CN107227495A - A kind of preparation technology of high-efficiency polyester raw material - Google Patents

A kind of preparation technology of high-efficiency polyester raw material Download PDF

Info

Publication number
CN107227495A
CN107227495A CN201710391153.7A CN201710391153A CN107227495A CN 107227495 A CN107227495 A CN 107227495A CN 201710391153 A CN201710391153 A CN 201710391153A CN 107227495 A CN107227495 A CN 107227495A
Authority
CN
China
Prior art keywords
bottle
piece
tow
raw material
sorting
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.)
Pending
Application number
CN201710391153.7A
Other languages
Chinese (zh)
Inventor
邹睿
邹舟
曾勇
张雄飞
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sichuan Shuanglong Industry Co Ltd
Original Assignee
Sichuan Shuanglong Industry Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sichuan Shuanglong Industry Co Ltd filed Critical Sichuan Shuanglong Industry Co Ltd
Priority to CN201710391153.7A priority Critical patent/CN107227495A/en
Publication of CN107227495A publication Critical patent/CN107227495A/en
Pending legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D1/00Treatment of filament-forming or like material
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D1/00Treatment of filament-forming or like material
    • D01D1/10Filtering or de-aerating the spinning solution or melt
    • D01D1/106Filtering
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/08Melt spinning methods
    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02JFINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
    • D02J13/00Heating or cooling the yarn, thread, cord, rope, or the like, not specific to any one of the processes provided for in this subclass

Abstract

The invention discloses a kind of preparation technology of high-efficiency polyester raw material, the preparation technology includes preparations of bottle piece, the pretreatment of bottle piece, the melting of bottle piece, filtering, homopolymerization, supercharging, spinning, winds into bucket, drawing-off, anxiety thermal finalization, curling, relaxation heat setting, cuts off and pack, and beneficial effects of the present invention are;The bottle piece pretreatment stage of production technology, bottle piece is according to white, blueness and other colors are divided into three major types, color proportioning is carried out according to the purposes of produced terylene, so the waste or used plastics of a variety of colors can be made fully to be applied, so as to avoid the pollution and waste of certain plastic bottle, the present invention sets nervous thermal finalization between drawing-off and curling, and multiple heating rollers are provided with to heat tow, so that the heating-up temperature of tow is in gradual rise, avoid because heating roller is few, the too quickly tow toughness caused of heating-up temperature rise is not enough, the poor situation of resilience.

