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CN1086404C - Impact-resistant polyester (PET) mixture and preparing process thereof - Google Patents

Impact-resistant polyester (PET) mixture and preparing process thereof Download PDF

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Publication number
CN1086404C
CN1086404C CN98102049A CN98102049A CN1086404C CN 1086404 C CN1086404 C CN 1086404C CN 98102049 A CN98102049 A CN 98102049A CN 98102049 A CN98102049 A CN 98102049A CN 1086404 C CN1086404 C CN 1086404C
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CN
China
Prior art keywords
pet
thermoplastic elastomer
preparation
maleic anhydride
require
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Expired - Fee Related
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CN98102049A
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Chinese (zh)
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CN1238356A (en
Inventor
何嘉松
卜文胜
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Institute of Chemistry CAS
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Institute of Chemistry CAS
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Priority to CN98102049A priority Critical patent/CN1086404C/en
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Publication of CN1086404C publication Critical patent/CN1086404C/en
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Expired - Fee Related legal-status Critical Current

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Abstract

本发明是一种聚酯PET与经过马来酸酐接枝的聚烯烃热塑弹性体POE的共混物,其中包括70-85份的聚对苯二甲酸乙二酯和15-30份的马来酸酐接枝聚烯烃热塑弹性体。本发明PET共混物具有冲击强度600-900J/m。The invention is a blend of polyester PET and polyolefin thermoplastic elastomer POE grafted with maleic anhydride, which includes 70-85 parts of polyethylene terephthalate and 15-30 parts of maleic anhydride Anhydride-grafted polyolefin thermoplastic elastomer. The PET blend of the present invention has an impact strength of 600-900 J/m.

Description

A kind of anti-impact polyester (PET) blend and preparation method thereof
The present invention relates to a kind of polyethylene terephthalate (PET) blend, specially refer to the blend of a kind of PET and thermoplastic elastomer.
PET is owing to have a better heat-resisting, good solubility-resistence and lower price and demonstrate wide application prospect.But it has shortcoming clearly simultaneously again, promptly slower crystallization rate and lower shock strength, thus limited its use in the engineering plastics field.
Patent US 4,845, and 169 use polyester-polyether elastomer PEE and triphenyl phosphorus modified PET, obtain PET shock strength 111J/m, tensile strength 66MPa, and modulus in flexure 5.2MPa, its shock strength is still not high enough.Patent US 4,895, and 899 PET comprises PET, polyethylene (PE), and polycarbonate (PC) and styrene-propene acid grafting EPDM obtain than high impact.Patent US 4,897, and 448 by adding poly terephthalic acid cyclohexyl (PCT), and PC and EPR improve the impact property of PET.
Purpose of the present invention is to overcome the low shortcoming of PET shock strength in the prior art, and a kind of PET blend than high impact property of having that uses the thermoplastic elastomer modification is provided.
The component and the content of PET blend of the present invention are as follows: (1) polyethylene terephthalate (PET) 70-85 part (2) maleic anhydride graft polyolefine thermoplastic elastomer (MAH-g-POE) 15-30 part
Above-mentioned PET intrinsic viscosity is at 0.7-1.0dl/g.
Above-mentioned polyolefine thermoplastic elastomer (POE) is the multipolymer of ethene and octene, and therein ethylene content is 65%-80%, and elastomeric melting index (MFI) is 0.5-5.0g/10min.
POE is a key character of the present invention with maleic anhydride (MAH) grafting.The maleic anhydride graft of POE is the melt grafting.
The preparation method of anti-impact polyester of the present invention (PET) is as follows: (1) is with 100 parts POE and the maleic anhydride (MAH) of 2-4 part, 0.05-0.4 part benzoyl peroxide (DCP) thorough mixing after in 160-180 ℃, extruding pelletization under the 30rpm obtains the MAH grafting POE (MAH-g-POE) of different MAH percentage of grafting.(2) with the PET of 70-85 part in 130 ℃ of dryings of vacuum drying oven after 8 hours, do with the MA-g-POE of 15-30 part and to mix, in twin screw extruder 220-270 ℃ then, extrude the water-cooled pelletizing under the 50rpm.
Behind above-mentioned blend pellet vacuum drying, be injection molded into standard Mechanics Performance Testing batten in 260-270 ℃, test by national standard, record PET blend shock strength at 600-900J/m.
Embodiment 1
Be 0.5 POE with 100 parts of MFI with after 3 parts of MAH and 0.2 part of DCP mix, in 180 ℃, extruding pelletization under the 30rpm obtains MAH-g-POE.85 parts of PET in 130 ℃ of dryings of vacuum drying oven after 8 hours, are done with 15 parts of MA-g-POE earlier and mix, in twin screw extruder 220-270 ℃ then, extrude the water-cooled pelletizing under the 50rpm.Behind the vacuum drying, be injection molded into standard in 270 ℃ and impact batten.Test result sees Table 1.
Embodiment 2
Be 0.5 POE with 100 parts of MFI with after 3 parts of MAH and 0.2 part of DCP mix, in 180 ℃, extruding pelletization under the 30rpm obtains MAH-g-POE.70 parts of PET in 130 ℃ of dryings of vacuum drying oven after 8 hours, are done with 30 parts MA-g-POE earlier and mix, in twin screw extruder 220-270 ℃ then, extrude the water-cooled pelletizing under the 50rpm.Behind the vacuum drying, be injection molded into standard in 270 ℃ and impact batten.Test result sees Table 1.
Embodiment 3
Be 2.5 POE with 100 parts of MFI with after 3 parts of MAH and 0.2 part of DCP mix, in 180 ℃, extruding pelletization under the 30rpm obtains MAH-g-POE.70 parts of PET in 130 ℃ of dryings of vacuum drying oven after 8 hours, are done with 30 parts MA-g-POE earlier and mix, in twin screw extruder 220-270 ℃ then, extrude the water-cooled pelletizing under the 50rpm.Behind the vacuum drying, be injection molded into standard in 270 ℃ and impact batten.Test result sees Table 1.
Table one embodiment PET MAH-g-POE Impact Strength
(POE?MFI?0.5)(POE?MFI?2.5) (J/m) 1 85 15 758 2 70 30 864 3 70 30 623

