), the fiber partition plate (101) penetrates through the first cooling pipe (171), a water outlet of the first cooling pipe (171) is communicated with one end of the water conveying pipe (172), the other end of the water conveying pipe (172) is communicated with the water storage tank (173), a water outlet of the water storage tank (173) is communicated with a material inlet of the stirring kettle (11), and a water outlet of the water storage tank (173) is connected with a valve (1731);
the cooling device (17) further comprises a second cooling pipe (174), the second cooling pipe (174) is wound on the conveying net (14) and is arranged in a staggered mode with the first cooling pipe (171), high-pressure cooling water is connected to a water inlet of the second cooling pipe (174), and a water outlet of the second cooling pipe (174) is communicated with the water conveying pipe (172);
the water inlet of the second cooling pipe (174) and the water inlet of the first cooling pipe (171) are respectively positioned at two ends of the conveying net (14);
an air drying device (19) is arranged between the cooling device (17) and the winding machine (18), the air drying device (19) comprises support frames (191) located on two sides of the fiber partition plate (101) and a fan (192) fixedly connected to one end of each support frame (191), the fan (192) is located in the middle of one side edge of the fiber partition plate (101), and the wind direction of the fan (192) is perpendicular to the length direction of the fiber partition plate (101);
the air-drying device (19) further comprises four compression rollers (193) rotatably arranged on the supporting frame (191), the four compression rollers (193) are located on two sides of the fan (192) in pairs, and the fiber partition plate (101) penetrates through the compression rollers (193) on two sides of the fan (192).
2. The process for producing a microglass fiber separator as claimed in claim 1, wherein: dewatering device (15) are including absorbing water box (151), vacuum pump (152), absorb water tub (153) and outlet pipe (154), it is the cuboid form box body of top trompil to absorb water box (151), it is located to absorb water box (151) the below of carrying net (14), the one end of absorbing water tub (153) with the air inlet intercommunication of vacuum pump (152), the other end with absorb water box (151) inner chamber intercommunication, the one end of outlet pipe (154) with the gas outlet intercommunication of vacuum pump (152), the other end with the water inlet intercommunication of cooling tube (171).
3. The process for producing a microglass fiber separator as claimed in claim 2, wherein: the water outlet pipe (154) is connected with a filter box (1541).
4. The process for producing a microglass fiber separator as claimed in claim 1, wherein: and a heat insulation plate (161) is arranged between the first cooling pipe (171) and the drying box (16).
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| Application Number | Priority Date | Filing Date | Title |
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| CN202010725244.1A CN111851117B (en) | 2020-07-25 | 2020-07-25 | Production process of superfine glass fiber partition plate |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202010725244.1A CN111851117B (en) | 2020-07-25 | 2020-07-25 | Production process of superfine glass fiber partition plate |
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| CN111851117B true CN111851117B (en) | 2022-08-30 |
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| CN113972439A (en) * | 2021-11-29 | 2022-01-25 | 无锡明奥达铁路配件有限公司 | Process for manufacturing separator rolling circle |
| CN114643727A (en) * | 2022-02-17 | 2022-06-21 | 范小兰 | Uniform sizing and fiber aggregation prevention equipment for production of superfine glass fiber partition plate |
| CN117698182B (en) * | 2024-02-05 | 2024-04-26 | 张家港市天磊玻纤有限公司 | Control system for AGM partition plate machining process |
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| CN207685587U (en) * | 2017-12-13 | 2018-08-03 | 浙江畅通科技有限公司 | A kind of AGM splitter plate moldings machine |
| CN209523067U (en) * | 2018-09-20 | 2019-10-22 | 天津市盛世德新材料科技有限公司 | A kind of impregnated paper production cooling device and system of processing |
| CN109537347A (en) * | 2018-12-06 | 2019-03-29 | 青岛领军新材料科技创新园发展有限公司 | A kind of wet forming device of ultra-fine basalt fiber super thick fibrofelt |
| CN209428832U (en) * | 2018-12-28 | 2019-09-24 | 宜昌金兴新材料有限公司 | A kind of paper plant's dryer quickly cooling device |
| CN110757779A (en) * | 2019-10-22 | 2020-02-07 | 常州丰锦塑胶科技有限公司 | Foam pipe forming equipment |
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2020
- 2020-07-25 CN CN202010725244.1A patent/CN111851117B/en active Active
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