CN102746469A - 丙烯酸丁酯接枝乙烯-辛烯嵌段共聚物颗粒料的制备方法 - Google Patents
丙烯酸丁酯接枝乙烯-辛烯嵌段共聚物颗粒料的制备方法 Download PDFInfo
- Publication number
- CN102746469A CN102746469A CN201210268066XA CN201210268066A CN102746469A CN 102746469 A CN102746469 A CN 102746469A CN 201210268066X A CN201210268066X A CN 201210268066XA CN 201210268066 A CN201210268066 A CN 201210268066A CN 102746469 A CN102746469 A CN 102746469A
- Authority
- CN
- China
- Prior art keywords
- obc
- acrylic acid
- block copolymer
- preparation
- octene block
- 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
Links
- 238000002360 preparation method Methods 0.000 title claims description 20
- 239000002245 particle Substances 0.000 title claims 2
- -1 ethylene-octylene Chemical group 0.000 title description 10
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 title 1
- 229920000642 polymer Polymers 0.000 title 1
- 239000000463 material Substances 0.000 claims abstract description 7
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims abstract 13
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims abstract 13
- 229920001400 block copolymer Polymers 0.000 claims abstract 13
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 claims abstract 3
- JKIJEFPNVSHHEI-UHFFFAOYSA-N Phenol, 2,4-bis(1,1-dimethylethyl)-, phosphite (3:1) Chemical compound CC(C)(C)C1=CC(C(C)(C)C)=CC=C1OP(OC=1C(=CC(=CC=1)C(C)(C)C)C(C)(C)C)OC1=CC=C(C(C)(C)C)C=C1C(C)(C)C JKIJEFPNVSHHEI-UHFFFAOYSA-N 0.000 claims abstract 3
- 235000019400 benzoyl peroxide Nutrition 0.000 claims abstract 3
- 239000000203 mixture Substances 0.000 claims description 13
- 239000008188 pellet Substances 0.000 claims 1
- 239000000956 alloy Substances 0.000 abstract description 19
- 238000000034 method Methods 0.000 abstract description 10
- 238000006243 chemical reaction Methods 0.000 abstract description 5
- 238000002844 melting Methods 0.000 abstract description 5
- 230000008018 melting Effects 0.000 abstract description 5
- 238000005453 pelletization Methods 0.000 abstract description 5
- 238000002156 mixing Methods 0.000 abstract 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 abstract 1
- 239000005977 Ethylene Substances 0.000 abstract 1
- 238000001125 extrusion Methods 0.000 abstract 1