Description

A kind of preparation technology of high-efficiency polyester raw material
Technical field
The present invention relates to terylene preparation field, more particularly to a kind of preparation technology of high-efficiency polyester raw material.
Background technology
At present, PET material consumption when making beverage, the packing container such as food and film is very big, especially beverage bottle and The consumption of mineral water bottle is annual, and all in cumulative year after year, used beverage bottle and mineral water bottle can cause substantial amounts of waste or used plastics, And the natural degradation of plastics is very slow, more suitable for recycling, using waste or used plastics white vase piece production terylene be it is a kind of well The method for solving waste or used plastics pollution, at present, the production technology for producing terylene using waste or used plastics white vase piece have been preliminarily formed, For example, patent application publication number is high using discarded bottle chips production weaving for CN201210556714 patent application-one kind The production technology of shelves core, the chopped fiber terylene resilience of existing production technology production is poor, during as clothes textile raw material, Body surface feels not soft, uncomfortable when wearing, and is unfavorable for the market public praise of chopped fiber clothing, eventually influences waste or used plastics white vase Piece produces the development of terylene, and prior art production polyester raw material inefficiency, and quality cannot be guaranteed.
The content of the invention
Special a kind of preparation technology of high-efficiency polyester raw material of offer of the invention, solves the polyester raw material that prior art is produced Resilience is poor, produces polyester raw material inefficiency, the problem of quality cannot be guaranteed.
Technical scheme is as follows:
A kind of preparation technology of high-efficiency polyester raw material, comprises the following steps:
It is prepared by a, bottle piece:Using PET waste or used plastics, the different white vase piece of color is prepared;
B, the pretreatment of bottle piece:First bottle tablet raw material is cleaned, dried after cleaning with drier, then, according to need Colour match is carried out to white vase piece and is mixed;
C, the melting of bottle piece:First the white vase piece matched is dried, then entered white vase piece feeding double screw extruder Row melting;
D, filtering, homopolymerization, supercharging;Fused mass after to being extruded through extruder is filtered, and subsequently enters homopolymerization kettle Viscosify and vacuumize removing small molecule, then by booster pump, with ensure spinning continuous production and melt pressure it is constant;
E, spinning, from booster pump come out after fused mass enter filament spinning component, by filament spinning component from spinneret spray,
F, wind into bucket:Tow after oil spout, is then wound and finally enters bucket by the oil injection agent on the tow of extrusion;
G, drawing-off:Tow in bucket is subjected to drawing-off;
H, nervous thermal finalization:The heating roller that the tow of drawing-off is sent into tension-setting machine, tension-setting machine is Upper nine times eight and cross arrangement, tow are wound through all heating rollers, and heating roller is heated using steam, all heating rollers Temperature according to tandem progressively be incremented by, maximum temperature be 200 degrees Celsius;
I, curling:The tow of winding is stretched, then loosened, tow is crimped naturally;
J, relaxation heat setting:Tow is subjected to hot-air seasoning;
K, cut-out packing:Product according to involved by tow is cut off and carried out to tow to the different demands of size Enter bag packing.
In such scheme, the step a points are following steps:
A1, raw material are unpacked:First, bottle brick binding is cut, bottle brick then is put into unpacking pond carries out mechanical unpacking;
A2, impurity sorting:Stock bottle after unpacking is delivered in sorting belt by the conveyer belt with magnetic force, iron impurity quilt Conveyer belt absorption is taken away, and workman sorts in sorting belt to the metal impurities without removal;
A3, a wash bottle:Stock bottle after sorting, which is transported in rinsing maching, to be cleaned, and rinsing maching is in cleaning stock bottle While by stock bottle be moved to rinsing maching outlet;
A4, de- mark:De- mark is carried out to the stock bottle after cleaning with label removing machine to handle, separated bottle mark is sent by wind to be blown to back Receive the stock bottle after case, de- mark and be transported to subsequent processing;
A5, secondary wash bottle:First, stock bottle is delivered into purge tank to be cleaned, is hot water and logical steaming in purge tank Vapour, then stock bottle is taken out and is delivered to highly basic tank cleaned, and is the mixing liquid of sodium hydroxide and water in highly basic tank, most Cleaned by purge tank again afterwards and be delivered to next step process;
A6, material and colour sorting:First, the artificial preliminary sorting for carrying out material, the stock bottle of non-PET materials is sorted Remove, afterwards, material secondary sorting and colour sorting are carried out successively by the automatic sorting system of material and color, most institute at last Need that the PET material stock bottles of color are sorted out and wind is delivered in feed bin;
A7, raw material are crushed and bottle cap separation:Stock bottle in feed bin is delivered into pulverizer to carry out at pulverization process, crushing Reason forms bottle piece, and then bottle piece is delivered in tank, and the fragment of covering part is in floating shape, and the bottle piece of bottle portion sinks to water In groove, finally the fragment of floating is got rid of, the bottle piece of submerged is delivered to next step process;
A8, the cleaning of bottle piece and dehydration:First bottle piece is cleaned with high-temperature water, then with added with sodium hydroxide and cleaning agent Rinse water is cleaned to bottle piece, and cleaning carries out drying dehydration with drier after finishing, after dehydration is finished, with normal-temperature water to bottle piece Cleaned, cleaning carries out drying dehydration with drier to bottle piece again after finishing, and production textile raw material can be carried out by eventually forming White vase piece.
In such scheme, the temperature of hot water is 85~95 degrees Celsius in the purge tank in described a5 steps, in highly basic tank Sodium hydroxide shared by weight percentage be 3.6~4.1%.
In such scheme, in described step b, white vase piece color proportioning is used in production cloth or home textile and its filler Chopped fiber when using blueness and white white vase piece mixing match, blue white vase piece accounts for 14%~ 19%, when producing the chopped fiber used in toy filler using the white vase piece mixing match of other colors.
5th, the preparation technology of a kind of high-efficiency polyester raw material according to claim 1, it is characterised in that:Described step In c, the operating temperature of double screw extruder is 270~290 degrees Celsius.
In such scheme, pressure is less than or equal to pressure constant in 16Mpa, filter process before the filter during step d filterings Power is 8.5Mpa, and double-filtration is used when filtering, and the screen pack of filter device therefor is 15 microns, two grades when the first order is filtered The screen pack for filtering filter device therefor is 25 microns.
