CN101550271A - Super toughness nylon resin and method for preparing same - Google Patents

Super toughness nylon resin and method for preparing same Download PDF

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Publication number
CN101550271A
CN101550271A CNA2009101348622A CN200910134862A CN101550271A CN 101550271 A CN101550271 A CN 101550271A CN A2009101348622 A CNA2009101348622 A CN A2009101348622A CN 200910134862 A CN200910134862 A CN 200910134862A CN 101550271 A CN101550271 A CN 101550271A
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China
Prior art keywords
nylon
resin
maleic anhydride
super
nylon resin
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Pending
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CNA2009101348622A
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Chinese (zh)
Inventor
张贞祥
官炳桂
涂日先
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HUIZHOU HUAJU PLASTICS TECHNOLOGY Co Ltd
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HUIZHOU HUAJU PLASTICS TECHNOLOGY Co Ltd
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Priority to CNA2009101348622A priority Critical patent/CN101550271A/en
Publication of CN101550271A publication Critical patent/CN101550271A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/625Screws characterised by the ratio of the threaded length of the screw to its outside diameter [L/D ratio]
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/04Particle-shaped
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/92895Barrel or housing

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The invention provides super thoughness nylon resin and a method for preparing same, comprising by weight: 65-85% nylon, 10-25% ethylenes elastic body grafted by maleic anhydride, 1-7% acrylonitrile-butadiene-styrene copolymer (ABS-g-MAH) grafted by maleic anhydride, 1-8% acrylonitrile-styrene copolymer (AS), and 1-3% other additives.

