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CN101508818A - ABS//PET alloy and method for producing the same - Google Patents

ABS//PET alloy and method for producing the same Download PDF

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Publication number
CN101508818A
CN101508818A CNA2008102413272A CN200810241327A CN101508818A CN 101508818 A CN101508818 A CN 101508818A CN A2008102413272 A CNA2008102413272 A CN A2008102413272A CN 200810241327 A CN200810241327 A CN 200810241327A CN 101508818 A CN101508818 A CN 101508818A
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CN
China
Prior art keywords
abs
pet
pet alloy
district temperature
alloy
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
CNA2008102413272A
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Chinese (zh)
Inventor
徐东
贺永
杨德武
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.)
Polymer Science Shenzhen New Materials Co Ltd
Original Assignee
Polymer Science Shenzhen New Materials 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.)
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Priority to CNA2008102413272A priority Critical patent/CN101508818A/en
Publication of CN101508818A publication Critical patent/CN101508818A/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
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/918Thermal treatment of the stream of extruded material, e.g. cooling characterized by differential heating or cooling
    • B29C48/9185Thermal treatment of the stream of extruded material, e.g. cooling characterized by differential heating or cooling in the direction of the stream of the material
    • 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
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B29C48/40Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
    • 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
    • B29C2948/92514Pressure
    • 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
    • B29C2948/92561Time, e.g. start, termination, duration or interruption
    • 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
    • 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
    • B29C2948/92904Die; Nozzle zone

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The invention discloses an ABS/PET alloy and a preparation method thereof. The ABS/PET alloy comprises the components with the weight percentage as follows: 21-72 percent of ABS, 14-60 percent of PET, 3-10 percent of compatilizer, 0.4-0.6 percent of antioxidant, 5-15 percent of toughener and 0.3-1 percent of lubricant. In the invention, proper compatilizer and intensifier are selected to melt an ABS system and a PET system together very well and the material which has stable size, high strength, high modulus and high fluidity is produced. The ABS/PET alloy integrates the advantages of ABS and PET and improves the heat resistance, impact resistance, processability and the like of the PET. The method for manufacturing the ABS/PET alloy comprises the technical steps as follows: firstly, the raw materials are mixed in proportion as above and then are put into a plastic extruder to be granulated at the temperature controlled within 230 DEG C to 260 DEG C; and the ABS/PET alloy is obtained.

Description

A kind of ABS/PET Alloy And Preparation Method
Technical field
The present invention relates to technical field of polymer materials, relate in particular to a kind of ABS/PET Alloy And Preparation Method.
Background technology
ABS resin is the current production rate maximum, most widely used plastics.It not only has tough, hard, firm phase isostatic mechanical property, and has dimensional stability, lower temperature resistance and processing fluidity preferably.ABS is an acrylonitrile-butadiene-styrene terpolymer, has gathered rigidity that glossiness that vinylbenzene has and plasticity, vinyl cyanide have and resistance to chemical reagents and excellent mechanical property, shock-resistance that divinyl has.
PET (polyethylene terephthalate) is a those semi-crystalline materials, and extraordinary chemical stability, physical strength, electrical insulation characteristics and thermostability are arranged, especially oil-proofness and solvent resistance excellence.PET uses separately, exists shortcomings such as impact property is not high, size instability, and these shortcomings are restricting the application of PET.And at present, still ABS and PET resin are not made the alloy application facet.
Summary of the invention
The object of the present invention is to provide a kind of ABS/PET Alloy And Preparation Method, make the material make have outstanding toughness and dimensional stability, high strength, high workability, resistance to chemical reagents.
For solving the problems of the technologies described above, the objective of the invention is to be achieved through the following technical solutions:
A kind of ABS/PET alloy, its composition is (%) by weight ratio: ABS 21-72%; PET14-60%; Compatilizer 3-10%; Oxidation inhibitor 0.4-0.6%; Toughner 5-15%; Lubricant 0.3-1%.
Wherein, also comprise toughener, its composition is (%): 5-15% by weight ratio.
Wherein, described ABS is vinyl cyanide, divinyl, styrene copolymer, and its rubber content is 35%-70%.
Wherein, described PET is a relative density 1.35~1.38,255~260 ℃ of fusing points, and melt viscosity is at the polyethylene terephthalate more than 0.9.
