CN207987376U - A kind of Novel polyester filament production system - Google Patents
A kind of Novel polyester filament production system Download PDFInfo
- Publication number
- CN207987376U CN207987376U CN201820243121.2U CN201820243121U CN207987376U CN 207987376 U CN207987376 U CN 207987376U CN 201820243121 U CN201820243121 U CN 201820243121U CN 207987376 U CN207987376 U CN 207987376U
- Authority
- CN
- China
- Prior art keywords
- lower section
- blow box
- manifold
- screw extruder
- ring blow
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 13
- 229920000728 polyester Polymers 0.000 title claims abstract description 13
- 238000004804 winding Methods 0.000 claims abstract description 8
- 239000002245 particle Substances 0.000 claims abstract description 4
- 238000007654 immersion Methods 0.000 claims description 15
- 238000009826 distribution Methods 0.000 claims description 9
- 238000001514 detection method Methods 0.000 claims description 4
- 239000003381 stabilizer Substances 0.000 claims description 4
- 238000003860 storage Methods 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 238000009987 spinning Methods 0.000 abstract description 13
- 239000004594 Masterbatch (MB) Substances 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 2
- 230000009286 beneficial effect Effects 0.000 abstract 1
- 238000005485 electric heating Methods 0.000 description 7
- 238000001816 cooling Methods 0.000 description 3
- 238000000578 dry spinning Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000004753 textile Substances 0.000 description 2
- 229920004934 Dacron® Polymers 0.000 description 1
- 229920004933 Terylene® Polymers 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Abstract
The utility model is related to experimental branch line technical fields,Disclose a kind of Novel polyester filament production system,Including screw extruder,Controller,The top of the screw extruder is equipped with feed hopper,The discharge port of the screw extruder is connected to by feeding pipe with the feed end of filter screen,The discharge end of the filter screen is connected to by feeding pipe with the feed end of metering pump,The discharge end of the metering pump is connected to by feeding pipe with the feed end of manifold,The lower section of the manifold is ring blow box,The lower section of the ring blow box is equipped with drafting tube,The lower section of the drafting tube is equipped with buncher,The lower section of the buncher is equipped with winding device,The feed hopper is internally provided with casing,The left side of the ring blow box is equipped with air inlet,The air inlet is connected to by gas pipeline with wind turbine,The input end of the wind turbine is equipped with high efficiency particle air filter.The utility model has the beneficial effects that Masterbatch is contributed to be mixed with slice, spinning effect is good.
Description
Technical field
The utility model is related to experimental branch line technical field, especially a kind of Novel polyester filament production system.
Background technology
Terylene is as one of three big main force's fibers in synthetic fibers, because its excellent material and chemical characteristic are answered extensively
For garment material and other non-garment industries.Dacron product since the advent of the world is also once dangled with it, intensity is high, is not easy
It wrinkles and all kinds of textiles is weaved as textile raw material by downstream user.
Polyester filament generally uses dry spinning to prepare, and traditional dry spinning refers to polymer melt from spinneret capillary
The spinning solution thread extruded in hole enters in spinning shaft, by the effect of stream of hot air in path, makes molten in stoste thread
Agent is quickly volatilized, and the solvent vapo(u)r evaporated is taken away by stream of hot air, and stoste is cured while gradually sloughing solvent,
And elongation attenuates and forms as-spun fibre under the action of winding tension.Traditional dry spinning apparatus structure is complicated, and operation is numerous
Trivial, installation and repair are inconvenient and of high cost, and wire vent is inefficient, and when spinning color silk, and Masterbatch mixing is uneven,
Seriously affect the color of color silk.
Utility model content
Purpose of the utility model is to solve the above problems, devise a kind of Novel polyester filament production system.
Realize that above-mentioned purpose the technical solution of the utility model is a kind of Novel polyester filament production system, including screw rod
The top of extruder, controller, the screw extruder is equipped with feed hopper, and the discharge port of the screw extruder passes through conveying pipeline
Road is connected to the feed end of filter screen, and the discharge end of the filter screen is connected to by feeding pipe with the feed end of metering pump, institute
The discharge end for stating metering pump is connected to by feeding pipe with the feed end of manifold, and the lower section of the manifold is ring blow box,
The lower section of the ring blow box is equipped with drafting tube, and the lower section of the drafting tube is equipped with buncher, and the lower section of the buncher is equipped with
Winding device, the feed hopper are internally provided with casing, and the lower part of described sleeve pipe sets that there are three the inner walls of stabilizer blade and feed hopper to connect
It connects, the left and right sides of the manifold is equipped with electric heating tube, and filter layer, deflector and spray are equipped with successively up and down in the manifold
The left side of filament plate, the ring blow box is equipped with air inlet, and the air inlet is connected to by gas pipeline with wind turbine, the wind turbine
Input end is equipped with high efficiency particle air filter, and air storage chamber and distribution plate, the gas outlet of the distribution plate are equipped in the ring blow box
Place is equipped with pressure detection instrument.
