CN201744308U - Polytetrafluoroethylene membrane heat treating device capable of controlling shrinkage - Google Patents
Polytetrafluoroethylene membrane heat treating device capable of controlling shrinkage Download PDFInfo
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- CN201744308U CN201744308U CN 201020275791 CN201020275791U CN201744308U CN 201744308 U CN201744308 U CN 201744308U CN 201020275791 CN201020275791 CN 201020275791 CN 201020275791 U CN201020275791 U CN 201020275791U CN 201744308 U CN201744308 U CN 201744308U
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- poly tetrafluoroethylene
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Abstract
The utility model provides a device for performing thermal contraction on a polytetrafluoroethylene filter membrane which has been longitudinally stretched. By using the device, the shrinkage of the polytetrafluoroethylene filter membrane can be controlled with production cycle shortened, production efficiency enhanced, the longitudinal stress of the filter membrane eliminated, super fine fiber reduced and the strength and the air permeation rate of the filter membrane improved. The device comprises a heater body; an unwinding device which feeds the polytetrafluoroethylene membrane into the heater body in constant tension and constant linear velocity; a winding device which makes the polytetrafluoroethylene membrane out of the heater body in constant tension and constant linear velocity; the heating device inside the heater body; a plurality of driving rollers the polytetrafluoroethylene membrane sequentially rounds and a plurality of tension detecting devices for detecting the polytetrafluoroethylene membrane tension between any two adjacent driving rollers. Each driving roller is respectively connected with the output shaft of a variable frequency motor. Each tension detecting device output end is connected with a programmable controller which is connected with a frequency converter. And each frequency converter is connected with the variable frequency motor which is connected with the rear driving roller between two driving rollers.
Description
Technical field
The utility model relates to the processing and manufacturing equipment of polytetrafluoroethylene (PTFE) miillpore filter, belongs to the processing and manufacturing technical field of polytetrafluoroethylene (PTFE) miillpore filter, especially the manufacturing field of air filtration film, clothes film and water filtration poly tetrafluoroethylene.
Background technology
The manufacturing technology of expanded polytetrafluoroethylsealing miillpore filter, majority does not have this step process of heat treatment on the market.The manufacturing process of expanded polytetrafluoroethylsealing miillpore filter is as follows: at first the expanded polytetrafluoroethylsealing powder is proportioned into the paste shape with proper auxiliary agent oil, make cylindrical blank by blank shaper, that puts that the machine of pushing is extruded into certain diameter under certain pressure cylindricly enters calender through guider and is pressed into calendared sheet, then through vertically draw, expanding forms the expanded microporous polytetra fluoroethylene-EPTEE film that is the two-dimensional plane structure.After vertical the drawing, for eliminating the vertical stress that remains in when drawing on the polytetrafluoroethylene film, the method that placement a period of time shrinks naturally under the normal in the past employing normal temperature is to polytetrafluoroethylene film natrual ageing, natural aging time normally 1～2 day, consuming time very long, and natural contraction can only be eliminated the stress of vertical drawstring outer surface, and the stress of inner surface still exists, and the polytetrafluoroethylene film the when existence of stress can cause the next process cross directional stretch is inhomogeneous.
The utility model content
The purpose of this utility model provides the equipment that a kind of teflon membrane filter that longitudinal stretching is crossed carries out thermal contraction, utilize this equipment can control the amount of contraction of teflon membrane filter, shorten the production cycle, enhance productivity, stress on the elimination filter membrane is vertical, reduce the existence of superfine fibre, improve the intensity and the air penetrability of filter membrane.
The poly tetrafluoroethylene Equipment for Heating Processing of controlled controlling shrinkage mass of the present utility model comprises poly tetrafluoroethylene is sent into the unwinding device, body of heater of body of heater, poly tetrafluoroethylene pulled out the wrap-up of body of heater with the permanent linear speed of permanent tension force with the permanent linear speed of permanent tension force; Have a plurality of drive rolls that heater, poly tetrafluoroethylene are walked around successively in the body of heater.