Wherein, described compatilizer is the one or more combination thing in ABS-g-MAH, ABS-g-GMA, AS-g-MAH, SEBS-g-MAH, glycidyl methacrylate (GMA), methyl methacrylate (MMA)-glycidyl methacrylate (GMA)-propylene ethyl ester (EA) ter-polymers (MGE).
Wherein, described toughner is the one or more combination thing in macromolecular elastomer NBR, TPU, SEBS, EPDM, high glue powder or the MBS core-shell type anti-impact modifier.
Wherein, described toughener is the one or more combination thing in organic rigid material MMA/St multipolymer, PMMA, MBS, PS, SAN or inorganic reinforcement glass fibre, carbon fiber, mica powder, kaolin, talcum powder, wollastonite, glass microballon, the whisker.
Wherein, described oxidation inhibitor is the composite of four [3-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester primary antioxidants and tricresyl phosphite (2,4-di-t-butyl phenyl ester) auxiliary anti-oxidant.
Wherein, described lubricant is the one or more combination thing in polysiloxane, calcium stearate, Zinic stearas, Magnesium Stearate, PE wax, PP wax, ABS wax, EVA wax, the ethylene bis stearamide.
A kind of preparation method of described ABS/PET alloy comprises step:
A: take by weighing ABS and PET resin by weight ratio, mix;
B: take by weighing compatilizer and toughner by weight ratio, mix;
C: take by weighing other auxiliary agents such as oxidation inhibitor, lubricant by weight ratio, mix, the above-mentioned material that mixes is put in the mixing tank together continued all to mix up to evenly;
D: mixed raw materials is put into the loading hopper of twin screw extruder, through melt extruding granulation; Complete processing is as follows: twin screw extruder one district temperature 230-260 ℃, two district temperature 230-260 ℃, three district temperature 230-260 ℃, four district temperature 230-260 ℃, five district temperature 230-260 ℃, six district temperature 230-260 ℃, seven district temperature 230-260 ℃, eight district temperature 230-260 ℃, head 230-260 ℃, residence time 2-3min, pressure are 12-18MPa.
Above technical scheme as can be seen, the present invention has following beneficial effect:
1: ABS/PET alloy compatilizer of the present invention and toughner, also improved the toughness of alloy simultaneously significantly in the consistency that improves ABS and PET, prepared ABS/PET alloy has the toughness of superelevation.
2: the super tough ABS/PET that the present invention makes keeps the physical and mechanical property of other every excellences of material when having superhigh tenacity.
3: the preparation technology of a kind of ABS/PET alloy that the present invention proposes is simple, cost is low.
Embodiment
ABS/PET is the mixture of acrylonitrile-butadiene-styrene terpolymer and polyethylene terephthalate, make up for each other's deficiencies and learn from each other, both improved the flowability of ABS, reduced the cost of ABS, improve the toughness of PET again, thereby had excellent comprehensive performances.ABS/PET is suitable for the office appliance shells such as computer peripheral equipment, printer and duplicating machine of automobile component, automotive trim, bumper skeleton, household appliances shell, top grade etc.
A kind of ABS/PET alloy provided by the invention, its composition is (%): ABS21-72% by weight ratio; PET 14-60%; Compatilizer 3-10%; Oxidation inhibitor O.4-0.6%; Toughner 5-15%; Lubricant 0.3-1%.
Wherein, described ABS is vinyl cyanide, divinyl, styrene copolymer, and its rubber content is 35%-70%; Described PET is a relative density 1.35~1.38,255~260 ℃ of fusing points, and melt viscosity is at the polyethylene terephthalate more than 0.9; Described compatilizer is the one or more combination thing in ABS-g-MAH, ABS-g-GMA, AS-g-MAH, SEBS-g-MAH, glycidyl methacrylate (GMA), methyl methacrylate (MMA)-glycidyl methacrylate (GMA)-propylene ethyl ester (EA) ter-polymers (MGE); Described toughner is the one or more combination thing in polymer elastomerics NBR, TPU, SEBS, EPDM, high glue powder or the MBS core-shell type anti-impact modifier; Described toughener is the one or more combination thing in organic rigid material MMA/St multipolymer, PMMA, MBS, PS, SAN or inorganic reinforcement glass fibre, carbon fiber, mica powder, kaolin, talcum powder, wollastonite, glass microballon, the whisker; Described oxidation inhibitor is the composite of four [3-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester primary antioxidants and tricresyl phosphite (2,4-di-t-butyl phenyl ester) auxiliary anti-oxidant; Described lubricant is the one or more combination thing in polysiloxane, calcium stearate, Zinic stearas, Magnesium Stearate, PE wax, PP wax, ABS wax, EVA wax, the ethylene bis stearamide.