- 238000003756 stirring Methods 0.000 abstract 1
- 229920001707 polybutylene terephthalate Polymers 0.000 description 48
- 229920001577 copolymer Polymers 0.000 description 15
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 10
- 229910000600 Ba alloy Inorganic materials 0.000 description 9
- 150000001875 compounds Chemical class 0.000 description 8
- 239000011236 particulate material Substances 0.000 description 7
- 238000012360 testing method Methods 0.000 description 6
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical compound C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 description 5
- BGYHLZZASRKEJE-UHFFFAOYSA-N [3-[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxy]-2,2-bis[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxymethyl]propyl] 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(CCC(=O)OCC(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)=C1 BGYHLZZASRKEJE-UHFFFAOYSA-N 0.000 description 5
- 239000000178 monomer Substances 0.000 description 5
- 235000019260 propionic acid Nutrition 0.000 description 5
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 5
- 230000035939 shock Effects 0.000 description 5
- 238000009835 boiling Methods 0.000 description 4
- 239000003999 initiator Substances 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 2
- 239000003112 inhibitor Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 230000002929 anti-fatigue Effects 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- WOLATMHLPFJRGC-UHFFFAOYSA-N furan-2,5-dione;styrene Chemical compound O=C1OC(=O)C=C1.C=CC1=CC=CC=C1 WOLATMHLPFJRGC-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229920006113 non-polar polymer Polymers 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion 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
- B29C48/04—Particle-shaped
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means 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
- B29C48/40—Means 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92704—Temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92876—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
- B29C2948/92895—Barrel or housing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92904—Die; Nozzle zone