Description

Super toughness nylon resin and preparation method thereof
Technical field
The present invention relates to a kind of super toughness nylon resin and preparation method thereof.
Background technology
Nylon resin is the engineering plastics of developing the earliest, and it has tough and tensile, wear-resisting, anti-solvent, oil resistant, melt viscosity is low, raw material is easy to obtain, recyclable and cost performance advantages of higher.But there are some shortcomings in nylon, as has very strong notch sensitivity, and brittle rupture takes place when jagged, poor, the easy fracture of low-temperature flexibility, and by often occurring the not high phenomenon of glossiness behind the toughening modifying again, this has limited the range of application of nylon greatly.Therefore, the exploitation nylon that not only had super threading property but also had a good gloss degree becomes the direction of development.
At present, the technology of preparation high gloss super toughness nylon resin is not found relevant report.Mainly concentrate on the exploitation of super-toughened nylon for this type of exploitation, the main mode that adopts can be divided into physically modified and chemical modification two big classes, comprises grafts blending, elastic body toughening, receives and be confused polymer toughening, crosslinked toughness reinforcing etc.
The method for preparing high strength ultra tough nylon alloy has been introduced by Beijing University of Chemical Technology in the CN1510084 patent, utilization " nuclear-shell " type multipolymer is as anti-impact modifier, the polymkeric substance that adopts band high reactivity reactive functional group to close simultaneously is an expanding material, prepare the blend alloy material that each component has good consistency and dispersing uniformity, and make alloy material except having all good characteristics of nylon, also have outstanding toughness, low-temperature impact-resistant performance, cold flexibility, chemical resistant properties, environment resistant and lower water-absorbent.Yueyang Petrochemical Plant, Baling Petrochemical Corp has been introduced process for preparing nylon with high rigidity, super toughness and high resistance to low temp in the CN1353141 patent, this method is a base-material with PA6, PA66, make compound compatilizer with EVA/PE-g-MAH, by producing nylon alloy with toughner blend such as EAA, EVA, PE.Super-toughened nylon and preparation method thereof has been introduced in the CN1445278 patent by Shanghai Communications University, prepares nylon/polyolefin elastomerics super-toughened nylon by dynamic vulcanization maleic anhydride graft polyolefin elastomer.The high strength ultra tough nylon alloy of ageing resistance by ultraviolet light has been introduced by Zhuzhou Times new materials Science Co., Ltd in the CN1727407 patent, in nylon resin, be that the polymkeric substance of main toughner, band oxygen functional group is secondary toughner, adds compound ultraviolet light auxiliary agent and oxidation inhibitor simultaneously by adding polymkeric substance that an amount of band high reaction activity official can close, improve the over-all properties of nylon resin, make alloy material have the aging and good mechanical strength of excellent in resistance low-temperature impact, ultraviolet resistance.Chen Zhicheng, Sun Shulin etc. have been delivered " research of ABS-g-MAH toughened polyamide 6 " article in " Chinese plastics " 2007 the 21st the 3rd phases of volume, adopt acrylonitrile-butadiene-styrene copolymer (ABS) and maleic anhydride (MAH) grafting with nucleocapsid structure to carry out toughness reinforcing to polyamide 6 (PA6).
Summary of the invention
The objective of the invention is to raising, a kind of high gloss super toughness nylon resin is provided,, make product can satisfy the use range of requirements at the higher level improving further its glossiness that improves on the flexible basis at super-toughened nylon performance and product appearance requirement.
Another object of the present invention provides the preparation method of high gloss super-toughened nylon.
Technical scheme of the present invention is as follows: the high gloss super toughness nylon resin, by comprising that weight percent is 65 ~ 85% nylon 6 or nylon 66, the vinyl elastomerics of 10 ~ 25% maleic anhydride graft, 1 ~ 7% maleic anhydride graft acrylonitrile-butadiene-styrene copolymer (ABS-g-MAH), 1 ~ 8% acrylonitritrile-styrene resin (AS), other auxiliary agent of 1 ~ 3% is formed.
