CN106480514A - A kind of low energy consumption fiber product preparation method - Google Patents
A kind of low energy consumption fiber product preparation method Download PDFInfo
- Publication number
- CN106480514A CN106480514A CN201610652310.0A CN201610652310A CN106480514A CN 106480514 A CN106480514 A CN 106480514A CN 201610652310 A CN201610652310 A CN 201610652310A CN 106480514 A CN106480514 A CN 106480514A
- Authority
- CN
- China
- Prior art keywords
- masterbatch
- screw extruder
- feeding barrel
- spinneret
- melt
- 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.)
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Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D1/00—Treatment of filament-forming or like material
- D01D1/04—Melting filament-forming substances
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D1/00—Treatment of filament-forming or like material
- D01D1/06—Feeding liquid to the spinning head
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D1/00—Treatment of filament-forming or like material
- D01D1/06—Feeding liquid to the spinning head
- D01D1/065—Addition and mixing of substances to the spinning solution or to the melt; Homogenising
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/10—Other agents for modifying properties
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/10—Other agents for modifying properties
- D01F1/106—Radiation shielding agents, e.g. absorbing, reflecting agents
Abstract
The invention discloses a kind of low energy consumption fiber product preparation method, comprises the steps：First polyester master particle is put into masterbatch drying machine to be dried, secondly after drying, the Masterbatch of polyester master particle and interpolation prepares spinning melt in screw extruder, then melt is extruded into melt stream by spinneret assembly, connected by transfer pipeline between the masterbatch drying machine and screw extruder, melt is sent to spinneret assembly through measuring pump by the screw extruder, the masterbatch drying machine is provided with one, the screw extruder and spinneret assembly arrange at least two groups, the transfer pipeline includes a main line and some branch lines that is drawn by main line, the main line is connected with masterbatch drying machine, the outlet of the branch line is connected with the feed hopper of each screw extruder, the feed hopper of the screw extruder is also associated with Masterbatch metered dispensing unit.The present invention is convenient, and the individual demand for different small lot clients is produced, it is to avoid excessive energy resource consumption.
Description
Present patent application is a kind of divisional application of invention and created name " melt spinning production technology ", original application
The applying date is August in 2014 26, Application No. 2014104239806.
Technical field
The present invention relates to melt spinning production technology.
Background technology
General melt spinning production equipment includes masterbatch drying machine, screw extruder and spinneret assembly, and master batch dries
By the connection of transfer pipeline between machine and screw extruder, the polyester granulate dry through masterbatch drying machine is through transfer pipeline
Transmit to screw extruder, melt is sent to spinneret assembly through measuring pump by screw extruder.Which is applied to large-scale batch
Quantify production, but for the individual demand of different small lot clients, which need also exist for all devices production is started,
It is well known, however, that production of chemical fibres is highly energy-consuming, production is carried out using this equipment and cause great energy waste.
In addition, for using in the fiber product on autumn in summer clothes, not only needing comfortable ventilating, and need to meet
Antiultraviolet and the demand of mosquito proof.
Content of the invention
The technical problem to be solved is exactly to provide a kind of low energy consumption fiber product preparation method, convenient for not
The individual demand of same small lot client is produced, it is to avoid excessive energy resource consumption, while making the fiber product that produces
Meet the demand of comfortable ventilating, antiultraviolet and mosquito proof.
For solving above-mentioned technical problem, the present invention is adopted the following technical scheme that：A kind of low energy consumption fiber product preparation method,
Comprise the steps：Secondly first polyester master particle is put into masterbatch drying machine to be dried, polyester master particle and interpolation after drying
Masterbatch prepares spinning melt in screw extruder, and then melt is extruded into melt stream by spinneret assembly, described
Connected by transfer pipeline between masterbatch drying machine and screw extruder, melt is sent to by the screw extruder through measuring pump
Spinneret assembly, the spinneret assembly include spinneret, and the spinneret is provided with the perseverance of several tapered radial distributions
The thin footpath spinneret orifice of set aperture, the masterbatch drying machine are provided with one, the screw extruder and spinneret assembly arrange to
Few two groups, the transfer pipeline includes a main line and some branch lines that is drawn by main line, the main line and mother
Grain drying machine connection, the outlet of the branch line are connected with the feed hopper of each screw extruder, the screw extruder
Feed hopper is also associated with Masterbatch metered dispensing unit, and the Masterbatch metered dispensing unit includes the feeding being sequentially connected
Bucket, blank cylinder, material blanking tube and online weighing conveying device, be provided with the blank cylinder by Masterbatch again cutting cutting dress
Put, the discharging opening of the material blanking tube is provided with striker plate, the striker plate is opened and closed by the control of online weighing conveying device, the color masterbatch
Grain includes activated carbon masterbatch, uvioresistant masterbatch and mosquito-proof masterbatch；The blank cylinder includes cylinder, and the cylinder enters
Mouth is provided with import flashboard, and the cartridge outlet is provided with outlet flashboard, and the inner barrel is provided with blank roller, the thin footpath spinneret orifice
Entrance point be provided with tapered inlet, the spinneret is provided with the guiding import of taper in spinneret orifice inlet side, thin footpath spinneret orifice
Tapered inlet is connected with guiding import.