In the present invention, take by weighing dry good ABS and PET resin and auxiliary agent by weight ratio; The starting material that weigh up are put into the dried 3~5min of mixing in the super mixer; At last mixed raw materials is put into the loading hopper of twin screw extruder, through melt extruding granulation.Complete processing is as follows: twin screw extruder one district temperature 230-260 ℃, two district temperature 230-260 ℃, three district temperature 230-260 ℃, four district temperature 230-260 ℃, five district temperature 230-260 ℃, six district temperature 230-260 ℃, seven district temperature 230-260 ℃, eight district temperature 230-260 ℃, head 230-260 ℃, residence time 2-3min, pressure are 12-18MPa.
For ease of the present invention is further understood, now describe the present invention in conjunction with specific embodiments:
In the composite-material formula of the following example, oxidation inhibitor is four [3-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester, tricresyl phosphite (2,4-di-t-butyl phenyl ester) selects for use Ciba company to produce, trade names are respectively Irganox1010, and Irganox168.Compatilizer is selected GMA type compatilizer for use, produces as logical plastic cement company limited of Shenyang section, and trade names KT-22, or the production of the four-dimensional superpolymer plastic cement in Shenyang company limited, trade names are SWR-6B etc.Toughner is selected polymer elastomeric-type toughner for use, as the NBR that U.S. GOOD YEAR company produces, trade mark P83.
Embodiment 1:
The ABS weight ratio is 71.3% (below be weight ratio), PET15%, toughener 5%, 1010/1680.2/0.2%, compatilizer 3%, toughner 5%, lubricant 0.3%.The material that mixes is joined in the hopper of twin screw extruder, through melt blending, extruding pelletization becomes matrix material.Wherein, screw rod is respectively distinguished the temperature setting and is respectively: district's temperature: 200 ℃; Two districts: 210 ℃; Three districts: 220 ℃; Four districts: 230 ℃; Five districts: 230 ℃; Six districts: 230 ℃; Seven districts: 230 ℃; Eight districts: 220 ℃; Head: 220 ℃; The residence time 2~3min.Pressure is 15MPa.
Embodiment 2:
The ABS weight ratio is 56.1% (below be weight ratio), PET20%, toughener 10%, 1010/1680.2/0.2%, compatilizer 5%, toughner 8%, lubricant 0.5%.The material that mixes is joined in the hopper of twin screw extruder, through melt blending, extruding pelletization becomes matrix material.Wherein, screw rod is respectively distinguished the temperature setting and is respectively: district's temperature: 200 ℃; Two districts: 210 ℃; Three districts: 220 ℃; Four districts: 230 ℃; Five districts: 230 ℃; Six districts: 230 ℃; Seven districts: 230 ℃; Eight districts: 220 ℃; Head: 220 ℃; The residence time 2~3min.Pressure is 15MPa.
Embodiment 3:
The ABS weight ratio is 35.8% (below be weight ratio), PET30%, toughener 15%, 1010/1680.2/0.2%, compatilizer 8%, toughner 10%, lubricant 0.8%.The material that mixes is joined in the hopper of twin screw extruder, through melt blending, extruding pelletization becomes matrix material.Wherein, screw rod is respectively distinguished the temperature setting and is respectively: district's temperature: 200 ℃; Two districts: 210 ℃; Three districts: 220 ℃; Four districts: 230 ℃; Five districts: 230 ℃; Six districts: 230 ℃; Seven districts: 230 ℃; Eight districts: 220 ℃; Head: 220 ℃; The residence time 2~3min.Pressure is 15MPa.
Embodiment 4:
The ABS weight ratio is 23.6% (below be weight ratio), PET40%, toughener 10%, 1010/1680.2/0.2%, compatilizer 10%, toughner 15%, lubricant 1.0%.The material that mixes is joined in the hopper of twin screw extruder, through melt blending, extruding pelletization becomes matrix material.Wherein, screw rod is respectively distinguished the temperature setting and is respectively: district's temperature: 200 ℃; Two districts: 210 ℃; Three districts: 220 ℃; Four districts: 230 ℃; Five districts: 230 ℃; Six districts: 230 ℃; Seven districts: 230 ℃; Eight districts: 220 ℃; Head: 220 ℃; The residence time 2~3min.Pressure is 15MPa.
