CN102294812A - Polystyrene wood-like profile and preparation method thereof - Google Patents

Polystyrene wood-like profile and preparation method thereof Download PDF

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Publication number
CN102294812A
CN102294812A CN2010102089897A CN201010208989A CN102294812A CN 102294812 A CN102294812 A CN 102294812A CN 2010102089897 A CN2010102089897 A CN 2010102089897A CN 201010208989 A CN201010208989 A CN 201010208989A CN 102294812 A CN102294812 A CN 102294812A
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CN
China
Prior art keywords
polystyrene
layer material
skin
masterbatch
high impact
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
CN2010102089897A
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Chinese (zh)
Inventor
李志杰
李晓强
张文杰
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.)
ZIBO INTCO FRAMING PRODUCTS CO Ltd
SHANGHAI INTCO INDUSTRIAL Co Ltd
Original Assignee
ZIBO INTCO FRAMING PRODUCTS CO Ltd
SHANGHAI INTCO INDUSTRIAL Co Ltd
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Publication date
Application filed by ZIBO INTCO FRAMING PRODUCTS CO Ltd, SHANGHAI INTCO INDUSTRIAL Co Ltd filed Critical ZIBO INTCO FRAMING PRODUCTS CO Ltd
Priority to CN2010102089897A priority Critical patent/CN102294812A/en
Publication of CN102294812A publication Critical patent/CN102294812A/en
Pending legal-status Critical Current

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Classifications

    • 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
    • B29C2948/9258Velocity
    • B29C2948/9259Angular velocity
    • 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
    • B29C2948/92885Screw or gear
    • 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

Abstract

The invention relates a preparation method of a polystyrene microcellular foam co-extruded wood-like material. The method is characterized by comprising the following steps: preparing a surface layer material and a core layer material, respectively feeding the surface layer material and the core layer material in an auxiliary extruder and a main extruder, co-extruding the surface layer material and the core layer material into a mold by the two extruders and integrating the surface layer material and the core layer material into a whole in the mold, wherein the surface layer material coats the surface of the core layer material. The base material of the surface layer material is high-impact polystyrene and comprises flow-line color masterbatch which has good compatibility with the high-impact polystyrene, and has fluidity and dispersibility different from those of the high-impact polystyrene; the core layer material is a polystyrene microcellular foam material, the weight ratio of the core layer material to the surface layer material is 85-95%: 5-15%. Various products with different effects can be produced under the conditions that the colors and qualities of the added primary color masterbatch and flow-line color masterbatch are different, the types of the flow-line color masterbatch are different and the processing processes are different; and the produced products with different effects include various wood-grain-like products, various products with different designs and colors and the like.