Preferably, the feeding barrel is obliquely installed, and the bottom of the feeding barrel is provided with a rotating disk, and the feeding bottom of the barrel exists
Low level side extreme lower position is provided with a discharge nozzle, and the feeding barrel is provided with one from the high-order lateral low level side of feeding barrel below bung
The feed pipe of extension, the entrance point of the feed pipe are passed from feeding barrel, and the port of export of the feed pipe is near the low of feeding barrel
Position side inner barrel wall.
Preferably, on the bung of the feeding barrel, capping has glass cover, and the bung end face high position side centre position is provided with
Bearing pin, the glass cover are hinged on bearing pin.
Preferably, the feeding barrel is inversed taper platform shape cylinder, and the angle of inclination of the feeding barrel is 45 degree, outside the feeding barrel
Bucket wall is provided with the connecting tube passed through for feed pipe, and the connecting tube is provided with screw and is fixed feed pipe with connecting tube.
Preferably, the material blanking tube is obliquely installed, and the material blanking tube is made up of multistage differing tilt angles sectional pipe, multistage
The angle of inclination of sectional pipe gradually reduces from high to low.
Present invention optimizes melt spinning production equipment and process, by the conveying between masterbatch drying machine and screw extruder
Pipeline is divided into a main line and some branch lines that is drawn by main line, while it is multigroup only to arrange a masterbatch drying machine
The dry polyester master particle of screw extruder and spinneret assembly supply, as such, it is possible to be simultaneous for different small lot clients'
Individual demand is produced.And larger and uneven according to the Masterbatch grain diameter of actually supplier supply, in small batches
The not high problem of precision is added in amount production, and the present invention further improves Masterbatch metered dispensing unit, on the one hand passes through blank
The cutting device arranged in cylinder carries out cutting homogenizing to Masterbatch, on the other hand by the blanking of progressively reduction of speed, makes online weighing
Conveying device more uniform can receive blanking and carry out accurate Weighing, once reach the Masterbatch quality of setting, i.e.,
Material blanking tube is closed rapidly by striker plate, while online weighing conveying device conveys color masterbatch to the feed hopper of screw extruder
Grain.
In addition, activated carbon masterbatch, uvioresistant masterbatch and mosquito-proof masterbatch in production technology of the present invention, is added with,
The interpolation of activated carbon masterbatch can make fabric more comfortable ventilating, and the interpolation of uvioresistant masterbatch and mosquito-proof masterbatch is then
Fabric can be made to meet the requirement of antiultraviolet and mosquito proof.
Description of the drawings
The invention will be further described with reference to the accompanying drawings and detailed description：
Fig. 1 is the general structure schematic diagram of the present invention；
Fig. 2 is the structural representation of Masterbatch metered dispensing unit；
Fig. 3 is feeding barrel structural representation；
Fig. 4 is staving and the feed pipe attachment structure schematic diagram of feeding barrel；
Fig. 5 is the partial structural diagram of spinneret.
Specific embodiment
Embodiments of the invention are illustrated below in conjunction with Fig. 1 and 5.
As shown in figure 1, a kind of melt spinning production equipment, including masterbatch drying machine 2, screw extruder 4 and spinning head group
Part 6, is connected by transfer pipeline 3 between the masterbatch drying machine and screw extruder, and melt is passed through by the screw extruder 4
Measuring pump 5 is sent to spinneret assembly 6.
Wherein, masterbatch drying machine 2 is provided with one, and screw extruder 4 and spinneret assembly 6 arrange at least two groups, multigroup
Screw extruder 4 and spinneret assembly Unit 6 are arranged parallel, and the transfer pipeline 3 includes a main line 31 and by main line
The some branch lines 32 that draws, the main line are connected with masterbatch drying machine, and the outlet of the branch line is squeezed with each screw rod
The feed hopper connection of press.