Embodiment 5:
The ABS weight ratio is 26.1% (below be weight ratio), PET50%, toughener 5%, 1010/1680.2/0.2%, compatilizer 5%, toughner 8%, lubricant 0.5%.The material that mixes is joined in the hopper of twin screw extruder, through melt blending, extruding pelletization becomes matrix material.Wherein, screw rod is respectively distinguished the temperature setting and is respectively: district's temperature: 200 ℃; Two districts: 210 ℃; Three districts: 220 ℃; Four districts: 230 ℃; Five districts: 230 ℃; Six districts: 230 ℃; Seven districts: 230 ℃; Eight districts: 220 ℃; Head: 220 ℃; The residence time 2~3min.Pressure is 15MPa.
Embodiment 6:
The ABS weight ratio is 21.1% (below be weight ratio), PET60%, toughener 5%, 1010/1680.2/0.2%, compatilizer 5%, toughner 8%, lubricant 0.5%.The material that mixes is joined in the hopper of twin screw extruder, through melt blending, extruding pelletization becomes matrix material.Wherein, screw rod is respectively distinguished the temperature setting and is respectively: district's temperature: 200 ℃; Two districts: 210 ℃; Three districts: 220 ℃; Four districts: 230 ℃; Five districts: 230 ℃; Six districts: 230 ℃; Seven districts: 230 ℃; Eight districts: 220 ℃; Head: 220 ℃; The residence time 2~3min.Pressure is 15MPa.
Performance test:
Tensile strength is tested by the GB/T1040 standard.Specimen types is the I type, batten size (mm): 170 (length) * (20 ± 0.2) (end width) * (4 ± 0.2) (thickness), and draw speed is 50mm/min;
Flexural strength and modulus in flexure are tested by GB 9341/T standard.Specimen types is specimen size (mm): (80 ± 2) * (10 ± 0.2) * (4 ± 0.2), rate of bending are 20mm/min;
Notched Izod impact strength is tested by the GB/T1043 standard.Specimen types is the I type, specimen size (mm): (80 ± 2) * (10 ± 0.2) * (4 ± 0.2); The breach type is a category-A, and the breach residual thickness is 3.2mm.
Embodiment 1~6 prescription and material property see Table 1:
Table 1
Form Embodiment 1 Embodiment 2 Embodiment 3 Embodiment 4 Embodiment 5 Embodiment 6
ABS(%) 71.3 56.1 35.8 23.6 26.1 21.1
PET(%) 15 20 30 40 50 60
Toughener (%) 5 10 15 10 5 5
Compatilizer (%) 3 5 8 10 10 5
Toughner (%) 5 8 10 15 8 8
1010(%) 0.2 0.2 0.2 0.2 0.2 0.2
168(%) 0.2 0.2 0.2 0.2 0.2 0.2
Lubricant (%) 0.3 0.5 0.8 1.0 0.5 0.5
Notched Izod impact strength (KJ/m 2) 83.2 81.1 78.5 81.3 82.4 78.1
Tensile strength (MPa) 70.2 73.1 77.7 75.3 78.2 80.7
Elongation at break (%) 90 83 85 107 85 67
Flexural strength (MPa) 88.5 95 108.2 100.7 113.4 115.3
Modulus in flexure (MPa) 2670 2700 2882 3012 3115 3018
More than a kind of ABS/PET Alloy And Preparation Method provided by the present invention is described in detail, used specific case herein principle of the present invention and embodiment are set forth, the explanation of above embodiment just is used for helping to understand method of the present invention and core concept thereof; Simultaneously, for one of ordinary skill in the art, according to thought of the present invention, the part that all can change in specific embodiments and applications, in sum, this description should not be construed as limitation of the present invention.

Claims (10)

1, a kind of ABS/PET alloy is characterized in that, its composition is (%) by weight ratio:
Acrylonitrile-butadiene-styrene copolymer ABS 21-72%;
Polyethylene terephtalate 14-60%;
Compatilizer 3-10%;
Toughner 5-15%;
Oxidation inhibitor 0.4-0.6%;
Lubricant 0.3-1%.