Further, the winding device includes the immersion cell being arranged in order, draw roll and take-up roll, in the immersion cell
Equipped with immersion oil roller, the take-up roll is set on supporting rack.
Further, it is additionally provided with Xelminator between the buncher and immersion cell.
Further, described sleeve pipe is hollow sleeve, and the ring blow box is annular.
A kind of Novel polyester filament production system made using the technical solution of the utility model, advantage are existed
In：1, it is equipped with casing in feed hopper, for adding Masterbatch in casing, Masterbatch is made to enter screw rod be sliced ratio uniform
In extruder；2, the temperature of the spinning solution in manifold can be ensured by electric heating tube being equipped in manifold, prevent spinning solution
Physical change is conducive to spinning；3, distribution plate being equipped in ring blow box can uniformly blow to cooling wind on tow, ad hoc to have electrostatic
Arrester can prevent tow from generating electrostatic during subsequent production.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the vertical view of feed pipe in the utility model；
In figure, 1, screw extruder；2, controller；3, feed hopper；4, discharge port；5, feeding pipe；6, filter screen；7, it counts
Amount pump；8, manifold；9, ring blow box；10, drafting tube；11, buncher；12, casing；13, stabilizer blade；14, electric heating tube；15、
Filter layer；16, draining plate；17, spinneret；18, air inlet；19, gas pipeline；20, wind turbine；21, high efficiency particulate air filter；22, it stores up
Gas chamber；23, distribution plate；24, pressure detector；25, immersion cell；26, draw roll；27, take-up roll；28, immersion oil roller；29, it supports
Frame；30, Xelminator.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
The every other embodiment obtained, shall fall within the protection scope of the present invention.
The utility model provides a kind of Novel polyester filament production system as shown in Figs. 1-2, including screw extruder
1, the top of controller 2, the screw extruder 1 is equipped with feed hopper 3, and the discharge port 4 of the screw extruder 1 passes through conveying pipeline
Road 5 is connected to the feed end of filter screen 6, and the discharge end of the filter screen 6 is connected by the feed end of feeding pipe 5 and metering pump 7
Logical, the discharge end of the metering pump 7 is connected to by feeding pipe 5 with the feed end of manifold 8, and the lower section of the manifold 8 is
The lower section of ring blow box 9, the ring blow box 9 is equipped with drafting tube 10, and the lower section of the drafting tube 10 is equipped with buncher 11, described
The lower section of buncher 11 is equipped with winding device, and the feed hopper 3 is internally provided with casing 12, and the lower part of described sleeve pipe 12 is equipped with three
A stabilizer blade 13 is connect with the inner wall of feed hopper 3, and the left and right sides of the manifold 8 is equipped with electric heating tube 14, and electric heating tube 14 is right
Manifold 8 is internally heated, and prevents spinning solution cooling from influencing spinning, filter layer 15 is equipped with successively up and down in the manifold 8,
The left side of deflector 16 and spinneret 17, the ring blow box 9 is equipped with air inlet 18, and the air inlet 18 passes through gas pipeline 19
It is connected to wind turbine 20, the input end of the wind turbine 20 is equipped with high efficiency particle air filter 21, and air storage chamber is equipped in the ring blow box 9
22 and distribution plate 23, pressure detection instrument 24 is equipped at the gas outlet of the distribution plate 23.
Preferably, the winding device includes the immersion cell 25 being arranged in order, draw roll 26 and take-up roll 27, the immersion oil
Immersion oil roller 28 is equipped in slot 25, the take-up roll 27 is set on supporting rack 29.
Preferably, Xelminator 30 is additionally provided between the buncher 11 and immersion cell 25.
Preferably, described sleeve pipe 12 is hollow sleeve, and the ring blow box 9 is annular, and distribution plate 23 is obliquely installed, inclines
Tilted direction is identical as the direction of tow, when using Masterbatch be added in screw extruder 1 from casing 12 so that spinning chips with
The ratio of Masterbatch addition is a kind of, improves Masterbatch and slice mixture homogeneity.