Above-mentioned nylon resin is nylon 66 (PA66) and nylon 6 (PA6), different for nylon component size and distribution, the viscosity difference is bigger, viscosity scope having between 2.2 ~ 4.5, consider and do glossiness and all reasonable nylon of toughness, in composition, select the PA66 or the PA6 of 2.7 viscositys; Nylon is easy to suction, before use will be in 90 ~ 110 ℃ drying hopper dry 3 ~ 4 hours.Part by weight in whole composition is 65 ~ 85% for PA66 or PA6, is preferably 70 ~ 80%.
The consistency of above-mentioned maleic anhydride graft acrylonitrile-butadiene-styrene copolymer and acrylonitritrile-styrene resin (AS).The ratio of vinyl elastomerics in whole composition of maleic anhydride graft is 10 ~ 25%, and best ratio is 17 ~ 23%.
Above-mentioned maleic anhydride graft acrylonitrile-butadiene-styrene copolymer (ABS-g-MAH), percentage of grafting is 1.1%, in this system, mainly utilize the nucleocapsid structure of acrylonitrile-butadiene-styrene copolymer (ABS), keep favorable rigidity simultaneously at the raising flexible; ABS has good glossiness again, and its grafts has also guaranteed the glossiness of resin in toughness reinforcing; Because of it has vinyl cyanide and styrene group, guaranteed the consistency of acrylonitritrile-styrene resin (AS) in whole system.ABS-g-MAH ratio in whole composition is 1 ~ 7%, and preferably ratio is 3 ~ 5%.
Above-mentioned acrylonitritrile-styrene resin (AS) has the differentiation of the blue end, the yellow end and white background on color, in order to guarantee good color, select the AS of white background here, utilizes AS can form nucleocapsid structure to guarantee toughness in elastomerics; Make full use of the good glossiness of AS simultaneously, make it in super-toughened nylon, improve glossiness.AS ratio in whole composition is 1 ~ 8%, and preferably ratio is 3 ~ 5%.
Other auxiliary agent of above-mentioned 1 ~ 3% mainly is 0.5 ~ 2% organo-silicic oil, the nucleator about 0.1-0.4%, the oxidation inhibitor about 0.2-0.5% and thermo-stabilizer.
The preparation method of above-mentioned materials is as follows: nylon in 90 ~ 110 ℃ drying hopper dry 3 ~ 4 hours, nylon with formula ratio, the vinyl elastomerics of maleic anhydride graft, maleic anhydride graft acrylonitrile-butadiene-styrene copolymer (ABS-g-MAH), acrylonitritrile-styrene resin (AS), after various auxiliary agents mix in the high-speed stirring bucket, from the batch mixing mouth, join temperature and be set at 230 ℃ ~ 290 ℃, length-to-diameter ratio (L/D) is 36: 1 ~ 48: 1 a screw combinations, by in the twin screw extruder of process stipulation, vacuumize granulation and make the high gloss super toughness nylon resin.
The product that makes by twin screw extruder has glossiness height and good toughness, and over-all properties is than more excellent, and is respond well.
The present invention is further described below by embodiment.
Embodiment one: high gloss super-toughened nylon 6 resin
Table one embodiment 1 ~ 5
Figure A20091013486200071
Nylon 6 in 90 ~ 110 ℃ drying hopper dry 3 ~ 4 hours, ratio in top embodiment weighs up, earlier the vinyl elastomerics of PA6, maleic anhydride graft, ABS-g-MAH, AS are added in the high-speed stirring bucket, add auxiliary agent then, in the high-speed stirring bucket, stir after 5 minutes, joining temperature from the batch mixing mouth is set in 40: 1 twin screw extruders of 230 ℃ ~ 270 ℃, length-to-diameter ratio (L/D), vacuumize granulation and make the high gloss super toughness nylon resin, the sampling material is injection molded into the standard batten 90 ~ 110 ℃ of dryings after 3 ~ 4 hours, carry out performance test, performance sees Table two.
The The performance test results of table two embodiment 1 ~ 5
Figure A20091013486200081
Embodiment two: high gloss super-toughened nylon 66 resin
Table three embodiment 6 ~ 10
Figure A20091013486200082
Figure A20091013486200091
Nylon 66 in 90 ~ 110 ℃ drying hopper dry 3 ~ 4 hours, ratio in top embodiment weighs up, earlier PA66, the vinyl elastomerics of maleic anhydride graft, ABS-g-MAH, AS adds in the high-speed stirring bucket, add auxiliary agent then, in the high-speed stirring bucket, stir after 5 minutes, from the batch mixing mouth, join temperature and be set at 240 ℃ ~ 290 ℃, in 40: 1 twin screw extruders of length-to-diameter ratio (L/D), vacuumize granulation and make the high gloss super toughness nylon resin, the sampling material is injection molded into the standard batten 90 ~ 110 ℃ of dryings after 3 ~ 4 hours, carry out performance test, performance sees Table four.
The The performance test results of table four embodiment 6 ~ 10
Figure A20091013486200092