Melt spinning production equipment is optimized, the transfer pipeline between masterbatch drying machine and screw extruder is divided into one
Main line and some branch lines that is drawn by main line, at the same only arrange masterbatch drying machine be multigroup screw extruder and
The dry polyester master particle of spinneret assembly supply, as such, it is possible to the individual demand for being simultaneous for different small lot clients enters
Row production.
And the feed hopper of screw extruder 4 is also associated with Masterbatch metered dispensing unit 1, as shown in Fig. 2 the color masterbatch
Grain metered dispensing unit 1 includes feeding barrel 11, blank cylinder 12, material blanking tube 13 and the online weighing conveying device being sequentially connected
14, it is provided with the cutting device of Masterbatch cutting again in the blank cylinder, the discharging opening of the material blanking tube is provided with striker plate, institute
State striker plate to be opened and closed by conveying device control of weighing.
The blank cylinder includes cylinder, and the cylinder import is provided with import flashboard, and the cartridge outlet is provided with outlet flashboard,
The inner barrel is provided with blank roller.Import flashboard is opened every time, and outlet flashboard cuts out, and after charging in cylinder is suitable, is closed
Import flashboard is closed, then blank roller is started working, and after the completion of blank, outlet flashboard is opened, to material blanking tube blanking.
The material blanking tube is obliquely installed, and the material blanking tube is made up of multistage differing tilt angles sectional pipe, multistage sectional pipe
Angle of inclination by height gradually reduce on earth.
Larger and uneven according to the Masterbatch grain diameter of actually supplier supply, small lot batch manufacture adds precision not
High problem, Masterbatch metered dispensing unit further improve, on the one hand the cutting device pair by arranging in blank cylinder
Masterbatch carries out cutting homogenizing, on the other hand by the blanking of progressively reduction of speed, enables online weighing conveying device more uniform
Receive blanking and accurate Weighing is carried out, once the Masterbatch quality of setting is reached, i.e., close by striker plate rapidly
Expects pipe, while online weighing conveying device conveys Masterbatch to the feed hopper of screw extruder.
The feeding barrel 11 is obliquely installed, and the feeding barrel includes staving 111, and feeding bottom of the barrel is provided with a rotating disk 114, turns
Disk controls rotation by the motor 115 below feeding barrel, and the feeding bottom of the barrel is provided with a discharge nozzle in low level side extreme lower position
113, the feeding barrel is provided with a feed pipe 112 extended from the high-order lateral low level side of feeding barrel below bung, described enter
The entrance point of expects pipe is passed from feeding barrel, and the port of export of the feed pipe is near the low level side inner barrel wall of feeding barrel.
As feeding barrel is obliquely installed, and as feed pipe stretches into feeding barrel, the feed pipe port of export from high-order side
Near feeding barrel low level side inner barrel wall, thus Masterbatch quantity in feeding barrel can be controlled to remain at certain height, while
Slowly run due to being provided with rotating disk in feeding bottom of the barrel, it is ensured that discharging is smooth, makes discharge nozzle be difficult to result in blockage.
In addition, capping has glass cover on the bung of the feeding barrel, the bung end face high position side centre position is provided with pin
Axle, the glass cover are hinged on bearing pin.It is easy to the situation that observes and control in feeding barrel.The feeding barrel is inversed taper platform shape
Cylinder, the angle of inclination of the feeding barrel is 45 degree, is so provided with beneficial to blanking.The feeding barrel outer barrel wall is provided with and supplies feed pipe
The connecting tube 116 for passing through, the connecting tube are provided with screw 117 and are fixed feed pipe with connecting tube.So feed pipe can be relative
Feeding barrel does expanding-contracting action and fixes, so as to adjust the quantity for entering Masterbatch in feeding barrel.
The spinneret assembly includes spinneret 61, and the spinneret is provided with the constant of several tapered radial distributions
The thin footpath spinneret orifice 611 in aperture, the entrance point of the thin footpath spinneret orifice are provided with tapered inlet 612, and the spinneret is in spinneret orifice
Inlet side is provided with the guiding import 613 of taper, and the tapered inlet of thin footpath spinneret orifice is connected with guiding import.The tapered inlet
The ratio 1.01～20 of the sectional area of import sectional area and thin footpath spinneret orifice:1.The aperture of the thin footpath spinneret orifice be 0.5～2mm,
Draw ratio 5～15:1.At thin footpath die orifice exit end the spacer holes of adjacent thin footpath spinneret orifice away from for thin footpath spinneret orifice diameter 0～
35%.
Melt spinning production technology, comprises the steps：First polyester master particle is put into masterbatch drying machine to be dried, its
After secondary drying, the Masterbatch of polyester master particle and interpolation prepares spinning melt in screw extruder, and then melt passes through spinning head group
Part is extruded into melt stream.