In summary, the beneficial effects of the invention are as follows:
1st, the chopped fiber using the production of PET waste or used plastics is corrosion-resistant, nonhygroscopic, and service life is longer, the bottle of preparation technology Piece pretreatment stage, bottle piece is divided into three major types according to white, blueness and other colors, is carried out according to the purposes of produced terylene Color is matched, and so the waste or used plastics of a variety of colors can be made fully to be applied, so as to avoid the pollution of certain plastic bottle And waste, it is of the invention that nervous thermal finalization is set between drawing-off and curling, and multiple heating rollers are provided with to tow heating, So that the heating-up temperature of tow is in gradual rise, it is to avoid because heating roller is few, the too quickly silk caused of heating-up temperature rise The situation that beam toughness is not enough, resilience is poor.
2nd, the present invention prepares polyester raw material by 11 steps, makes preparing for polyester raw material more efficient.
3rd, the present invention passes through filtering, homopolymerization, supercharging, anxiety thermal finalization, the setting of relaxation heat setting these steps so that The polyester raw material quality prepared is guaranteed
Embodiment
For the present invention is better achieved, the present invention is described in detail with reference to specific embodiment, but this The embodiment of invention is not limited to this.
A kind of preparation technology of high-efficiency polyester raw material, it is characterised in that comprise the following steps:
It is prepared by a, bottle piece:Using PET waste or used plastics, the different white vase piece of color is prepared;
B, the pretreatment of bottle piece:First bottle tablet raw material is cleaned, dried after cleaning with drier, then, according to need Colour match is carried out to white vase piece and is mixed;
C, the melting of bottle piece:First the white vase piece matched is dried, then entered white vase piece feeding double screw extruder Row melting;
D, filtering, homopolymerization, supercharging;Fused mass after to being extruded through extruder is filtered, and subsequently enters homopolymerization kettle Viscosify and vacuumize removing small molecule, then by booster pump, with ensure spinning continuous production and melt pressure it is constant;
E, spinning, from booster pump come out after fused mass enter filament spinning component, by filament spinning component from spinneret spray,
F, wind into bucket:Tow after oil spout, is then wound and finally enters bucket by the oil injection agent on the tow of extrusion;
G, drawing-off:Tow in bucket is subjected to drawing-off;
H, nervous thermal finalization:The heating roller that the tow of drawing-off is sent into tension-setting machine, tension-setting machine is Upper nine times eight and cross arrangement, tow are wound through all heating rollers, and heating roller is heated using steam, all heating rollers Temperature according to tandem progressively be incremented by, maximum temperature be 200 degrees Celsius;
I, curling:The tow of winding is stretched, then loosened, tow is crimped naturally;
J, relaxation heat setting:Tow is subjected to hot-air seasoning;
K, cut-out packing:Product according to involved by tow is cut off and carried out to tow to the different demands of size Enter bag packing.
It is preferred that, the step a points are following steps:
A1, raw material are unpacked:First, bottle brick binding is cut, bottle brick then is put into unpacking pond carries out mechanical unpacking;
A2, impurity sorting:Stock bottle after unpacking is delivered in sorting belt by the conveyer belt with magnetic force, iron impurity quilt Conveyer belt absorption is taken away, and workman sorts in sorting belt to the metal impurities without removal;
A3, a wash bottle:Stock bottle after sorting, which is transported in rinsing maching, to be cleaned, and rinsing maching is in cleaning stock bottle While by stock bottle be moved to rinsing maching outlet;
A4, de- mark:De- mark is carried out to the stock bottle after cleaning with label removing machine to handle, separated bottle mark is sent by wind to be blown to back Receive the stock bottle after case, de- mark and be transported to subsequent processing;
A5, secondary wash bottle:First, stock bottle is delivered into purge tank to be cleaned, is hot water and logical steaming in purge tank Vapour, then stock bottle is taken out and is delivered to highly basic tank cleaned, and is the mixing liquid of sodium hydroxide and water in highly basic tank, most Cleaned by purge tank again afterwards and be delivered to next step process;
A6, material and colour sorting:First, the artificial preliminary sorting for carrying out material, the stock bottle of non-PET materials is sorted Remove, afterwards, material secondary sorting and colour sorting are carried out successively by the automatic sorting system of material and color, most institute at last Need that the PET material stock bottles of color are sorted out and wind is delivered in feed bin;
A7, raw material are crushed and bottle cap separation:Stock bottle in feed bin is delivered into pulverizer to carry out at pulverization process, crushing Reason forms bottle piece, and then bottle piece is delivered in tank, and the fragment of covering part is in floating shape, and the bottle piece of bottle portion sinks to water In groove, finally the fragment of floating is got rid of, the bottle piece of submerged is delivered to next step process;
A8, the cleaning of bottle piece and dehydration:First bottle piece is cleaned with high-temperature water, then with added with sodium hydroxide and cleaning agent Rinse water is cleaned to bottle piece, and cleaning carries out drying dehydration with drier after finishing, after dehydration is finished, with normal-temperature water to bottle piece Cleaned, cleaning carries out drying dehydration with drier to bottle piece again after finishing, and production textile raw material can be carried out by eventually forming White vase piece.
It is preferred that, the temperature of hot water is the hydrogen in 85~95 degrees Celsius, highly basic tank in the purge tank in described a5 steps The percentage of weight shared by sodium oxide molybdena is 3.6~4.1%.
It is preferred that, in described step b, white vase piece color proportioning is short used in production cloth or home textile and its filler Using blueness and white white vase piece mixing match during fiber, blue white vase piece accounts for 14%~19%, When producing the chopped fiber used in toy filler using the white vase piece mixing match of other colors.
It is preferred that, in described step c, the operating temperature of double screw extruder is 270~290 degrees Celsius.
It is preferred that, pressure is less than or equal to pressure constant in 16Mpa, filter process and is before filter during step d filtering 8.5Mpa, uses double-filtration when filtering, the screen pack of filter device therefor is 15 microns, secondary filtration when the first order is filtered The screen pack of filter device therefor is 25 microns.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all essences in the present invention Any modifications, equivalent substitutions and improvements made within refreshing and principle etc., should be included in the scope of the protection.