Description

A kind of polystyrene imitating wood section and preparation method thereof
Technical field
The present invention relates to the little foaming co-extrusion method of a kind of polystyrene.Be specifically related to the little foaming co-extrusion of a kind of polystyrene imitated wood material and preparation method thereof.
Background technology
Series of advantages such as the polystyrene imitating wood section has that light weight, price are low, insect protected, mothproof, moisture-proof, asepsis environment-protecting, long service life.Be widely used in places such as photo frame, picture frame, home decoration material.The technology of imitative wood grain mainly contains following several in the imitated wood material manufacturing process of polystyrene at present: use the various decorative patterns of reflex printing on the surface of polystyrene extruded material 1.; 2. make various decorative patterns at the surface lacquer of polystyrene extruded material; 3. coat gypsum on the surface of polystyrene extruded material, spray paint then and make various decorative patterns.Wherein use the technology of reflex printing wood grain complicated, it is higher to consume energy, and need special equipment that paster and material are heated so that printing ink prints on the polystyrene material, and the paster waste is bigger; The wood grain kind that surface lacquer technology is made is less, and lacquer comes off easily; Gypsum coats lacquer spraying technique, though the lacquer difficult drop-off, itself comes off gypsum easily, and service life is shorter.Therefore demand developing a kind of preparation method of polystyrene imitating wood section urgently, to satisfy the demand in market.
Summary of the invention
The objective of the invention is to provides a kind of high efficiency wood grain manufacture craft for the little foaming co-extrusion of polystyrene material shows, to overcome the defective of prior art.The present invention designs a kind of preparation method of polystyrene imitating wood section, it is characterized in that: preparation skin-material and core material, skin-material and core material are put into respectively in auxiliary extruder and the main extruder, in two extruders co-extrusion to a mould, combine together in mould, wherein skin-material is coated on the surface of core material.The skin-material base material be high impact polystyrene and contain with the high impact polystyrene compatibility good, but mobile and dispersed different flow liner look mother, core material is the polystyrene micro-foaming material, and core material and skin-material weight ratio are 85-95%: 5-15%.Being formulated as of skin-material: get 100 parts of high impact polystyrenes, add primary colours Masterbatch 1-5 part and flow liner Masterbatch 1-5 part, use low speed mixer to mix; Being formulated as of core material: get 100 parts of polystyrene, blowing agent 1-5 part, Masterbatch 1-5 part, plasticizer 1-3 part adds high-speed mixer and mixes.The primary colours Masterbatch is better mobile, is uniformly dispersed, and flow liner look mother is and the high impact polystyrene compatibility is good but melt index is lower, and is dispersed relatively poor in high impact polystyrene.The processing temperature that adds the extruder of core material is 130-180 ℃, and screw speed is 10-35rpm, and the extruder processing temperature that adds skin-material is 150-180 ℃, and screw speed is 5-40rpm.The wood-imitating type material surface of coextrusion produces the embossing of stereoeffect or other effect and handles.Preparation principle disclosed in this invention is: utilize the Masterbatch of different substrate materials, make primary colours Masterbatch and flow liner Masterbatch respectively.Wherein the flowability of primary colours Masterbatch and better dispersed is dispersed in process and forms background color in the polystyrene material, and the flow liner look female and the high impact polystyrene compatibility is good, but melt index is lower, and is dispersed relatively poor in high impact polystyrene.In process, can not be dispersed in the polystyrene material, along with extruding of material forms wood grain or other decorative pattern.Different according to primary colours Masterbatch that skin-material added and flow liner Masterbatch color, the difference of component, the difference of the kind of flow liner Masterbatch, the difference of processing technology can be produced the product of multiple different-effect.As various imitative wood grain products, the product of various patterns etc.
The specific embodiment