The beneficial effect of equipment described in the utility model: the utility model is to adopt the mode of heat-treatment furnace heat shrink through the poly tetrafluoroethylene behind the longitudinal stretching, eliminate the stress on the poly tetrafluoroethylene, with respect to natrual ageing, can significantly shorten the production cycle, enhance productivity.The permanent linear speed control of permanent tension force is adopted in the utility model unwinding and rewinding, and each drive roll speed is stepless adjustable in the body of heater, according to the amount of contraction of setting, can reach predetermined contractive effect by drive roll speed ratio in the debugging body of heater.
Above-mentioned Equipment for Heating Processing, unwinding device comprise unreel motor, with unreel the let off roll that motor links to each other, be used to detect the unwinding tension checkout gear of the unwinding tension of poly tetrafluoroethylene, the output of unwinding tension checkout gear connects Programmable Logic Controller, and Programmable Logic Controller links to each other with the frequency converter that unreels that control unreels motor speed.
Above-mentioned Equipment for Heating Processing, wrap-up comprises winding motor, the wind-up roll that links to each other with winding motor, be used to detect the rolling tension detecting apparatus of the rolling tension force of poly tetrafluoroethylene, the output of rolling tension detecting apparatus connects Programmable Logic Controller, and Programmable Logic Controller links to each other with the rolling frequency converter of control winding motor rotating speed.
Above-mentioned Equipment for Heating Processing also comprises a plurality of tension detecting apparatus of the poly tetrafluoroethylene tension force between adjacent two drive rolls arbitrarily that are used to detect; Each drive roll links to each other with the output shaft of a variable-frequency motor respectively; The output of each tension detecting apparatus connects the Programmable Logic Controller that links to each other with frequency converter, each frequency converter be connected with the variable-frequency motor that links to each other of the drive roll in back in two drive rolls.
Description of drawings
Fig. 1 is the schematic diagram of Equipment for Heating Processing
Fig. 2 is the control principle figure of Equipment for Heating Processing
Fig. 3 is that the speed ratios such as drive roll in the Equipment for Heating Processing are adjusted schematic diagram
The specific embodiment
Referring to Fig. 1, the poly tetrafluoroethylene Equipment for Heating Processing of this controlled controlling shrinkage mass comprises unwinding device 100, body of heater 200, wrap-up 300, PLC, touch-screen HMI, frequency converter etc.
Wrap-up 300 comprises rolling variable-frequency motor, the wind-up roll 17 that links to each other with the rolling variable-frequency motor, carry-over pinch rolls 12,13,14, driven roll 16, comprise the rolling tension detecting apparatus of rolling tension force that is used to detect poly tetrafluoroethylene of the floating roller 15 of tension force, the output of unwinding tension checkout gear connects the rolling frequency converter of control rolling variable-frequency motor rotating speed.
Heat treatment body of heater 200 comprises case 18, is arranged on electric heating tube 19 and drive roll 5,6,7,8,9,10,11 in the case 18.Each drive roll links to each other with the variable-frequency motor that drives its rotation respectively, and each variable-frequency motor joins with the frequency converter of its rotating speed of control.
Participate in Fig. 2, PLC links to each other with touch-screen HMI, frequency converter (comprising the frequency converter of controlling each variable-frequency motor, the rolling frequency converter of control winding motor, the frequency converter that unreels that control unreels motor) etc. respectively.
Adopt the communication of fieldbus mode, distributed I/O system carries out the collection of spot sensor signal, and touch-screen is given PLC with the control signal transfer of data, realizes stepless speed regulation by sending to each Frequency Converter Control motor after the PLC analyzing and processing.
The control purpose of unwinding device is that permanent tension force, permanent linear speed initiatively unreel, unreeling control unreels frequency converter, the floating roller feedback of tension force etc. and constitutes closed-loop control system by unreeling variable-frequency motor, vector, the package amount of following the tracks of the vertical drawstring 101 on the let off roll is simulated by vector frequency converter and unreels rate curve, according to unreeling the tension feedback fair curve under the actual conditions, realize that permanent tension force, permanent linear speed initiatively unreel.
The working mechanism and the unwinding device of wrap-up are similar, unique different be that the rate curve that simulates of vector rolling frequency converter is logically opposite, unreel the motor speed curve and should be by little to big variation, the winding motor speed curves is by greatly to little variation.