Claims (6)

1. a kind of preparation technology of high-efficiency polyester raw material, it is characterised in that comprise the following steps:
It is prepared by a, bottle piece:Using PET waste or used plastics, the different white vase piece of color is prepared;
B, the pretreatment of bottle piece:First bottle tablet raw material is cleaned, dried after cleaning with drier, it is then, right as needed White vase piece carries out colour match and mixed;
C, the melting of bottle piece:First the white vase piece matched is dried, then white vase piece feeding double screw extruder is melted Melt;
D, filtering, homopolymerization, supercharging;Fused mass after to being extruded through extruder is filtered, and subsequently enters homopolymerization kettle thickening With vacuumize removing small molecule, then by booster pump, with ensure spinning continuous production and melt pressure it is constant;
E, spinning, from booster pump come out after fused mass enter filament spinning component, by filament spinning component from spinneret spray,
F, wind into bucket:Tow after oil spout, is then wound and finally enters bucket by the oil injection agent on the tow of extrusion;
G, drawing-off:Tow in bucket is subjected to drawing-off;
H, nervous thermal finalization:The heating roller that the tow of drawing-off is sent into tension-setting machine, tension-setting machine is upper nine Eight and cross arrangement are descended, tow is wound through all heating rollers, and heating roller is heated using steam, the temperature of all heating rollers Degree is progressively incremented by according to tandem, and maximum temperature is 200 degrees Celsius;
I, curling:The tow of winding is stretched, then loosened, tow is crimped naturally;
J, relaxation heat setting:Tow is subjected to hot-air seasoning;
K, cut-out packing:Product according to involved by tow is cut off to tow and carried out into bag to the different demands of size Packing.
2. a kind of preparation technology of high-efficiency polyester raw material according to claim 1, it is characterised in that:The step a points are Following steps:
A1, raw material are unpacked:First, bottle brick binding is cut, bottle brick then is put into unpacking pond carries out mechanical unpacking;
A2, impurity sorting:Stock bottle after unpacking is delivered in sorting belt by the conveyer belt with magnetic force, and iron impurity is conveyed Band absorption is taken away, and workman sorts in sorting belt to the metal impurities without removal;
A3, a wash bottle:Stock bottle after sorting, which is transported in rinsing maching, to be cleaned, and rinsing maching is same cleaning stock bottle When by stock bottle be moved to rinsing maching outlet;
A4, de- mark:De- mark is carried out to the stock bottle after cleaning with label removing machine to handle, separated bottle mark is sent by wind is blown to recovery Stock bottle after case, de- mark is transported to subsequent processing;
A5, secondary wash bottle:First, stock bottle is delivered into purge tank to be cleaned, is hot water and logical steam in purge tank, so Stock bottle is taken out and is delivered to highly basic tank afterwards and is cleaned, is the mixing liquid of sodium hydroxide and water in highly basic tank, again finally Cleaned by purge tank and be delivered to next step process;
A6, material and colour sorting:First, the artificial preliminary sorting for carrying out material, the stock bottle sorting of non-PET materials is gone Remove, afterwards, material secondary sorting and colour sorting are carried out successively by the automatic sorting system of material and color, it is most required at last The PET material stock bottles of color are sorted out and wind is delivered in feed bin;
A7, raw material are crushed and bottle cap separation:Stock bottle in feed bin is delivered to pulverizer and carries out pulverization process, pulverization process shape Into bottle piece, then bottle piece is delivered in tank, the fragment of covering part is in floating shape, and the bottle piece of bottle portion sinks to tank In, finally the fragment of floating is got rid of, the bottle piece of submerged is delivered to next step process;
A8, the cleaning of bottle piece and dehydration:First bottle piece is cleaned with high-temperature water, then with the cleaning added with sodium hydroxide and cleaning agent Water is cleaned to bottle piece, and cleaning carries out drying dehydration with drier after finishing, after dehydration is finished, bottle piece is carried out with normal-temperature water Cleaning, cleaning carries out drying dehydration with drier to bottle piece again after finishing, and eventually forming can carry out producing textile raw material White vase piece.
3. a kind of preparation technology of high-efficiency polyester raw material according to claim 2, it is characterised in that:In described a5 steps Purge tank in the temperature of hot water be 85~95 degrees Celsius, the percentage of weight shared by the sodium hydroxide in highly basic tank for 3.6~ 4.1%.
4. a kind of preparation technology of high-efficiency polyester raw material according to claim 1, it is characterised in that:In described step b, White vase piece color proportioning is mixed using blueness and white white vase piece in the chopped fiber used in production cloth or home textile and its filler Proportioning is closed, blue white vase piece accounts for 14%~19%, in the chopped fiber used in production toy filler The white vase piece mixing match of other colors of Shi Caiyong.
5. a kind of preparation technology of high-efficiency polyester raw material according to claim 1, it is characterised in that:In described step c, The operating temperature of double screw extruder is 270~290 degrees Celsius.
6. a kind of preparation technology of high-efficiency polyester raw material according to claim 1, it is characterised in that the step d filterings When filter before pressure be less than or equal to 16Mpa, constant pressure is 8.5Mpa in filter process, and two-stage mistake is used when filtering Filter, the screen pack of filter device therefor is 15 microns when the first order is filtered, and the screen pack of secondary filtration filter device therefor is 25 microns.
CN201710391153.7A 2017-05-27 2017-05-27 A kind of preparation technology of high-efficiency polyester raw material Pending CN107227495A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710391153.7A CN107227495A (en) 2017-05-27 2017-05-27 A kind of preparation technology of high-efficiency polyester raw material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710391153.7A CN107227495A (en) 2017-05-27 2017-05-27 A kind of preparation technology of high-efficiency polyester raw material