Specifically, Masterbatch includes activated carbon masterbatch, uvioresistant masterbatch and mosquito-proof masterbatch.Therein mosquito-proof
Masterbatch can be using Masterbatch, and activated carbon color masterbatch disclosed in the Chinese invention patent of Application No. 201310738611.1
Grain, uvioresistant masterbatch then commercially can be purchased, in addition, the addition of Masterbatch is routinely, as various colors
Ratio between master batch can be added with equal proportion, it is also possible to according to circumstances take the circumstances into consideration to increase and decrease, certainly, according to the need of other functions
Ask, it is also possible to add the master batch of other functions again.
Claims (5)
1. a kind of low energy consumption fiber product preparation method, comprises the steps：First polyester master particle is put into masterbatch drying machine to enter
Row drying, after secondly drying, the Masterbatch of polyester master particle and interpolation prepares spinning melt in screw extruder, and then melt leads to
Cross spinneret assembly and melt stream be extruded into, connected by transfer pipeline between the masterbatch drying machine and screw extruder,
Melt is sent to spinneret assembly through measuring pump by the screw extruder, and the spinneret assembly includes spinneret, the spray
Filament plate is provided with the thin footpath spinneret orifice in the constant aperture of several tapered radial distributions, it is characterised in that：The master batch dries
Machine is provided with one, and the screw extruder and spinneret assembly arrange at least two groups, and the transfer pipeline includes a supervisor
Road and some branch lines that is drawn by main line, the main line are connected with masterbatch drying machine, the outlet of the branch line
It is connected with the feed hopper of each screw extruder, the feed hopper of the screw extruder is also associated with Masterbatch metering distribution dress
Put, the Masterbatch metered dispensing unit includes feeding barrel, blank cylinder, material blanking tube and the online weighing conveying dress being sequentially connected
Put, be provided with the cutting device of Masterbatch cutting again in the blank cylinder, the discharging opening of the material blanking tube is provided with striker plate, institute
State striker plate to be opened and closed by the control of online weighing conveying device, the Masterbatch includes activated carbon masterbatch, uvioresistant masterbatch
And mosquito-proof masterbatch；The blank cylinder includes cylinder, and the cylinder import is provided with import flashboard, and the cartridge outlet is provided with out
Mouth flashboard, the inner barrel are provided with blank roller, and the entrance point of the thin footpath spinneret orifice is provided with tapered inlet, and the spinneret exists
Spinneret orifice inlet side is provided with the guiding import of taper, and the tapered inlet of thin footpath spinneret orifice is connected with guiding import.
2. a kind of low energy consumption fiber product preparation method according to claim 1, it is characterised in that：The feeding barrel is inclined
Arrange, the bottom of the feeding barrel is provided with a rotating disk, and the feeding bottom of the barrel is provided with a discharge nozzle, institute in low level side extreme lower position
Stating feeding barrel, a feed pipe extended from the high-order lateral low level side of feeding barrel, the import of the feed pipe is provided with below bung
End is passed from feeding barrel, and the port of export of the feed pipe is near the low level side inner barrel wall of feeding barrel.
3. a kind of low energy consumption fiber product preparation method according to claim 2, it is characterised in that：The bucket of the feeding barrel
On mouth, capping has glass cover, and the bung end face high position side centre position is provided with bearing pin, and the glass cover is hinged on bearing pin.
4. a kind of low energy consumption fiber product preparation method according to claim 2, it is characterised in that：The feeding barrel is for falling
Taper type cylinder, the angle of inclination of the feeding barrel is 45 degree, and the feeding barrel outer barrel wall is provided with the connecting tube passed through for feed pipe,
The connecting tube is provided with screw and is fixed feed pipe with connecting tube.