Wherein screw extruder 1, metering pump 7, electric heating tube 14, wind turbine 20, pressure detection instrument 24 are electrical with controller 2
Connection（Belonging to the prior art, details are not described herein）.
When specifically used：Surrounding that spinning chips are open from feed hopper 3 enters, and Masterbatch is from the casing 12 in feed inlet 3
In enter in screw extruder 1, by the melt extruded of screw extruder 1, spun by entering after filter screen 6 and metering pump 7
Silk case 8 starts spinning, and the side of manifold 8 is equipped with the temperature that electric heating tube 14 maintains spinning melt, tow lead to ring blow box 9 into
Row cooling, then carries out drawing-off by drafting tube 10, then by immersion cell 25, is rolled up in take-up roll 27 after draw roll 26
Around being ready for subsequent processing
Finally it should be noted that：The above descriptions are merely preferred embodiments of the present invention, is not limited to this
Utility model, although the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art
For, it still can be with technical scheme described in the above embodiments is modified, or to which part technical characteristic
Equivalent replacement is carried out, within the spirit and principle of the utility model, any modification, equivalent replacement, improvement and so on,
It should be included within the scope of protection of this utility model.
Claims (4)
1. a kind of Novel polyester filament production system, including screw extruder, controller, are characterized in that, the screw extruder
Top be equipped with feed hopper, the discharge port of the screw extruder is connected to by feeding pipe with the feed end of filter screen, described
The discharge end of filter screen is connected to by feeding pipe with the feed end of metering pump, and the discharge end of the metering pump passes through feeding pipe
It being connected to the feed end of manifold, the lower section of the manifold is ring blow box, and the lower section of the ring blow box is equipped with drafting tube,
The lower section of the drafting tube is equipped with buncher, and the lower section of the buncher is equipped with winding device, and the feed hopper is internally provided with
The lower part of casing, described sleeve pipe is set there are three the connection of the inner wall of stabilizer blade and feed hopper, and the left and right sides of the manifold is equipped with electricity
Heating tube, is equipped with filter layer, deflector and spinneret in the manifold successively up and down, the left side of the ring blow box be equipped with into
Gas port, the air inlet are connected to by gas pipeline with wind turbine, and the input end of the wind turbine is equipped with high efficiency particle air filter, described
It is equipped with air storage chamber and distribution plate in ring blow box, pressure detection instrument is equipped at the gas outlet of the distribution plate.
2. a kind of Novel polyester filament production system according to claim 1, which is characterized in that the winding device includes
Immersion cell, draw roll and the take-up roll being arranged in order, immersion oil roller is equipped in the immersion cell, and the take-up roll is set to supporting rack
On.
3. a kind of Novel polyester filament production system according to claim 2, which is characterized in that the buncher and immersion oil
Xelminator is additionally provided between slot.
4. a kind of Novel polyester filament production system according to claim 3, which is characterized in that described sleeve pipe is hollow sleeve
Pipe, the ring blow box are annular.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820243121.2U CN207987376U (en) | 2018-02-11 | 2018-02-11 | A kind of Novel polyester filament production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820243121.2U CN207987376U (en) | 2018-02-11 | 2018-02-11 | A kind of Novel polyester filament production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207987376U true CN207987376U (en) | 2018-10-19 |
Family
ID=63824401
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820243121.2U Expired - Fee Related CN207987376U (en) | 2018-02-11 | 2018-02-11 | A kind of Novel polyester filament production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207987376U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111020730A (en) * | 2019-11-26 | 2020-04-17 | 浙江及时宇特种纤维科技有限公司 | Low-melting-point polyester thermal fuse preparation equipment and process |
| CN111235716A (en) * | 2020-01-09 | 2020-06-05 | 晏庆光 | Fibril heating machine of polyester fiber spinning process |
-
2018
- 2018-02-11 CN CN201820243121.2U patent/CN207987376U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111020730A (en) * | 2019-11-26 | 2020-04-17 | 浙江及时宇特种纤维科技有限公司 | Low-melting-point polyester thermal fuse preparation equipment and process |
| CN111020730B (en) * | 2019-11-26 | 2021-02-05 | 浙江及时宇特种纤维科技有限公司 | Low-melting-point polyester thermal fuse preparation equipment and process |
| CN111235716A (en) * | 2020-01-09 | 2020-06-05 | 晏庆光 | Fibril heating machine of polyester fiber spinning process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181019 |