CN102634073A - Starch/polypropylene degradable composite material and preparation method thereof - Google Patents
Starch/polypropylene degradable composite material and preparation method thereof Download PDFInfo
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- CN102634073A CN102634073A CN2012101239345A CN201210123934A CN102634073A CN 102634073 A CN102634073 A CN 102634073A CN 2012101239345 A CN2012101239345 A CN 2012101239345A CN 201210123934 A CN201210123934 A CN 201210123934A CN 102634073 A CN102634073 A CN 102634073A
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- 229920002472 Starch Polymers 0.000 title claims abstract description 145
- 235000019698 starch Nutrition 0.000 title claims abstract description 143
- 239000008107 starch Substances 0.000 title claims abstract description 143
- 239000004743 Polypropylene Substances 0.000 title claims abstract description 129
- 229920001155 polypropylene Polymers 0.000 title claims abstract description 129
- 239000002131 composite material Substances 0.000 title claims abstract description 73
- 238000002360 preparation method Methods 0.000 title claims abstract description 22
- -1 polypropylene Polymers 0.000 claims abstract description 60
- 239000004014 plasticizer Substances 0.000 claims abstract description 33
- 235000015112 vegetable and seed oil Nutrition 0.000 claims abstract description 29
- 239000008158 vegetable oil Substances 0.000 claims abstract description 29
- 239000002994 raw material Substances 0.000 claims abstract description 22
- 239000000463 material Substances 0.000 claims description 40
- 238000002156 mixing Methods 0.000 claims description 35
- 239000003549 soybean oil Substances 0.000 claims description 34
- 235000012424 soybean oil Nutrition 0.000 claims description 34
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 27
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 27
- 229920005989 resin Polymers 0.000 claims description 25
- 239000011347 resin Substances 0.000 claims description 25
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims description 20
- 229920002261 Corn starch Polymers 0.000 claims description 19
- 239000008120 corn starch Substances 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 15
- 229920000881 Modified starch Polymers 0.000 claims description 9
- 229920000107 Acetylated distarch adipate Polymers 0.000 claims description 8
- 239000004368 Modified starch Substances 0.000 claims description 8
- 235000019426 modified starch Nutrition 0.000 claims description 8
- 229920001592 potato starch Polymers 0.000 claims description 6
- 229920006242 ethylene acrylic acid copolymer Polymers 0.000 claims description 5
- 244000017020 Ipomoea batatas Species 0.000 claims description 4
- 235000002678 Ipomoea batatas Nutrition 0.000 claims description 4
- 239000001245 distarch phosphate Substances 0.000 claims description 4
- 235000013804 distarch phosphate Nutrition 0.000 claims description 4
- 238000002844 melting Methods 0.000 claims description 4
- 230000008018 melting Effects 0.000 claims description 4
- 235000019483 Peanut oil Nutrition 0.000 claims description 3
- 239000000312 peanut oil Substances 0.000 claims description 3
- 229920003012 Hydroxypropyl distarch phosphate Polymers 0.000 claims description 2
- 240000003183 Manihot esculenta Species 0.000 claims description 2
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 claims description 2
- 240000002853 Nelumbo nucifera Species 0.000 claims description 2
- 235000006508 Nelumbo nucifera Nutrition 0.000 claims description 2
- 229910019142 PO4 Inorganic materials 0.000 claims description 2
- 235000003283 Pachira macrocarpa Nutrition 0.000 claims description 2
- 235000019482 Palm oil Nutrition 0.000 claims description 2
- 235000019496 Pine nut oil Nutrition 0.000 claims description 2
- 235000019486 Sunflower oil Nutrition 0.000 claims description 2
- 240000001085 Trapa natans Species 0.000 claims description 2
- 235000014364 Trapa natans Nutrition 0.000 claims description 2
- 240000004922 Vigna radiata Species 0.000 claims description 2
- 235000010721 Vigna radiata var radiata Nutrition 0.000 claims description 2
- 235000011469 Vigna radiata var sublobata Nutrition 0.000 claims description 2