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Graft Or Block Polymers (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
本发明涉及一种丙烯酸熔融接枝乙烯-辛烯嵌段共聚物的制备方法,该方法以93~96重量份乙烯-辛烯嵌段共聚物为基体材料,添加3.5~6.0重量份丙烯酸、0.2~0.4重量份过氧化二苯甲酰、0.3~0.6重量份三(2,4-二叔丁基苯基)亚磷酸酯,通过搅拌混合、密炼熔融接枝反应、双螺杆挤出切粒而成丙烯酸接枝乙烯-辛烯嵌段共聚物(OBC-g-AA)。采用本方法制备的OBC-g-AA,接枝率为1.25%-1.45%,用作PET与OBC共混合金材料相容剂,制备PET/OBC/OBC-g-AA合金材料,与纯PET相比,断裂伸长率提高了235%-273%,缺口冲击强度提高了65%-85%,抗冲击韧性大幅度提高。
Description
技术领域
本发明涉及乙烯-辛烯嵌段共聚物接枝物的制备方法,具体的说是一种丙烯酸丁酯熔融接枝乙烯-辛烯嵌段共聚物颗粒料的制备方法。
背景技术
聚对苯二甲酸丁二醇酯(PBT)是结晶型热塑性聚酯,具有高耐热、耐疲劳、自润滑、低摩擦系数、力学强度高、耐候性好等优点,主要用于汽车部件、电子器件、家用电器壳体等领域。其缺点是缺口冲击强度低,成型收缩率大,制约了其广泛应用 。
乙烯-辛烯嵌段共聚物(OBC)是美国Dow化学公司近年来开发生产的烯烃弹性体,OBC分子链中 “硬”“ 软”段交替排列,与乙烯-辛烯共聚物相比,其耐热温度高、耐磨损性能和柔韧性能好、综合性能明显优于其他聚烯烃类弹性体,应用前景较为广阔。由于OBC是非极性聚合物,与含极性基团的聚对苯二甲酸丁二醇酯(PBT)直接共混,相容性差,制成的合金材料力学强度下降。因此,对OBC进行熔融接枝改性,在OBC中引入极性基团,可改善其与PBT的相容性,提高OBC与PBT的界面粘结力,制备出性能优异的工程塑料合金材料,拓展OBC的应用领域。
近年来,采用熔融接枝方法,对聚烯烃进行改性已有较多报道,如熔融法制备POE-g-GMA马来酸酐-苯乙烯熔融接枝聚丙烯、熔融接枝法制备POE-g-AA、熔融接枝法制备LLDPE-g-GMA、GMA/St双组分单体熔融接枝聚丙烯、双单体MMA/St熔融接枝POE等。检索大量的专利文献和公开发表的研究论文,尚未见采用乙烯-辛烯嵌段共聚物(OBC)为基体材料,丙烯酸丁酯(BA)为接枝单体,过氧化二异丙苯(DCP)为引发剂,四[β-(3, 5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯为抗氧剂,采用熔融接枝法制备丙烯酸丁酯接枝乙烯-辛烯嵌段共聚物的报道。
发明内容
为了克服现有OBC与聚对苯二甲酸丁二醇酯(PBT)直接共混相容性差,制成的合金材料力学强度下降等缺陷,本发明提供了一种丙烯酸丁酯熔融接枝乙烯-辛烯嵌段共聚物的制备方法。本方法以乙烯-辛烯嵌段共聚物(OBC)为基体材料,丙烯酸丁酯(BA)为接枝单体,过氧化二异丙苯(DCP)为引发剂,四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯(抗氧剂1010)为抗氧剂,采用双螺杆挤出熔融接枝法制备丙烯酸丁酯接枝乙烯-辛烯嵌段共聚物(OBC-g-BA)颗粒料。
采用本方法制备的OBC-g-BA,接枝率为1.57%-1.85% ,用作PBT与OBC共混合金材料相容剂,制备PBT /OBC/ OBC-g-BA合金材料,与纯PBT相比,其断裂伸长率提高了75%-97%,缺口冲击强度提高了60%-85%,抗冲击性能较大幅度提高。
为了实现本发明目的所采用的以下技术方案:
配方
乙烯-辛烯嵌段共聚物(OBC)91.5~95.5重量份,丙烯酸丁酯(BA)4.0~7.5重量份, 过氧化二异丙苯(DCP)0.2~0.5重量份,四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯(抗氧剂1010)0.3~0.5重量份。
制备方法
将乙烯-辛烯嵌段共聚物、丙烯酸丁酯、过氧化二异丙苯、四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯按配方比例计量后,置于搅拌机中,控制搅拌机转速60r/min,温度25±1℃,搅拌混合5min成混合料;将混合料置于反应型双螺杆挤出机中进行熔融接枝反应,控制反应型双螺杆挤出机料筒温度为Ⅰ区140℃~145℃、Ⅱ区148℃~153℃、Ⅲ区155℃~158℃、Ⅳ区158℃~161℃、Ⅴ区161℃~164℃、Ⅵ区161℃~164℃、Ⅶ区161℃~164℃、Ⅷ区157℃~160℃,模头温度为155℃~157℃;控制反应型双螺杆挤出机螺杆转速为60~100r/min挤出切粒成丙烯酸丁酯接枝乙烯-辛烯嵌段共聚物(OBC-g-BA)颗粒料。
本发明所述的乙烯-辛烯嵌段共聚物(OBC),其密度为 0.887g/cm3、熔体质量流动速率为5.0g/10min、拉伸强度为17MPa、断裂伸长率为1300%。
本发明所述的丙烯酸丁酯(BA),其纯度为质量百分数99.2%、沸点为145℃。