5. a kind of low energy consumption fiber product preparation method according to claim 1, it is characterised in that：The material blanking tube is inclined
Arrange, the material blanking tube is made up of multistage differing tilt angles sectional pipe, and the angle of inclination of multistage sectional pipe is from high to low progressively
Reduce.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610652310.0A CN106480514B (en) | 2014-08-26 | 2014-08-26 | A kind of low energy consumption fiber product preparation method |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410423980.6A CN104264243B (en) | 2014-08-26 | 2014-08-26 | A kind of melt spinning production technology |
| CN201610652310.0A CN106480514B (en) | 2014-08-26 | 2014-08-26 | A kind of low energy consumption fiber product preparation method |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410423980.6A Division CN104264243B (en) | 2014-08-26 | 2014-08-26 | A kind of melt spinning production technology |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106480514A true CN106480514A (en) | 2017-03-08 |
| CN106480514B CN106480514B (en) | 2018-07-20 |
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| CN201610652310.0A Active CN106480514B (en) | 2014-08-26 | 2014-08-26 | A kind of low energy consumption fiber product preparation method |
| CN201610657165.5A Active CN106435767B (en) | 2014-08-26 | 2014-08-26 | A kind of Multi-function chemical product preparation process |
| CN201410423980.6A Active CN104264243B (en) | 2014-08-26 | 2014-08-26 | A kind of melt spinning production technology |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201610657165.5A Active CN106435767B (en) | 2014-08-26 | 2014-08-26 | A kind of Multi-function chemical product preparation process |
| CN201410423980.6A Active CN104264243B (en) | 2014-08-26 | 2014-08-26 | A kind of melt spinning production technology |
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Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106436022A (en) * | 2016-11-23 | 2017-02-22 | 天鼎丰非织造布有限公司 | Preparing method for gray ultraviolet resistant non-woven |
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| JPH05171514A (en) * | 1991-12-24 | 1993-07-09 | Nippon Ester Co Ltd | Method for melt-spinning polyester |
| CN1552961A (en) * | 2003-05-30 | 2004-12-08 | 厦门翔鹭化纤股份有限公司 | Extruding fusion method for low-fusing point polyester and preparing method for low-fusing point polyester composite fibre |
| CN102230233A (en) * | 2011-06-15 | 2011-11-02 | 大连合成纤维研究设计院股份有限公司 | One-step direct spinning process for terylene industrial yarn |
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| CN203049105U (en) * | 2013-01-08 | 2013-07-10 | 浙江裕鑫聚磐实业有限公司 | Colored-spinning fiber production device based on three-basic-color theory |
| CN103556245A (en) * | 2013-11-14 | 2014-02-05 | 苏州千色纺化纤有限公司 | Processing machine for producing textile thread made of polyester fiber |
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| US3754735A (en) * | 1970-07-08 | 1973-08-28 | Slack & Parr Ltd | Polymer coloration |
| DE3382683T3 (en) * | 1982-04-28 | 2001-02-22 | Du Pont | Process for remelting polyamides. |
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| JP5969977B2 (en) * | 2011-03-15 | 2016-08-17 | フマキラー株式会社 | Insect repellent fiber manufacturing method and insect repellent fiber manufactured by the method |
| CN102418169B (en) * | 2011-08-09 | 2014-01-22 | 苏州龙杰特种纤维股份有限公司 | Sea-island fibre and preparation method thereof |
| CN102392317A (en) * | 2011-09-07 | 2012-03-28 | 浙江三志纺织有限公司 | Method for producing differential terylene color yarns |
| CN203174235U (en) * | 2013-01-24 | 2013-09-04 | 大连华阳化纤科技有限公司 | Bi-component synthetic fiber spinning manifold |
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- 2014-08-26 CN CN201610652310.0A patent/CN106480514B/en active Active
- 2014-08-26 CN CN201610657165.5A patent/CN106435767B/en active Active
- 2014-08-26 CN CN201410423980.6A patent/CN104264243B/en active Active
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| JPH05171514A (en) * | 1991-12-24 | 1993-07-09 | Nippon Ester Co Ltd | Method for melt-spinning polyester |
| CN1552961A (en) * | 2003-05-30 | 2004-12-08 | 厦门翔鹭化纤股份有限公司 | Extruding fusion method for low-fusing point polyester and preparing method for low-fusing point polyester composite fibre |
| CN102230233A (en) * | 2011-06-15 | 2011-11-02 | 大连合成纤维研究设计院股份有限公司 | One-step direct spinning process for terylene industrial yarn |
| CN103046144A (en) * | 2013-01-08 | 2013-04-17 | 浙江裕鑫聚磐实业有限公司 | Trichromatic theory pun-dyed fiber production method and trichromatic theory pun-dyed fiber production equipment |
| CN203049105U (en) * | 2013-01-08 | 2013-07-10 | 浙江裕鑫聚磐实业有限公司 | Colored-spinning fiber production device based on three-basic-color theory |
| CN103556245A (en) * | 2013-11-14 | 2014-02-05 | 苏州千色纺化纤有限公司 | Processing machine for producing textile thread made of polyester fiber |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106480514B (en) | 2018-07-20 |
| CN104264243B (en) | 2016-11-23 |
| CN104264243A (en) | 2015-01-07 |
| CN106435767B (en) | 2018-08-21 |
| CN106435767A (en) | 2017-02-22 |
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