CN109651775A - A kind of chemical thickening method of reuse polyethylene terephthalate - Google Patents

A kind of chemical thickening method of reuse polyethylene terephthalate Download PDF

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Publication number
CN109651775A
CN109651775A CN201811589894.7A CN201811589894A CN109651775A CN 109651775 A CN109651775 A CN 109651775A CN 201811589894 A CN201811589894 A CN 201811589894A CN 109651775 A CN109651775 A CN 109651775A
Authority
CN
China
Prior art keywords
polyethylene terephthalate
screw extruder
reuse
chain extender
melting extrusion
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
CN201811589894.7A
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Chinese (zh)
Inventor
马海燕
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.)
Nantong New Silk Monofilament Polytron Technologies Inc
Original Assignee
Nantong New Silk Monofilament Polytron Technologies Inc
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 Nantong New Silk Monofilament Polytron Technologies Inc filed Critical Nantong New Silk Monofilament Polytron Technologies Inc
Priority to CN201811589894.7A priority Critical patent/CN109651775A/en
Publication of CN109651775A publication Critical patent/CN109651775A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L67/00Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
    • C08L67/02Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • C08L2205/025Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure

Abstract

The invention discloses a kind of chemical thickening methods of reuse polyethylene terephthalate, including ingredient: the bottle piece of the reunion material of polyethylene terephthalate, polyethylene terephthalate is mixed, it is sent into double screw extruder melting extrusion, chain extender is added during melting extrusion to be reacted, the reaction time 30 seconds ~ 5 minutes;The screw diameter of double screw extruder is 36 ~ 53mm, and extruder temperature is 270 DEG C, and screw extruder carries out vacuumize process.The method of the present invention is easy, can effectively improve reuse polyethylene terephthalate inherent viscosity, reuse polyethylene terephthalate inherent viscosity is increased to 0.85dl/g or more.

Description

A kind of chemical thickening method of reuse polyethylene terephthalate
Technical field
The present invention relates to a kind of thickening methods of reuse polyethylene terephthalate.
Background technique
The returns of existing polyethylene terephthalate, since inherent viscosity is low, generally in 0.55dl/g or so, It is difficult to that high-intensitive monofilament is made.
Summary of the invention
The purpose of the present invention is to provide a kind of reuse polyethylene terephthalate inherent viscosities of capable of effectively improving The chemical thickening method of reuse polyethylene terephthalate.
The technical solution of the invention is as follows:
A kind of chemical thickening method of reuse polyethylene terephthalate, it is characterized in that: including the following steps:
(1) ingredient: the raw material of following mass percent is mixed:
The reunion material 30 ~ 50% of polyethylene terephthalate
The bottle piece 50 ~ 70% of polyethylene terephthalate;
(2) above-mentioned raw materials are sent into double screw extruder melting extrusion, chain extender is added during melting extrusion and is reacted, instead 30 seconds ~ 5 minutes between seasonable;The screw diameter of double screw extruder be 36 ~ 53mm, extruder temperature be 270 DEG C, screw extruder into Row vacuumize process.
The chain extender are as follows: bisoxazoline (BOZ), pyromellitic acid anhydride (PMDA), diisocyanate one kind or Three kinds of compoundings (compound proportion is bisoxazoline: pyromellitic acid anhydride: diisocyanate=20 ~ 30:30 ~ 40:30 ~ 50);Chain extension The dosage of agent is the 0.1 ~ 0.5% of step (1) raw material dosage.
The method of the present invention is easy, can effectively improve reuse polyethylene terephthalate inherent viscosity, by poly- pair of reuse Ethylene terephthalate inherent viscosity is increased to 0.85dl/g or more.
Below with reference to embodiment, the invention will be further described.
Embodiment 1:
A kind of chemical thickening method of reuse polyethylene terephthalate, including the following steps:
(1) ingredient: the raw material of following mass percent is mixed:
The reunion material 40% of polyethylene terephthalate
The bottle piece 60% of polyethylene terephthalate;
(2) above-mentioned raw materials are sent into double screw extruder melting extrusion, chain extender is added during melting extrusion and is reacted, instead 2 minutes between seasonable;The screw diameter of double screw extruder is 42mm(or 38 mm, 41mm, 51 mm, 52mm), extruder temperature is 270 DEG C, screw extruder carries out vacuumize process.
The chain extender are as follows: bisoxazoline;The dosage of chain extender is the 0.2% of step (1) raw material dosage.
Products obtained therefrom inherent viscosity >=0.85dl/g.
Embodiment 2:
A kind of chemical thickening method of reuse polyethylene terephthalate, including the following steps:
(1) ingredient: the raw material of following mass percent is mixed:
The reunion material 50% of polyethylene terephthalate
The bottle piece 50% of polyethylene terephthalate;
(2) above-mentioned raw materials are sent into double screw extruder melting extrusion, chain extender is added during melting extrusion and is reacted, instead 3 minutes between seasonable;The screw diameter of double screw extruder is 50mm(or 38 mm, 42 mm, 51 mm, 52mm), extruder temperature is 270 DEG C, screw extruder carries out vacuumize process.
The chain extender are as follows: pyromellitic acid anhydride;The dosage of chain extender is the 0.3% of step (1) raw material dosage.
Products obtained therefrom inherent viscosity >=0.90dl/g.
Embodiment 3:
A kind of chemical thickening method of reuse polyethylene terephthalate, including the following steps:
(1) ingredient: the raw material of following mass percent is mixed:
The reunion material 30% of polyethylene terephthalate
The bottle piece 70% of polyethylene terephthalate;
(2) above-mentioned raw materials are sent into double screw extruder melting extrusion, chain extender is added during melting extrusion and is reacted, instead 4 minutes between seasonable;The screw diameter of double screw extruder is 53mm(or 38 mm, 42 mm, 51 mm, 52mm), extruder temperature is 270 DEG C, screw extruder carries out vacuumize process.
The chain extender are as follows: three kinds of bisoxazoline (BOZ), pyromellitic acid anhydride (PMDA), diisocyanate compounds (compound proportion is bisoxazoline: pyromellitic acid anhydride: diisocyanate=20 ~ 30:30 ~ 40:30 ~ 50);The dosage of chain extender It is the 0.45% of step (1) raw material dosage.
Products obtained therefrom inherent viscosity >=0.99dl/g.