Claims (5)

1. the preparation method of a PET blend is characterized in that being undertaken by following step:
(1) by weight with 100 parts polyolefine thermoplastic elastomer and the maleic anhydride of 2-4 part, in 160-180 ℃, extruding pelletization under the 30rpm obtains maleic anhydride graft polyolefine thermoplastic elastomer behind the benzoyl peroxide thorough mixing of 0.05-0.4 part,
(2) with the PET of 70-85 part in 130 ℃ of dryings of vacuum drying oven after 8 hours, with the above-mentioned maleic anhydride graft polyolefine thermoplastic elastomer of 15-30 part in twin screw extruder 220-270 ℃, under the 50rpm blend extrude, granulation.
2. require the preparation method of described PET blend according to right 1, the intrinsic viscosity that it is characterized in that described PET is 0.7-1.0dl/g.
3. require the preparation method of described PET blend according to right 1, it is characterized in that described polyolefine thermoplastic elastomer is the multipolymer of ethene and octene.
4. require the preparation method of described PET blend according to right 3, it is characterized in that ethylene content is 65%-80% in the described multipolymer.
5. require the preparation method of described PET blend according to right 3, the melting index that it is characterized in that described multipolymer is 0.5-5.0g/10min.
CN98102049A 1998-06-05 1998-06-05 Impact-resistant polyester (PET) mixture and preparing process thereof Expired - Fee Related CN1086404C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN98102049A CN1086404C (en) 1998-06-05 1998-06-05 Impact-resistant polyester (PET) mixture and preparing process thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN98102049A CN1086404C (en) 1998-06-05 1998-06-05 Impact-resistant polyester (PET) mixture and preparing process thereof

Publications (2)

Publication Number Publication Date
CN1238356A CN1238356A (en) 1999-12-15
CN1086404C true CN1086404C (en) 2002-06-19

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102154733A (en) * 2011-03-09 2011-08-17 宁波大发化纤有限公司 Blended fiber of polyethylene terephthalate and polyethylene and preparation method thereof

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102234414A (en) * 2010-05-07 2011-11-09 财团法人塑胶工业技术发展中心 Toughened polyethylene terephthalate/polycarbonate compositions
CN108530848A (en) * 2018-04-25 2018-09-14 横店集团得邦工程塑料有限公司 High thermal deformation basalt fibre enhancing halogen-free flameproof PET material and preparation method thereof
CN108641309A (en) * 2018-04-25 2018-10-12 横店集团得邦工程塑料有限公司 A kind of relay halogen-free enhanced flame-retardant PBT material and preparation method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01201360A (en) * 1988-02-05 1989-08-14 Unitika Ltd Resin composition for extruded sheet
JPH01201359A (en) * 1988-02-05 1989-08-14 Unitika Ltd Resin composition for extruded sheet
JPH03285940A (en) * 1990-04-02 1991-12-17 Mitsui Petrochem Ind Ltd Polyolefin resin composition
CN1017812B (en) * 1987-11-13 1992-08-12 克罗瑞德无嗓音电源有限公司 Deposition apparatus
CN1135228A (en) * 1993-10-04 1996-11-06 伊斯曼化学公司 Concentrates for improving polyester compositions and method of making same
JP3285940B2 (en) * 1992-07-24 2002-05-27 松下電工株式会社 lighting equipment

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1017812B (en) * 1987-11-13 1992-08-12 克罗瑞德无嗓音电源有限公司 Deposition apparatus
JPH01201360A (en) * 1988-02-05 1989-08-14 Unitika Ltd Resin composition for extruded sheet
JPH01201359A (en) * 1988-02-05 1989-08-14 Unitika Ltd Resin composition for extruded sheet
JPH03285940A (en) * 1990-04-02 1991-12-17 Mitsui Petrochem Ind Ltd Polyolefin resin composition
JP3285940B2 (en) * 1992-07-24 2002-05-27 松下電工株式会社 lighting equipment
CN1135228A (en) * 1993-10-04 1996-11-06 伊斯曼化学公司 Concentrates for improving polyester compositions and method of making same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102154733A (en) * 2011-03-09 2011-08-17 宁波大发化纤有限公司 Blended fiber of polyethylene terephthalate and polyethylene and preparation method thereof
CN102154733B (en) * 2011-03-09 2013-07-03 宁波大发化纤有限公司 Blended fiber of polyethylene terephthalate and polyethylene and preparation method thereof

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