- 239000004359 castor oil Substances 0.000 claims description 2
- 235000019438 castor oil Nutrition 0.000 claims description 2
- 239000003240 coconut oil Substances 0.000 claims description 2
- 235000019864 coconut oil Nutrition 0.000 claims description 2
- 235000012343 cottonseed oil Nutrition 0.000 claims description 2
- 239000002385 cottonseed oil Substances 0.000 claims description 2
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 claims description 2
- DVROLKBAWTYHHD-UHFFFAOYSA-N hydroxy propyl distarch phosphate Chemical compound OC1C(O)C(OC)OC(CO)C1OC(O)CCOC1C(OC2C(C(O)C(OC3C(C(OP(O)(=O)OC4C(C(O)C(OC)OC4CO)O)C(C)OC3CO)O)OC2COC2C(C(O)C(OC)C(CO)O2)O)O)OC(CO)C(OC)C1O DVROLKBAWTYHHD-UHFFFAOYSA-N 0.000 claims description 2
- 239000001310 hydroxy propyl distarch phosphate Substances 0.000 claims description 2
- 235000013825 hydroxy propyl distarch phosphate Nutrition 0.000 claims description 2
- 239000000944 linseed oil Substances 0.000 claims description 2
- 235000021388 linseed oil Nutrition 0.000 claims description 2
- 239000003921 oil Substances 0.000 claims description 2
- 235000019198 oils Nutrition 0.000 claims description 2
- 239000002540 palm oil Substances 0.000 claims description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 2
- 239000010452 phosphate Substances 0.000 claims description 2
- 239000010490 pine nut oil Substances 0.000 claims description 2
- 235000009165 saligot Nutrition 0.000 claims description 2
- 239000002600 sunflower oil Substances 0.000 claims description 2
- 239000002383 tung oil Substances 0.000 claims description 2
- 229940100445 wheat starch Drugs 0.000 claims description 2
- 240000008042 Zea mays Species 0.000 claims 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 claims 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 claims 1
- 235000005822 corn Nutrition 0.000 claims 1
- 229920003023 plastic Polymers 0.000 abstract description 16
- 239000004033 plastic Substances 0.000 abstract description 16
- 239000002362 mulch Substances 0.000 abstract description 4
- 239000005022 packaging material Substances 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000001746 injection moulding Methods 0.000 description 33
- 229940099112 cornstarch Drugs 0.000 description 17
- 239000003153 chemical reaction reagent Substances 0.000 description 14
- 239000000155 melt Substances 0.000 description 12
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 8
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 7
- 239000004698 Polyethylene Substances 0.000 description 5
- 229920000573 polyethylene Polymers 0.000 description 5
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 4
- 239000008187 granular material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 150000003384 small molecules Chemical class 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 239000004793 Polystyrene Substances 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 229920006238 degradable plastic Polymers 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 235000011187 glycerol Nutrition 0.000 description 3
- 229920001911 maleic anhydride grafted polypropylene Polymers 0.000 description 3
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 2
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 2
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 2
- 239000004202 carbamide Substances 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 238000009863 impact test Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 229920005615 natural polymer Polymers 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 239000004631 polybutylene succinate Substances 0.000 description 2
- 229920002961 polybutylene succinate Polymers 0.000 description 2
- 229920002223 polystyrene Polymers 0.000 description 2
- 239000000600 sorbitol Substances 0.000 description 2
- 239000012745 toughening agent Substances 0.000 description 2
- UPZFLZYXYGBAPL-UHFFFAOYSA-N 2-ethyl-2-methyl-1,3-dioxolane Chemical group CCC1(C)OCCO1 UPZFLZYXYGBAPL-UHFFFAOYSA-N 0.000 description 1
- 235000019759 Maize starch Nutrition 0.000 description 1