2, ABS/PET alloy as claimed in claim 1 is characterized in that: also comprise toughener, its
Forming is (%): 5-15% by weight ratio.
3, ABS/PET alloy as claimed in claim 1 is characterized in that: described ABS is vinyl cyanide, divinyl, styrene copolymer, and its rubber content is 35%-70%.
4, ABS/PET alloy as claimed in claim 1 is characterized in that: described PET is a relative density 1.35~1.38,255~260 ℃ of fusing points, and melt viscosity is at the polyethylene terephthalate more than 0.9.
5, ABS/PET alloy as claimed in claim 1 is characterized in that: described compatilizer is the one or more combination thing in ABS-g-MAH, ABS-g-GMA, AS-g-MAH, SEBS-g-MAH, glycidyl methacrylate (GMA), methyl methacrylate (MMA)-glycidyl methacrylate (GMA)-propylene ethyl ester (EA) ter-polymers (MGE).
6, ABS/PET alloy as claimed in claim 1 is characterized in that: described toughner is the one or more combination thing in polymer elastomerics NBR, TPU, SEBS, EPDM, high glue powder or the MBS core-shell type anti-impact modifier.
7, ABS/PET alloy as claimed in claim 1 is characterized in that: described toughener is the one or more combination thing in organic rigid material MMA/St multipolymer, PMMA, MBS, PS, SAN or inorganic reinforcement glass fibre, carbon fiber, mica powder, kaolin, talcum powder, wollastonite, glass microballon, the whisker.
8, ABS/PET alloy as claimed in claim 1 is characterized in that: described oxidation inhibitor is the composite of four [3-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester primary antioxidants and tricresyl phosphite (2,4-di-t-butyl phenyl ester) auxiliary anti-oxidant.
9, ABS/PET alloy as claimed in claim 1 is characterized in that: described lubricant is the one or more combination thing in polysiloxane, calcium stearate, Zinic stearas, Magnesium Stearate, PE wax, PP wax, ABS wax, EVA wax, the ethylene bis stearamide.
10, a kind of preparation method of the alloy of ABS/PET according to claim 1 is characterized in that, comprises step:
A: take by weighing ABS and PET resin by weight ratio, mix;
B: take by weighing compatilizer and toughner by weight ratio, mix;
C: take by weighing other auxiliary agents such as oxidation inhibitor, lubricant by weight ratio, mix, the above-mentioned material that mixes is put in the mixing tank together continued all to mix up to evenly;
D: mixed raw materials is put into the loading hopper of twin screw extruder, through melt extruding granulation; Complete processing is as follows: twin screw extruder one district temperature 230-260 ℃, two district temperature 230-260 ℃, three district temperature 230-260 ℃, four district temperature 230-260 ℃, five district temperature 230-260 ℃, six district temperature 230-260 ℃, seven district temperature 230-260 ℃, eight district temperature 230-260 ℃, head 230-260 ℃, residence time 2-3min, pressure are 12-18MPa.