Publications (1)

Publication Number Publication Date
CN107227495A true CN107227495A (en) 2017-10-03

Family

ID=59933830

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710391153.7A Pending CN107227495A (en) 2017-05-27 2017-05-27 A kind of preparation technology of high-efficiency polyester raw material

Country Status (1)

Country Link
CN (1) CN107227495A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110629374A (en) * 2019-08-26 2019-12-31 宁波大千纺织品有限公司 Staggered corrugated elastic knitted fabric and preparation method thereof
CN112538674A (en) * 2019-09-23 2021-03-23 江阴远闻纺织有限公司 Moisture-absorbing sweat-releasing regenerated polyester core-spun yarn and manufacturing method thereof
CN113201800A (en) * 2021-04-07 2021-08-03 宿迁逸达新材料有限公司 Method and equipment for preparing polyester staple fibers by using waste polyester raw materials
CN113249840A (en) * 2021-06-08 2021-08-13 龙游生生纺织科技有限公司 Degradable colored spun fancy yarn and preparation method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008051430A1 (en) * 2008-10-11 2010-04-15 Trevira Gmbh Superabsorbent bicomponent fiber
CN103789873A (en) * 2014-02-25 2014-05-14 盛虹集团有限公司 Regenerated skin-core structure composite fiber and preparation method thereof
CN103882542A (en) * 2014-04-01 2014-06-25 仪征市中兴涤纶纤维厂 Preparation method of polyester FDYs special for bottle reworked material regenerative special-shaped superbright woven tapes
CN104846448A (en) * 2015-06-10 2015-08-19 河北金怡化纤有限公司 Production process for producing differentiated polyester staple fibers by using PET plastic bottle sheets
CN104890143A (en) * 2015-06-10 2015-09-09 河北吉悦再生物资回收有限公司 Production technology capable of utilizing PET waste plastics for producing bottle purifying pieces for fibrous raw materials