This method is that all standard compliant vertical drawstring 101 of concrete specification requirement making according to the polytetrafluoroethylene (PTFE) miillpore filter is placed on the let off roll 1 of permanent tension force, permanent linear speed active unwinding device; These vertical drawstrings enter in the heat treatment body of heater 200 behind driven roll 2, the floating roller 3 of tension force, driven roll 4; 7 drive rolls 5,6,7,8,9,10,11 are arranged in the heat treatment body of heater 200, speed between every drive roll is successively decreased, vertical drawstring constantly shrinks between each drive roll of process, finally come out of the stove after the floating roller 15 of carry-over pinch rolls 12,13,14, tension force, driven roll 16 are rolled into heat treatment band 301 on wind-up roll 17.
Heat treatment body of heater 200 bottoms are equipped with electric heating tube 19, and the temperature control system that is made of temp controlled meter, controllable silicon, temperature sensor etc. guarantees that temperature range is adjustable at 100 ℃～200 ℃ in the body of heater.Vertical drawstring divides 6 sections strokes to shrink between drive roll 5,6,7,8,9,10,11 these 7 rollers, and each drive roll all has a variable-frequency motor and its rotating speed of Frequency Converter Control.
The asynchronism(-nization) that vertical drawstring is placed at a certain temperature, amount of contraction also are different.For the amount of contraction that realizes being scheduled to just must at first be determined the time that vertical drawstring moves in body of heater, but go out speed ratio between each drive roll according to decomposing ST rough calculation between each drive roll, and the amount of contraction between each drive roll is not even distribution under the actual conditions, for avoiding vertical drawstring pine or tension to occur at each drive roll, just must be optimized fine setting to the speed ratio between each drive roll, guaranteeing under the suitable tension force situation of vertical drawstring heat treatment process the control of realization amount of contraction and stable.
According to different shrinkage factor n% (referring to Fig. 3), can calculate corresponding rolling linear velocity V
2With unreel linear velocity V
1Ratio be 1-n%.Suppose that the shrinkage factor that the vertical drawstring of certain technology was deposited in T ℃ environment t minute is n%, the vertical stroke length overall of drawstring in body of heater is S rice, then unreels linear velocity V
1=(1+n%) S/t, rolling linear velocity V
2=V
1(1-n%), the linear resonance surface velocity of drive roll 5 with unreel linear velocity coupling, the linear resonance surface velocity of drive roll 11 and rolling linear velocity V
2Identical, the shrinkage factor of 6 sections strokes is the same in theory, and then the linear velocity ratio between each adjacent two drive roll is
The linear velocity of drive roll 6
The linear velocity of drive roll 7
By that analogy, but in fact because vertical drawstring has a process in the heating of body of heater inner surface, certainty is shunk fewly because self surface temperature is low at first, so shrinkage factor is different in the process that vertical drawstring moves on each drive roll in body of heater, in practical operation, usually adopting theoretic each roller linear velocity is reference, the direction that enters body of heater with vertical drawstring is a starting point, adjust the linear velocity of each roller from front to back successively, make 6 strokes that certain overfeed ratio all be arranged, avoid because vertical drawstring crosses pine on 6 strokes or tension influences product quality.
Embodiment 1-30:
Selected expanded polytetrafluoroethylsealing powder powder molecular weight is 8,000,000, and used finish is an Isopar M type oil.Vertical drawstring width 170mm, thickness 141.7 μ m; Length 600m.To indulge the permanent linear speed of the permanent tension force of drawstring with unwinding device and enter body of heater through driven roll 2, the floating roller 3 of tension force, driven roll 4, and pass through the identical drive roll of diameter 5,6,7,8,9,10,11 successively, each drive roll rotating speed sees Table 1.Temperature relies on the speed ratio of each drive roll to shrink for down in the vertical different bodies of heater of drawstring in table 1, again through carry-over pinch rolls 12,13,14 tractions, and rolling behind the floating roller 15 control tension force of tension force.The poly tetrafluoroethylene width of rolling, length, length shrinkage factor see Table 1.
This patent is to adopt the mode of heat-treatment furnace heat shrink through the poly tetrafluoroethylene behind the longitudinal stretching, to eliminate the stress on the poly tetrafluoroethylene.The permanent linear speed control of permanent tension force is adopted in unwinding and rewinding, divides multistage to shrink in the body of heater, and each drive roll speed is stepless adjustable in the body of heater, according to the amount of contraction of setting, can reach predetermined effect by drive roll speed ratio in the debugging body of heater.The utility model aims to provide production technology and the equipment that the teflon membrane filter that longitudinal stretching is crossed carries out thermal contraction, utilize this method can pass through the amount of contraction of control teflon membrane filter, stress on the elimination filter membrane is vertical, reduce the existence of superfine fibre, improve the intensity and the air penetrability of filter membrane.