Preparation skin-material and core material, skin-material and core material are put into respectively in auxiliary extruder and the main extruder, in two extruders co-extrusion to a mould, in mould, combine together, wherein skin-material is coated on the surface of core material, the shared weight ratio of core material is 85-95%, and the shared weight ratio of skin-material is 5-15%.The skin-material base material be high impact polystyrene and contain with the high impact polystyrene compatibility good, but melt index is lower, dispersed relatively poor flow liner look mother in high impact polystyrene, core material is the polystyrene micro-foaming material, being formulated as of skin-material: get 100 parts of high impact polystyrenes, add primary colours Masterbatch 1-5 part and flow liner Masterbatch 1-5 part, use low speed mixer to mix.Wherein the primary colours Masterbatch is better mobile, is uniformly dispersed, and the flow liner look female and the high impact polystyrene compatibility is good, but melt index is lower, and is dispersed relatively poor in high impact polystyrene.Being formulated as of core material: get 100 parts of polystyrene, blowing agent 1-5 part, Masterbatch 1-5 part, plasticizer 1-3 part adds high-speed mixer and mixes.The processing temperature that adds the extruder of core material is 130-180 ℃, and screw speed is 10-35rpm, and the extruder processing temperature that adds skin-material is 150-180 ℃, and screw speed is 5-40rpm.The wood-imitating type material surface of coextrusion produces the embossing of stereoeffect or other effect and handles.
High impact polystyrene primary colours look mother of the present invention comprises following components in weight percentage: high impact polystyrene I 90%-98% pigment I 1.5%-8%, antioxidant 0.2%-1% and ultra-violet absorber 0.3%-1%, above-mentioned material is stirred with high mixer, add in the double screw extruder, extrude pelletizing, promptly get high impact polystyrene primary colours Masterbatch;
High impact polystyrene I among the aforesaid high impact polystyrene primary colours look mother be melt flow rate (MFR) be 5-20g/10min (200 ℃, extrusion grade high impact polystyrene 5Kg), pigment I adds various environmental-friendly pigments according to the color demand;
High impact polystyrene flow liner look mother of the present invention comprises following components in weight percentage: high impact polystyrene II 70%-85%ABS 13%-20% pigment II 1.5%-8% antioxidant 0.2%-1% ultra-violet absorber 0.3%-1%, above-mentioned material is stirred with high mixer, add in the double screw extruder, extrude pelletizing, promptly get high impact polystyrene flow liner Masterbatch;
High impact polystyrene II among the aforesaid high impact polystyrene flow liner look mother be melt turnover be 0.5-5g/10min (200 ℃, high impact polystyrene 5Kg), pigment II adds various environmental-friendly pigments according to the color demand;
Being formulated as of skin-material: get 100 parts of weight of high impact polystyrene, add primary colours Masterbatch 1-5 part weight and flow liner Masterbatch 1-5 part weight, the use low speed mixer mixes, wherein the primary colours Masterbatch requires better mobile, be uniformly dispersed, the requirement of flow liner look female is good with the high impact polystyrene compatibility but mobile and dispersed different.Being formulated as of core material: get 100 parts of weight of polystyrene, blowing agent 1-5 part weight, Masterbatch 1-5 part weight, plasticizer 1-3 part weight adds high-speed mixer and mixes.The processing temperature that adds the extruder of core material is 130-180 ℃, and screw speed is 10-35rpm, and the extruder processing temperature that adds skin-material is 150-180 ℃, and screw speed is 5-40rpm.This material processing technique is that double-layer coextrusion goes out processing, and wherein skin-material is a high impact polystyrene, and core material is the polystyrene micro-foaming material.Two kinds of materials use in two extruders co-extrusion to a mould, combine together in mould, and wherein skin-material is coated on the surface of core material.Wherein the shared weight ratio of core material is 85-95%, and the shared weight ratio of skin-material is 5-15%.
Embodiment 1---and 4
1. high impact polystyrene material (HIPS), primary colours Masterbatch, flow liner Masterbatch are prepared in proportion, add the low speed mixer mixing as the skin-material raw material.Material prescription specifically sees Table one (1 weight portion 1 kilogram)
Table one
2. with 100 parts of polystyrene materials, 2 parts of blowing agents, 1 part of Masterbatch (embodiment 1-2 uses yellow Masterbatch, embodiment 3-4 to use white Masterbatch), 2 parts in plasticizer adds high-speed mixer and mixes as the core material raw material.
Wherein blowing agent can use the Hangzhou ancient cooking vessel to get over the AK-8 blowing agent of chemical industry Co., Ltd;
Masterbatch can use the H palette master batch of new particle chemical color limited company;
Plasticizer can use dioctyl phthalate.
The sandwich layer polystyrene material can use the recovery polystyrene material.
Co-extrusion modling: process equipment comprises the main extruder of single screw extrusion machine conduct and auxiliary extruder of single screw extrusion machine conduct that screw diameter is φ 45 that a screw diameter is φ 90.Core material added in the main extruder extrude, will skin-material add in the auxiliary extruder and extrude, material imports in the co-extruding mould, cooling forming.Wherein main extruder processing temperature is 130-180 ℃, and screw speed is 10-35rpm, auxiliary extruder barrel processing temperature such as table two, and screw speed is 5-40rpm.
Table two
Figure BSA00000181857400051
The extruded product surface effect is: embodiment 1-2 is imitative wood grain effect, and 1 lines is closeer, and 2 lines is lighter, and embodiment 3-4 is a purple flow liner effect, 3 lines comparatively dense, and 4 lines is lighter.