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008051430A1 (en) * 2008-10-11 2010-04-15 Trevira Gmbh Superabsorbent bicomponent fiber
CN103789873A (en) * 2014-02-25 2014-05-14 盛虹集团有限公司 Regenerated skin-core structure composite fiber and preparation method thereof
CN103882542A (en) * 2014-04-01 2014-06-25 仪征市中兴涤纶纤维厂 Preparation method of polyester FDYs special for bottle reworked material regenerative special-shaped superbright woven tapes
CN104846448A (en) * 2015-06-10 2015-08-19 河北金怡化纤有限公司 Production process for producing differentiated polyester staple fibers by using PET plastic bottle sheets
CN104890143A (en) * 2015-06-10 2015-09-09 河北吉悦再生物资回收有限公司 Production technology capable of utilizing PET waste plastics for producing bottle purifying pieces for fibrous raw materials

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110629374A (en) * 2019-08-26 2019-12-31 宁波大千纺织品有限公司 Staggered corrugated elastic knitted fabric and preparation method thereof
CN112538674A (en) * 2019-09-23 2021-03-23 江阴远闻纺织有限公司 Moisture-absorbing sweat-releasing regenerated polyester core-spun yarn and manufacturing method thereof
CN113201800A (en) * 2021-04-07 2021-08-03 宿迁逸达新材料有限公司 Method and equipment for preparing polyester staple fibers by using waste polyester raw materials
CN113249840A (en) * 2021-06-08 2021-08-13 龙游生生纺织科技有限公司 Degradable colored spun fancy yarn and preparation method thereof
CN113249840B (en) * 2021-06-08 2022-09-23 龙游生生纺织科技有限公司 Degradable colored spun fancy yarn and preparation method thereof

Similar Documents

Publication Publication Date Title
CN107227495A (en) A kind of preparation technology of high-efficiency polyester raw material
CN103710783B (en) The method of polyester staple fiber produced by waste polyester bottle
CN102505182B (en) Method for preparing functional ultraviolet-resistant polyester staple fiber from waste renewable polyester bottle chips
CN103305960B (en) Method for manufacturing polyester staple fibers through recycled polyester bottles
CN100999264A (en) Braided bag and its production technology and device
CN101144191B (en) Method for producing terylene pre-tropism continuous yarn by utilizing reclaimed polyester bottle
CN104890143B (en) The production technology of fibrous raw material white vase piece is produced using PET waste or used plastics
CN106702503B (en) A kind of effective regenerated polyester fiber spinning technique for solving fracture of wire phenomenon
CN102094252A (en) PET flat filament drawing machine set
CN103484971A (en) Method for preparing anion far-infrared short fibers employing waste renewable polyester bottle flakes
CN111334887A (en) Polyester waste cloth regenerated fiber spinning process with efficient flow and improved quality
CN104264287B (en) Method for preparing rope net ribbon-like filaments by drawing waste and old polyethylene terephthalate (PET) bottle sheets
CN105951250B (en) A kind of spinning method for genuine of fluffy flame
CN104452310A (en) New technology for preparing high-performance polyester fiber based on waste clothes
CN101070638A (en) Polypropylene-fabric filament producing technology
CN104178841A (en) Method for manufacturing safety nets by waste polyester bottles
CN110219070B (en) Process for preparing 3D fly-knitted yarn by regenerating waste polyester yarns
CN208701271U (en) Useless PET polyester circular regeneration product line
CN102963596A (en) Method for manufacturing plastic package for hazardous chemical substance
CN105155021A (en) Preparation method of environment-friendly type woven bag
CN111793836B (en) Method for preparing fibers by directly spinning waste polyester textiles as raw materials
CN107151822A (en) A kind of regenerated resources produce the new technology of terylene
CN205498009U (en) Mesh braided bag flat filament wire drawing machine
CN208701266U (en) Waster terylene cloth corner material manufactures PET polyester flat production line
KR102508241B1 (en) Manufacturing method of monofilament yarn using recycled PET

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20171003