本发明的有益效果是:①采用丙烯酸丁酯(BA)为接枝单体,过氧化二异丙苯(DCP)为引发剂,对乙烯-辛烯嵌段共聚物(OBC)进行熔融接枝改性,制备了OBC-g- BA;②添加四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯,提高了OBC-g-BA制备过程的抗氧化性能和PBT/OBC/ OBC-g-BA合金材料热加工性能;③本方法制备的OBC-g-BA,接枝率为1.55%-1.87% ,用作PBT与OBC共混合金材料相容剂,制备PBT/OBC/ OBC-g-BA合金材料,与纯PBT相比,其断裂伸长率提高了75%-97%,缺口冲击强度提高了60%-85%,抗冲击性能较大幅度提高。
具体实施方式
实施例1:
将密度为 0.887g/cm3、熔体质量流动速率为5.0g/10min、拉伸强度为17MPa、断裂伸长率为1300%的OBC 91.5㎏,纯度为质量百分数99.2%、沸点为145℃的BA 4.0㎏, DCP 0.2㎏,抗氧剂1010 0.3㎏ 置于搅拌机中,控制搅拌机转速60r/min,温度25℃,搅拌混合5min成混合料;将混合料置于反应型双螺杆挤出机中进行熔融接枝反应,控制反应型双螺杆挤出机料筒温度为Ⅰ区140℃、Ⅱ区148℃、Ⅲ区155℃、Ⅳ区161℃、Ⅴ区161℃、Ⅵ区161℃、Ⅶ区161℃、Ⅷ区157℃,模头温度为155℃,控制反应型双螺杆挤出机螺杆转速为60r/min挤出切粒成OBC-g-BA颗粒料。
本实施例制成的OBC-g-BA,接枝率为1.58%,用作PBT与OBC共混合金材料相容剂,制备PBT/OBC/ OBC-g-BA合金材料,按照GB/T1040.3-2006标准测试拉伸强度和断裂伸长率,按照GB/T1043.1-2008标准测试缺口冲击强度,其性能见表1,含2% OBC-g-BA、13% OBC的 PBT/OBC/ OBC-g-BA合金材料,与纯PBT相比,其断裂伸长率提高了77.71%,缺口冲击强度提高了64.95%,拉伸强度降低6.80%,抗冲击性能较大幅度提高;与PBT/OBC相比,其断裂伸长率、缺口冲击强度、拉伸强度均明显提高。
表1 PBT、PBT /OBC及PBT/OBC/ OBC-g-BA力学性能
组成和比例(重量比) | 断裂伸长率(%) | 缺口冲击强度(J/m) | 拉伸强度(MPa) |
PBT 100 | 11.17 | 15.75 | 57.48 |
PBT/OBC 87/13 | 13.46 | 13.84 | 46.65 |
PBT/OBC/OBC-gBA 85/13/2 | 19.85 | 25.98 | 53.57 |
实施例2:
将密度为 0.887g/cm3、熔体质量流动速率为5.0g/10min、拉伸强度为17MPa、断裂伸长率为1300%的OBC 95.5㎏,纯度为质量百分数99.2%、沸点为145℃的BA 7.5㎏, DCP 0.5㎏,抗氧剂1010 0.5㎏置于搅拌机中,控制搅拌机转速60r/min,温度26℃,搅拌混合5min成混合料;将混合料置于反应型双螺杆挤出机中进行熔融接枝反应,控制反应型双螺杆挤出机料筒温度为Ⅰ区145℃、Ⅱ区153℃、Ⅲ区158℃、Ⅳ区160℃、Ⅴ区164℃、Ⅵ区164℃、Ⅶ区164℃、Ⅷ区160℃,模头温度为157℃;控制反应型双螺杆挤出机螺杆转速为100r/min挤出切粒成OBC-g-BA颗粒料。
实施例2制成的OBC-g-BA,接枝率为1.73%,用作PBT与OBC共混合金材料相容剂,制备PBT/OBC/ OBC-g-BA合金材料,按照GB/T1040.3-2006标准测试拉伸强度和断裂伸长率,按照GB/T1043.1-2008标准测试缺口冲击强度,其性能见表2,含2% OBC-g-BA、13% OBC的 PBT/OBC/ OBC-g-BA合金材料,与纯PBT相比,其断裂伸长率提高了87.47%,缺口冲击强度提高了76.38%,拉伸强度降低6.19%,抗冲击性能较大幅度提高;与PBT/OBC相比,其断裂伸长率、缺口冲击强度、拉伸强度均明显提高。
表2 PBT、PBT /OBC及PBT/OBC/ OBC-g-BA力学性能
组成和比例(重量比) | 断裂伸长率(%) | 缺口冲击强度(J/m) | 拉伸强度(MPa) |
PBT 100 | 11.17 | 15.75 | 57.48 |
PBT/OBC 87/13 | 13.46 | 13.84 | 46.65 |
PBT/OBC/OBC-gBA 85/13/2 | 20.94 | 27.78 | 53.92 |
实施例3:
将密度为 0.887g/cm3、熔体质量流动速率为5.0g/10min、拉伸强度为17MPa、断裂伸长率为1300%的OBC 93.5㎏,纯度为质量百分数99.2%、沸点为145℃的BA 6.0㎏, DCP 0.35㎏,抗氧剂1010 0.35㎏置于搅拌机中,控制搅拌机转速60r/min,温度24℃,搅拌混合5min成混合料;将混合料置于反应型双螺杆挤出机中进行熔融接枝反应,控制反应型双螺杆挤出机料筒温度为Ⅰ区143℃、Ⅱ区150℃、Ⅲ区157℃、Ⅳ区159℃、Ⅴ区162℃、Ⅵ区162℃、Ⅶ区162℃、Ⅷ区158℃,模头温度为156℃;控制反应型双螺杆挤出机螺杆转速为80r/min挤出切粒成OBC-g-BA颗粒料。
表3 PBT、PBT /OBC及PBT/OBC/ OBC-g-BA力学性能