CNA2008102413272A 2008-12-17 2008-12-17 ABS//PET alloy and method for producing the same Pending CN101508818A (en)

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Cited By (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101857712A (en) * 2010-06-08 2010-10-13 从化市聚赛龙工程塑料有限公司 Halogen-free flame-retardant ABS/PET alloy and preparation method thereof
CN101870796A (en) * 2009-04-24 2010-10-27 上海金发科技发展有限公司 Acrylonitrile-butadiene-styrene terpolymer/polyethylene glycol terephthalate composite material and preparation method thereof
CN102050909A (en) * 2009-10-28 2011-05-11 东丽纤维研究所(中国)有限公司 Functionalized polymer and preparation method thereof
CN102181122A (en) * 2011-01-27 2011-09-14 上海锦湖日丽塑料有限公司 ABS (acrylonitrile-butadiene-styrene)/regenerated PET (polyethylene terephthalate) resin composition and preparation method thereof
CN102181121A (en) * 2011-01-27 2011-09-14 上海锦湖日丽塑料有限公司 High-fatigue-resistance ABS (Acrylonitrile Butadiene Styrene) resin composition and preparation method thereof
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CN102477207A (en) * 2010-11-29 2012-05-30 上海杰事杰新材料(集团)股份有限公司 Weather-resistant enhanced PEN (polyethylene naphthalate) short fiber/ABS (acrylonitrile butadiene styrene) composite material and preparation method thereof
CN102532788A (en) * 2010-12-28 2012-07-04 合肥杰事杰新材料股份有限公司 High gloss and high tenacity PET/ABS (Polyethylene Terephthalate/Acrylonitrile Butadiene Styrene) alloy resin and preparation method thereof
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CN106633603A (en) * 2016-12-25 2017-05-10 合肥会通新材料有限公司 ABS (Acrylonitrile Butadiene Styrene)/PET (Polyethylene Terephthalate) alloy material and preparation method thereof
CN106633598A (en) * 2016-12-15 2017-05-10 苏州博云塑业有限公司 Composition capable of improving mechanical property and flowing property of blending alloy ABS/PBT and preparation method
CN108070196A (en) * 2016-11-18 2018-05-25 合肥市和裕达塑业有限公司 A kind of anticorrosive, high-low temperature resistant ABS material and its preparation method and application
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Cited By (41)

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CN101870796A (en) * 2009-04-24 2010-10-27 上海金发科技发展有限公司 Acrylonitrile-butadiene-styrene terpolymer/polyethylene glycol terephthalate composite material and preparation method thereof
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CN101857712A (en) * 2010-06-08 2010-10-13 从化市聚赛龙工程塑料有限公司 Halogen-free flame-retardant ABS/PET alloy and preparation method thereof
CN102399409A (en) * 2010-09-16 2012-04-04 佛山市顺德区威林工程塑料有限公司 Carbon fiber reinforced ABS resin with unique fiber arrangement effect and manufacturing method thereof
CN102321327B (en) * 2010-09-30 2013-02-27 深圳市科聚新材料有限公司 Multi-grafted phenylethylene-ethylene-butylene copolymer and preparation method thereof
CN102321327A (en) * 2010-09-30 2012-01-18 深圳市科聚新材料有限公司 Multi-grafted phenylethylene-ethylene-butylene copolymer and preparation method thereof
CN102477207B (en) * 2010-11-29 2014-11-19 上海杰事杰新材料(集团)股份有限公司 Weather-resistant reinforced PEN (Polyethylene Naphthalate) chopped fiber/ABS (Acrylonitrile Butadiene Styrene) composite material and preparation method thereof
CN102477207A (en) * 2010-11-29 2012-05-30 上海杰事杰新材料(集团)股份有限公司 Weather-resistant enhanced PEN (polyethylene naphthalate) short fiber/ABS (acrylonitrile butadiene styrene) composite material and preparation method thereof
CN102532788A (en) * 2010-12-28 2012-07-04 合肥杰事杰新材料股份有限公司 High gloss and high tenacity PET/ABS (Polyethylene Terephthalate/Acrylonitrile Butadiene Styrene) alloy resin and preparation method thereof
CN102181122A (en) * 2011-01-27 2011-09-14 上海锦湖日丽塑料有限公司 ABS (acrylonitrile-butadiene-styrene)/regenerated PET (polyethylene terephthalate) resin composition and preparation method thereof
CN102181121A (en) * 2011-01-27 2011-09-14 上海锦湖日丽塑料有限公司 High-fatigue-resistance ABS (Acrylonitrile Butadiene Styrene) resin composition and preparation method thereof
CN102367286A (en) * 2011-06-27 2012-03-07 深圳市科聚新材料有限公司 ABS/PET compatilizer, its preparation method and ABS/PET alloy