Table 1:
Claims (4)
1. the poly tetrafluoroethylene Equipment for Heating Processing of a controlled controlling shrinkage mass is characterized in that: it comprises sends into poly tetrafluoroethylene the unwinding device, body of heater of body of heater, poly tetrafluoroethylene is pulled out the wrap-up of body of heater with the permanent linear speed of permanent tension force with the permanent linear speed of permanent tension force; Have a plurality of drive rolls that heater, poly tetrafluoroethylene are walked around successively in the body of heater.
2. Equipment for Heating Processing as claimed in claim 1, it is characterized in that: unwinding device comprise unreel motor, with unreel the let off roll that motor links to each other, be used to detect the unwinding tension checkout gear of the unwinding tension of poly tetrafluoroethylene, the output of unwinding tension checkout gear connects Programmable Logic Controller, and Programmable Logic Controller links to each other with the frequency converter that unreels that control unreels motor speed.
3. Equipment for Heating Processing as claimed in claim 1 it is characterized in that: further comprising a plurality of tension detecting apparatus of the poly tetrafluoroethylene tension force between adjacent two drive rolls arbitrarily that are used to detect; Each drive roll links to each other with the output shaft of a variable-frequency motor respectively; The output of each tension detecting apparatus connects the Programmable Logic Controller that links to each other with frequency converter, each frequency converter be connected with the variable-frequency motor that links to each other of the drive roll in back in two drive rolls.
4. Equipment for Heating Processing as claimed in claim 1, it is characterized in that: wrap-up comprises winding motor, the wind-up roll that links to each other with winding motor, be used to detect the rolling tension detecting apparatus of the rolling tension force of poly tetrafluoroethylene, the output of rolling tension detecting apparatus connects Programmable Logic Controller, and Programmable Logic Controller links to each other with the rolling frequency converter of control winding motor rotating speed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201020275791 CN201744308U (en) | 2010-07-28 | 2010-07-28 | Polytetrafluoroethylene membrane heat treating device capable of controlling shrinkage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201020275791 CN201744308U (en) | 2010-07-28 | 2010-07-28 | Polytetrafluoroethylene membrane heat treating device capable of controlling shrinkage |
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| Publication Number | Publication Date |
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| CN201744308U true CN201744308U (en) | 2011-02-16 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201020275791 Expired - Fee Related CN201744308U (en) | 2010-07-28 | 2010-07-28 | Polytetrafluoroethylene membrane heat treating device capable of controlling shrinkage |
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|---|---|
| CN (1) | CN201744308U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101905124A (en) * | 2010-07-28 | 2010-12-08 | 中材科技股份有限公司 | Heat treatment equipment and method capable of controlling shrinkage mass of polytetrafluoroethylene membrane |
| CN102514186A (en) * | 2012-01-05 | 2012-06-27 | 四川省资阳市雅之江塑业有限公司 | Tensile drying oven for producing strip media |
| CN103359540A (en) * | 2012-03-31 | 2013-10-23 | 北京纺机所装备技术有限公司 | Traction and tension control device for arranging tows |
-
2010
- 2010-07-28 CN CN 201020275791 patent/CN201744308U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101905124A (en) * | 2010-07-28 | 2010-12-08 | 中材科技股份有限公司 | Heat treatment equipment and method capable of controlling shrinkage mass of polytetrafluoroethylene membrane |
| CN101905124B (en) * | 2010-07-28 | 2013-09-25 | 中材科技股份有限公司 | Heat treatment equipment and method capable of controlling shrinkage mass of polytetrafluoroethylene membrane |
| CN102514186A (en) * | 2012-01-05 | 2012-06-27 | 四川省资阳市雅之江塑业有限公司 | Tensile drying oven for producing strip media |
| CN103359540A (en) * | 2012-03-31 | 2013-10-23 | 北京纺机所装备技术有限公司 | Traction and tension control device for arranging tows |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110216 Termination date: 20150728 |
|
| EXPY | Termination of patent right or utility model |