组成和比例(重量比) | 断裂伸长率(%) | 缺口冲击强度(J/m) | 拉伸强度(MPa) |
PBT 100 | 11.17 | 15.75 | 57.48 |
PBT/OBC 87/13 | 13.46 | 13.84 | 46.65 |
PBT/OBC/OBC-gBA 85/13/2 | 21.87 | 29.02 | 54.32 |
实施例3制成的OBC-g-BA,接枝率为1.85%,用作PBT与OBC共混合金材料相容剂,制备PBT/OBC/ OBC-g-BA合金材料,按照GB/T1040.3-2006标准测试拉伸强度和断裂伸长率,按照GB/T1043.1-2008标准测试缺口冲击强度,其性能见表3,含2% OBC-g-BA、13% OBC的 PBT/OBC/ OBC-g-BA合金材料,与纯PBT相比,其断裂伸长率提高了95.80%,缺口冲击强度提高了84.25%,拉伸强度降低5.50%,抗冲击性能较大幅度提高;与PBT/OBC相比,其断裂伸长率、缺口冲击强度、拉伸强度均明显提高。
Claims (6)
1.一种丙烯酸熔融接枝乙烯-辛烯嵌段共聚物的制备方法,其特征是:
配方
乙烯-辛烯嵌段共聚物93~96重量份,丙烯酸3.5~6.0重量份, 过氧化二苯甲酰0.2~0.4重量份,三(2, 4-二叔丁基苯基)亚磷酸酯0.3~0.6重量份;
制备方法
1)将乙烯-辛烯嵌段共聚物、丙烯酸、过氧化二苯甲酰置于搅拌机中搅拌混合3min成混合料;
2)将混合料置于密炼机中熔融接枝反应8min后,加入三(2, 4-二叔丁基苯基)亚磷酸酯,继续密炼4min成胶体料;
3)将胶体料置于异向双螺杆挤出机料斗中,控制异向双螺杆挤出机料筒温度和模头温度,挤出切粒成丙烯酸接枝乙烯-辛烯嵌段共聚物颗粒料。
2.根据权利要求1所述的丙烯酸熔融接枝乙烯-辛烯嵌段共聚物的制备方法,其特征是所述的乙烯-辛烯嵌段共聚物,其密度为 0.877g/cm3,熔体质量流动速率为1.0g/10min,拉伸强度为13MPa,断裂伸长率为1300%。
3.根据权利要求1所述的丙烯酸熔融接枝乙烯-辛烯嵌段共聚物的制备方法,其特征是所述的丙烯酸,其质量百分含量为99.5%、熔点为14℃、相对密度为1.05。
4.根据权利要求1所述的丙烯酸熔融接枝乙烯-辛烯嵌段共聚物的制备方法,其特征是所述的搅拌机转速为120r/min,温度为30±1℃。
5.根据权利要求1所述的丙烯酸熔融接枝乙烯-辛烯嵌段共聚物的制备方法,其特征是所述的密炼机转速为70r/min,温度为166±1℃。
6.根据权利要求1所述的丙烯酸熔融接枝乙烯-辛烯嵌段共聚物的制备方法,其特征是所述的异向双螺杆挤出机料筒温度为Ⅰ区143~148℃,Ⅱ区150~155℃,Ⅲ区157~160℃,Ⅳ区160~163℃,Ⅴ区158~161℃,异向双螺杆挤出机模头温度为155~158℃。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210268066XA CN102746469A (zh) | 2012-07-31 | 2012-07-31 | 丙烯酸丁酯接枝乙烯-辛烯嵌段共聚物颗粒料的制备方法 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210268066XA CN102746469A (zh) | 2012-07-31 | 2012-07-31 | 丙烯酸丁酯接枝乙烯-辛烯嵌段共聚物颗粒料的制备方法 |
Publications (1)
Publication Number | Publication Date |
---|---|
CN102746469A true CN102746469A (zh) | 2012-10-24 |
Family
ID=47026993
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201210268066XA Pending CN102746469A (zh) | 2012-07-31 | 2012-07-31 | 丙烯酸丁酯接枝乙烯-辛烯嵌段共聚物颗粒料的制备方法 |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102746469A (zh) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102746468A (zh) * | 2012-07-31 | 2012-10-24 | 福建师范大学 | 一种丙烯酸熔融接枝乙烯-辛烯嵌段共聚物的制备方法 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1122144A (zh) * | 1993-04-28 | 1996-05-08 | 陶氏化学公司 | 接枝改性的基本线型乙烯聚合物与其它热塑性聚合物的共混物 |
EP0792894A2 (de) * | 1996-02-28 | 1997-09-03 | PCD-Polymere Gesellschaft m.b.H. | Kontinuierliches Verfahren zur Modifizierung von Polyolefinen in der festen Phase |