CN102391437B (en) * 2011-10-09 2013-04-24 深圳市科聚新材料有限公司 Multi-grafted acrylonitrile-butadiene-styrene (ABS) copolymer and preparation method thereof
CN102391437A (en) * 2011-10-09 2012-03-28 深圳市科聚新材料有限公司 Multi-grafted acrylonitrile-butadiene-styrene (ABS) copolymer and preparation method thereof
CN102382432A (en) * 2011-11-25 2012-03-21 深圳市科聚新材料有限公司 High-impact polyethylene terephthalate (PET) composite material and preparation method thereof
CN102604318B (en) * 2012-03-27 2014-06-25 成都硕屋科技有限公司 Short-fiber modified ABS/PET (Acrylonitrile Butadiene Styrene/Polyethylene Terephthalate) resin alloy material and preparation method thereof
CN102604318A (en) * 2012-03-27 2012-07-25 成都硕屋科技有限公司 Short-fiber modified ABS/PET (Acrylonitrile Butadiene Styrene/Polyethylene Terephthalate) resin alloy material and preparation method thereof
CN102643506A (en) * 2012-05-04 2012-08-22 金发科技股份有限公司 Flame retardant permanent anti-static acrylonitrile butadiene styrene (ABS) /polyethylene terephthalate (PET) alloy and preparation method thereof
CN102675810B (en) * 2012-05-11 2014-05-07 江苏安格特科技发展有限公司 High-impact extrusion grade ABS (Acrylonitrile Butadiene Styrene) nanocomposite material
CN102675810A (en) * 2012-05-11 2012-09-19 江苏安格特科技发展有限公司 High-impact extrusion grade ABS (Acrylonitrile Butadiene Styrene) nanocomposite material
CN102863732A (en) * 2012-09-12 2013-01-09 江苏安格特科技发展有限公司 Low-temperature impact-resistant extrusion-grade acrylonitrile butadiene styrene (ABS) alloy material
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CN103772882A (en) * 2012-10-25 2014-05-07 合肥杰事杰新材料股份有限公司 Weather-proof flame retardant ABS/PET material for extrusion process and preparation method of ABS/PET material
CN102977561A (en) * 2012-12-13 2013-03-20 东莞市信诺橡塑工业有限公司 Toughened polytrimethylene terephthalate alloy and preparation method thereof
CN102977561B (en) * 2012-12-13 2014-08-13 东莞市信诺橡塑工业有限公司 Toughened polytrimethylene terephthalate alloy and preparation method thereof
CN103146106A (en) * 2013-03-27 2013-06-12 苏州双象光学材料有限公司 Formula of polymer composite material and preparation method thereof
CN103289299A (en) * 2013-06-24 2013-09-11 苏州新区佳合塑胶有限公司 ABS/PET composite antibacterial material and preparation method thereof
CN103289299B (en) * 2013-06-24 2015-11-25 苏州新区佳合塑胶有限公司 A kind of ABS/PET composite antibacterial material and preparation method
CN103524993A (en) * 2013-09-17 2014-01-22 安徽科聚新材料有限公司 Super-tough acrylonitrile-butadiene-styrene (ABS) and polyethylene terephthalate (PET) alloy material and preparation method thereof
CN104072936A (en) * 2013-12-24 2014-10-01 惠州新大都合成材料科技有限公司 Acrylonitrile-butadiene-styrene resin mixture and preparation method thereof
CN104974463A (en) * 2015-07-31 2015-10-14 重庆友强高分子材料有限公司 High-glossiness heat-resistant ABS/PET (acrylonitrile-butadiene-styrene/polyethylene terephthalate) bottle chip composite material and preparation method thereof
CN105157196A (en) * 2015-08-21 2015-12-16 滁州晨润工贸有限公司 Method for manufacturing low-temperature-resisting air conditioner panel
CN105199303B (en) * 2015-09-16 2017-10-24 广东天保新材料有限责任公司 A kind of HI high impact, the modification regeneration ABS material of resistance to greasy dirt and preparation method thereof
CN105199303A (en) * 2015-09-16 2015-12-30 广东天保新材料有限责任公司 High-impact greasy-dirt-resistant modified regenerated ABS material and preparation method thereof
CN108070196A (en) * 2016-11-18 2018-05-25 合肥市和裕达塑业有限公司 A kind of anticorrosive, high-low temperature resistant ABS material and its preparation method and application
CN106633598A (en) * 2016-12-15 2017-05-10 苏州博云塑业有限公司 Composition capable of improving mechanical property and flowing property of blending alloy ABS/PBT and preparation method
CN106633603A (en) * 2016-12-25 2017-05-10 合肥会通新材料有限公司 ABS (Acrylonitrile Butadiene Styrene)/PET (Polyethylene Terephthalate) alloy material and preparation method thereof
CN110079045A (en) * 2019-03-26 2019-08-02 星威国际家居股份有限公司 Highlight antiflaming heat-proof ABS alloy modification material
WO2020192108A1 (en) * 2019-03-26 2020-10-01 星威国际家居股份有限公司 High-light flame-retardant heat-resistant abs alloy modified material
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