Claims (6)

1. the preparation method of a polystyrene imitating wood section, it is characterized in that: preparation skin-material and core material, skin-material and core material are put into respectively in auxiliary extruder and the main extruder, in two extruders co-extrusion to a mould, combine together in mould, wherein skin-material is coated on the surface of core material.
2. polystyrene imitating wood section, it is characterized in that: the skin-material base material be high impact polystyrene and contain with the high impact polystyrene compatibility good, but mobile and dispersed different flow liner look mother, core material is the polystyrene micro-foaming material, and core material and skin-material weight ratio are 85-95%: 5-15%.
3. by the described a kind of polystyrene imitating wood section of claim 2, it is characterized in that: being formulated as of skin-material: get 100 parts of high impact polystyrenes, add primary colours Masterbatch 1-5 part and flow liner Masterbatch 1-5 part, use low speed mixer to mix; Being formulated as of core material: get 100 parts of polystyrene, blowing agent 1-5 part, Masterbatch 1-5 part, plasticizer 1-3 part adds high-speed mixer and mixes.
4. by the described a kind of polystyrene imitating wood section of claim 3, it is characterized in that: the primary colours Masterbatch is for better mobile, be uniformly dispersed, flow liner look mother is and the high impact polystyrene compatibility is good but melt index is lower, and is dispersed relatively poor in high impact polystyrene.
5. press the preparation method of the described a kind of polystyrene imitating wood section of claim 1, it is characterized in that: the processing temperature that adds the extruder of core material is 130-180 ℃, screw speed is 10-35rpm, the extruder processing temperature that adds skin-material is 150-180 ℃, and screw speed is 5-40rpm.
6. by the preparation method of the described a kind of polystyrene imitating wood section of claim 1, it is characterized in that: the wood-imitating type material surface of coextrusion produces the embossing of stereoeffect or other effect and handles.
CN2010102089897A 2010-06-24 2010-06-24 Polystyrene wood-like profile and preparation method thereof Pending CN102294812A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103213366A (en) * 2012-01-19 2013-07-24 上海英科实业有限公司 Glass fiber reinforced polystyrene micro-foam double-layer co-extrusion section and its making method
CN104895266A (en) * 2014-03-07 2015-09-09 于珓 MW-wood imitation building material
CN105108992A (en) * 2015-08-28 2015-12-02 上海伊兆实业有限公司 Production process of picture frame strip
CN114311863A (en) * 2021-12-29 2022-04-12 黄山美森新材料科技股份有限公司 High-temperature-resistant and flame-retardant co-extruded polystyrene foam material and preparation method thereof

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103213366A (en) * 2012-01-19 2013-07-24 上海英科实业有限公司 Glass fiber reinforced polystyrene micro-foam double-layer co-extrusion section and its making method
CN103213366B (en) * 2012-01-19 2016-06-22 上海英科实业有限公司 Styrafil fretting map dual-layer coextrusion section and preparation method thereof
CN104895266A (en) * 2014-03-07 2015-09-09 于珓 MW-wood imitation building material
CN105108992A (en) * 2015-08-28 2015-12-02 上海伊兆实业有限公司 Production process of picture frame strip
CN114311863A (en) * 2021-12-29 2022-04-12 黄山美森新材料科技股份有限公司 High-temperature-resistant and flame-retardant co-extruded polystyrene foam material and preparation method thereof
CN114311863B (en) * 2021-12-29 2023-09-29 黄山美森新材料科技股份有限公司 High-temperature-resistant flame-retardant co-extruded polystyrene foam material and preparation method thereof

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Application publication date: 20111228