CN101747600A (zh) * | 2009-12-15 | 2010-06-23 | 华南理工大学 | 一种聚对苯二甲酸乙二醇酯共混物的制备方法 |
CN102391432A (zh) * | 2011-09-07 | 2012-03-28 | 上海日之升新技术发展有限公司 | 高流动性乙烯-α-辛烯接枝共聚物及制备方法 |
-
2012
- 2012-07-31 CN CN201210268066XA patent/CN102746469A/zh active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1122144A (zh) * | 1993-04-28 | 1996-05-08 | 陶氏化学公司 | 接枝改性的基本线型乙烯聚合物与其它热塑性聚合物的共混物 |
EP0792894A2 (de) * | 1996-02-28 | 1997-09-03 | PCD-Polymere Gesellschaft m.b.H. | Kontinuierliches Verfahren zur Modifizierung von Polyolefinen in der festen Phase |
CN101747600A (zh) * | 2009-12-15 | 2010-06-23 | 华南理工大学 | 一种聚对苯二甲酸乙二醇酯共混物的制备方法 |
CN102391432A (zh) * | 2011-09-07 | 2012-03-28 | 上海日之升新技术发展有限公司 | 高流动性乙烯-α-辛烯接枝共聚物及制备方法 |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102746468A (zh) * | 2012-07-31 | 2012-10-24 | 福建师范大学 | 一种丙烯酸熔融接枝乙烯-辛烯嵌段共聚物的制备方法 |
CN102746468B (zh) * | 2012-07-31 | 2014-05-07 | 福建师范大学 | 一种丙烯酸熔融接枝乙烯-辛烯嵌段共聚物的制备方法 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103571039B (zh) | 高熔指聚丙烯组合物及其制备方法 | |
CN101914252B (zh) | 低成本环保型可注塑成型的高耐热高抗冲硬质聚氯乙烯复合物及制备方法 | |
CN101747600B (zh) | 一种聚对苯二甲酸乙二醇酯共混物的制备方法 | |
CN102391432B (zh) | 高流动性乙烯-α-辛烯接枝共聚物及制备方法 | |
CN101709125B (zh) | 基于界面增容的聚苯乙烯/聚烯烃纳米复合材料及制备方法 | |
CN101921491A (zh) | 一种木塑复合材料 | |
CN101245125B (zh) | 高流动乙烯-醋酸乙烯酯共聚物接枝马来酸酐产品及其制备方法和应用 | |
CN103436012B (zh) | 一种超高分子量聚乙烯改性尼龙66及其制备方法 | |
CN109181281B (zh) | 一种用于尼龙增韧的合金增韧剂 | |
CN105037951A (zh) | 一种无机刚性粒子三元共混增韧体系的ppr管材及其制备方法 | |
CN104592622B (zh) | 一种提高熔接线力学性能的聚丙烯复合材料及其制备方法 | |
CN102321217B (zh) | 一种熔融聚丙烯接枝马来酸酐的共聚物及其制备方法 | |
CN103265755A (zh) | 一种多元复合改性聚丙烯塑料及制备方法 | |
CN101870807B (zh) | 一种聚碳酸酯/聚乙烯合金导电复合材料及其制备方法 | |
CN104045898A (zh) | 一种超高分子量聚乙烯材料及其制备方法 | |
CN103756346A (zh) | 诱导β-结晶增韧的聚丙烯木塑复合材料及其制备方法 | |
CN110144092A (zh) | 一种环保硬质pvc改性材料及其制备方法 | |
CN109517119A (zh) | 一种增强pc/abs合金韧性和组份相容性的复合型材料及其制备方法 | |
CN106928624B (zh) | 一种基于挤出机工艺的核壳尼龙增韧剂及制备方法和应用 | |
JP2011190442A (ja) | ポリエチレン系樹脂組成物 | |
CN102746469A (zh) | 丙烯酸丁酯接枝乙烯-辛烯嵌段共聚物颗粒料的制备方法 | |
CN102746468B (zh) | 一种丙烯酸熔融接枝乙烯-辛烯嵌段共聚物的制备方法 | |
CN102295797A (zh) | 一种无卤阻燃聚烯烃材料及其制备方法和应用 | |
CN1328312C (zh) | 一种植物纤维聚丙烯复合材料及制备方法 | |
JP2009114402A (ja) | 射出成形用ポリエステル樹脂組成物及びその成形品 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20121024 |