Claims (2)

1. a kind of chemical thickening method of reuse polyethylene terephthalate, it is characterized in that: including the following steps:
(1) ingredient: the raw material of following mass percent is mixed:
The reunion material 30 ~ 50% of polyethylene terephthalate
The bottle piece 50 ~ 70% of polyethylene terephthalate;
(2) above-mentioned raw materials are sent into double screw extruder melting extrusion, chain extender is added during melting extrusion and is reacted, instead 30 seconds ~ 5 minutes between seasonable;The screw diameter of double screw extruder be 36 ~ 53mm, extruder temperature be 270 DEG C, screw extruder into Row vacuumize process.
2. a kind of chemical thickening method of reuse polyethylene terephthalate according to claim 1, it is characterized in that: The chain extender are as follows: bisoxazoline, pyromellitic acid anhydride, one kind of diisocyanate or three kinds of compoundings, compound proportion are Bisoxazoline: pyromellitic acid anhydride: diisocyanate=20 ~ 30:30 ~ 40:30 ~ 50;The dosage of chain extender is that step (1) is former Expect the 0.1 ~ 0.5% of dosage.
CN201811589894.7A 2018-12-25 2018-12-25 A kind of chemical thickening method of reuse polyethylene terephthalate Pending CN109651775A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811589894.7A CN109651775A (en) 2018-12-25 2018-12-25 A kind of chemical thickening method of reuse polyethylene terephthalate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811589894.7A CN109651775A (en) 2018-12-25 2018-12-25 A kind of chemical thickening method of reuse polyethylene terephthalate

Publications (1)

Publication Number Publication Date
CN109651775A true CN109651775A (en) 2019-04-19

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811589894.7A Pending CN109651775A (en) 2018-12-25 2018-12-25 A kind of chemical thickening method of reuse polyethylene terephthalate

Country Status (1)

Country Link
CN (1) CN109651775A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110126136A (en) * 2019-05-20 2019-08-16 安徽东锦资源再生科技有限公司 Utilize the technics of enhancing viscosity of Pillar recovery bottle piece processing HMLS Polyester silk
CN110669321A (en) * 2019-11-11 2020-01-10 南通新帝克单丝科技股份有限公司 Preparation method of chemically tackified regenerated PET (polyethylene terephthalate) and monofilament
CN110983452A (en) * 2019-12-19 2020-04-10 中山市东龙新材料有限公司 Preparation method of black PET zipper monofilament

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004101666A2 (en) * 2003-05-19 2004-11-25 Polymers Australia Pty. Limited Polyester masterbatch composition
CN101659757A (en) * 2009-09-28 2010-03-03 华东理工大学 Method for preparing medium-viscosity PET slice by recycled low-viscosity polyester yarn
CN102417697A (en) * 2011-09-22 2012-04-18 东莞上海大学纳米技术研究院 Waste PET toughening tackifying method and PET pellet prepared by using same
CN102797067A (en) * 2012-08-28 2012-11-28 扬州天富龙科技纤维有限公司 Preparation method of renewable polyester POY (Pre-oriented Yarn) color fibers
CN104829809A (en) * 2014-02-11 2015-08-12 王祖文 High-molecular foam material
US20180044518A1 (en) * 2010-05-06 2018-02-15 Johnson & Johnson Vision Care, Inc. Non-reactive, hydrophilic polymers having terminal siloxanes and methods for making and using the same

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004101666A2 (en) * 2003-05-19 2004-11-25 Polymers Australia Pty. Limited Polyester masterbatch composition
CN101659757A (en) * 2009-09-28 2010-03-03 华东理工大学 Method for preparing medium-viscosity PET slice by recycled low-viscosity polyester yarn
US20180044518A1 (en) * 2010-05-06 2018-02-15 Johnson & Johnson Vision Care, Inc. Non-reactive, hydrophilic polymers having terminal siloxanes and methods for making and using the same
CN102417697A (en) * 2011-09-22 2012-04-18 东莞上海大学纳米技术研究院 Waste PET toughening tackifying method and PET pellet prepared by using same
CN102797067A (en) * 2012-08-28 2012-11-28 扬州天富龙科技纤维有限公司 Preparation method of renewable polyester POY (Pre-oriented Yarn) color fibers
CN104829809A (en) * 2014-02-11 2015-08-12 王祖文 High-molecular foam material

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110126136A (en) * 2019-05-20 2019-08-16 安徽东锦资源再生科技有限公司 Utilize the technics of enhancing viscosity of Pillar recovery bottle piece processing HMLS Polyester silk
CN110126136B (en) * 2019-05-20 2021-04-23 安徽东锦资源再生科技有限公司 Tackifying process for processing high-modulus low-shrinkage polyester yarns by utilizing recycled polyester bottle flakes
CN110669321A (en) * 2019-11-11 2020-01-10 南通新帝克单丝科技股份有限公司 Preparation method of chemically tackified regenerated PET (polyethylene terephthalate) and monofilament
CN110983452A (en) * 2019-12-19 2020-04-10 中山市东龙新材料有限公司 Preparation method of black PET zipper monofilament

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Application publication date: 20190419

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