Claims (2)

1, a kind of super toughness nylon resin, it is characterized in that: by comprising that weight percent is 65 ~ 85% nylon 6 or nylon 66, the vinyl elastomerics of 10 ~ 25% maleic anhydride graft, 1 ~ 7% maleic anhydride graft acrylonitrile-butadiene-styrene copolymer, 1 ~ 8% acrylonitritrile-styrene resin, and 1 ~ 3% silicone based lubricant, oxidation inhibitor, nucleator, thermo-stabilizer are formed.
2, the preparation method of super toughness nylon resin as claimed in claim 1, it is characterized in that: nylon in 90 ~ 110 ℃ drying hopper dry 3 ~ 4 hours, mix in the high-speed stirring bucket preparing material on request, joining temperature from the batch mixing mouth, to be set at 230 ℃ ~ 290 ℃, length-to-diameter ratio (L/D) be 36: 1 ~ 48: 1 screw combinations, by in the twin screw extruder of process stipulation, vacuumize granulation and make.
CNA2009101348622A 2008-04-03 2009-04-03 Super toughness nylon resin and method for preparing same Pending CN101550271A (en)

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CN200810027201.5 2008-04-03
CN200810027201 2008-04-03
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102276977A (en) * 2011-06-10 2011-12-14 东莞劲胜精密组件股份有限公司 High-performance anti-warping nylon material and preparation method thereof
CN103205122A (en) * 2013-04-28 2013-07-17 常熟市筑紫机械有限公司 Preparation method of polyamide alloy material modified by styrene-acrylonitrile copolymer
CN103232704A (en) * 2013-04-28 2013-08-07 常熟市筑紫机械有限公司 Styrene-acrylonitrile copolymer modified polyamide alloy material
CN103242654A (en) * 2013-04-28 2013-08-14 常熟市筑紫机械有限公司 Preparation method of styrene-acrylonitrile copolymer modified polyamide composite material
WO2014018738A1 (en) * 2012-07-26 2014-01-30 Invista Technologies S.A R.L. Thermoplastic composition for use in high impact applications
CN103571184A (en) * 2012-07-31 2014-02-12 金发科技股份有限公司 Nylon 6 molding composition, and preparation method and application thereof
CN105647177A (en) * 2016-02-04 2016-06-08 南通瑞隆新材料有限公司 Preparation method of ABS-toughened polyamide
US9388312B2 (en) 2012-07-26 2016-07-12 Invista North America S.A.R.L. Thermoplastic composition for use in high impact applications

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102276977A (en) * 2011-06-10 2011-12-14 东莞劲胜精密组件股份有限公司 High-performance anti-warping nylon material and preparation method thereof
CN102276977B (en) * 2011-06-10 2015-03-18 东莞劲胜精密组件股份有限公司 High-performance anti-warping nylon material and preparation method thereof
WO2014018738A1 (en) * 2012-07-26 2014-01-30 Invista Technologies S.A R.L. Thermoplastic composition for use in high impact applications
CN104684999A (en) * 2012-07-26 2015-06-03 因温斯特技术公司 Thermoplastic composition for use in high impact applications
US9056982B2 (en) 2012-07-26 2015-06-16 Invista North America S.A.R.L. Thermoplastic composition for use in high impact applications
US9388312B2 (en) 2012-07-26 2016-07-12 Invista North America S.A.R.L. Thermoplastic composition for use in high impact applications
CN103571184A (en) * 2012-07-31 2014-02-12 金发科技股份有限公司 Nylon 6 molding composition, and preparation method and application thereof
CN103571184B (en) * 2012-07-31 2017-04-19 金发科技股份有限公司 Nylon 6 molding composition, and preparation method and application thereof
CN103205122A (en) * 2013-04-28 2013-07-17 常熟市筑紫机械有限公司 Preparation method of polyamide alloy material modified by styrene-acrylonitrile copolymer
CN103232704A (en) * 2013-04-28 2013-08-07 常熟市筑紫机械有限公司 Styrene-acrylonitrile copolymer modified polyamide alloy material
CN103242654A (en) * 2013-04-28 2013-08-14 常熟市筑紫机械有限公司 Preparation method of styrene-acrylonitrile copolymer modified polyamide composite material
CN105647177A (en) * 2016-02-04 2016-06-08 南通瑞隆新材料有限公司 Preparation method of ABS-toughened polyamide

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Inventor after: Zhang Zhenxiang

Inventor after: Guan Binggui

Inventor after: Tu Rixian

Inventor after: Chen Xudong

Inventor before: Zhang Zhenxiang

Inventor before: Guan Binggui

Inventor before: Tu Rixian

COR Change of bibliographic data

Free format text: CORRECT: INVENTOR; FROM: ZHANG ZHENXIANG GUAN BINGGUI TU RIXIAN TO: ZHANG ZHENXIANG GUAN BINGGUI TURIXIAN CHEN XUDONG

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Open date: 20091007