- 229920008262 Thermoplastic starch Polymers 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- OGBUMNBNEWYMNJ-UHFFFAOYSA-N batilol Chemical class CCCCCCCCCCCCCCCCCCOCC(O)CO OGBUMNBNEWYMNJ-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000007385 chemical modification Methods 0.000 description 1
- 235000005687 corn oil Nutrition 0.000 description 1
- 239000002285 corn oil Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229920001038 ethylene copolymer Polymers 0.000 description 1
- 229920000578 graft copolymer Polymers 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 239000008204 material by function Substances 0.000 description 1
- 239000012785 packaging film Substances 0.000 description 1
- 229920006280 packaging film Polymers 0.000 description 1
- 239000010816 packaging waste Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000004628 starch-based polymer Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 230000037303 wrinkles Effects 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
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Biological Depolymerization Polymers (AREA)
Abstract
本发明公开了一种淀粉/聚丙烯可降解复合材料,由重量百分含量50%~70%的淀粉、5%~15%的植物油增塑剂、15%~30%的聚丙烯或改性聚丙烯以及5%~30%的相容剂原料制成,通过相容剂改善淀粉与聚丙烯的相容性,通过植物油增塑剂对淀粉进行塑化,塑化的淀粉性能稳定,使得本发明淀粉/聚丙烯可降解复合材料的韧性和抗冲击性大大增强,同时性能稳定,适用于塑料包装材料、农用地膜及一次性餐具等领域。本发明还公开了一种淀粉/聚丙烯可降解复合材料的制备方法,制备简单,易于实施,易于操作和控制,制备成本低廉,易于工业化生产,具有广阔的应用前景。The invention discloses a starch/polypropylene degradable composite material, which consists of 50% to 70% of starch by weight, 5% to 15% of vegetable oil plasticizer, 15% to 30% of polypropylene or modified Made of polypropylene and 5% to 30% compatibilizer raw materials, the compatibility of starch and polypropylene is improved by the compatibilizer, and the starch is plasticized by the vegetable oil plasticizer, and the plasticized starch has stable performance, making this product The toughness and impact resistance of the invented starch/polypropylene degradable composite material are greatly enhanced, and the performance is stable at the same time, which is suitable for the fields of plastic packaging materials, agricultural mulch films and disposable tableware. The invention also discloses a preparation method of the starch/polypropylene degradable composite material, which is simple in preparation, easy in implementation, easy in operation and control, low in preparation cost, easy in industrialized production, and has broad application prospects.
Description
技术领域 technical field
本发明涉及塑料材料领域,具体涉及一种淀粉/聚丙烯可降解复合材料及其制备方法。The invention relates to the field of plastic materials, in particular to a starch/polypropylene degradable composite material and a preparation method thereof.
背景技术 Background technique
塑料工业迅速发展,其用途已经渗透到国民经济的各个领域,用途十分广泛。中国每年产生的废弃塑料约为500万吨,其中大多数废弃塑料为聚丙烯(PP)、聚乙烯(PE)和聚苯乙烯(PS)材料,这些材料不能够自然分解。因此,由PP材料、PE材料、PS材料制备的一次性塑料包装废弃物及其相应的农用薄膜和一次性餐具,如果被随意丢弃将会因其非降解性堆积在土地上,从而造成严重的白色污染,而且这种潜在的污染同时也会随着人们使用量的增加和时间的积累而加剧,目前我国白色污染严重,已经引起政府有关部门和社会的普遍关注,相关法律法规已经出台,尤其是在欧美市场,非可降解塑料的使用受到严格的限制。The plastic industry has developed rapidly, and its use has penetrated into various fields of the national economy, and its use is very extensive. China produces about 5 million tons of waste plastics every year, most of which are polypropylene (PP), polyethylene (PE) and polystyrene (PS) materials, which cannot be decomposed naturally. Therefore, if the disposable plastic packaging waste made of PP material, PE material and PS material and its corresponding agricultural film and disposable tableware are randomly discarded, they will be piled up on the land due to their non-degradability, causing serious damage. White pollution, and this potential pollution will also intensify with the increase of people's usage and the accumulation of time. At present, my country's white pollution is serious, which has attracted the general attention of relevant government departments and society. Relevant laws and regulations have been issued, especially Especially in the European and American markets, the use of non-degradable plastics is strictly restricted.
随着人们环保意识的不断提高,可生物降解的环境友好材料将会受到越来越多的关注,相关产业链和研发的投入已经形成,据报道2013年,美国的生物可降解需求量将会有26亿美元的市场空间,我国目前可降解塑料的需求量也是巨大的,据相关行业分析为300万吨,然而真正意义的可降解塑料如聚乳酸(PLA)、聚羟基脂肪酸酯(PHA)和聚丁二酸丁二醇酯(PBS)等价格非常昂贵而且性能较传统塑料如PP和PE有一定差距,导致其在近几年内发展的市场认可度不高,而淀粉基塑料(主要是淀粉对PP、PE和PS等等传统塑料的填充而得到的复合可降解塑料),由于其是在与传统的塑料填充共混的基础上发展起来的,不仅具有传统塑料的性能,而且价格便宜及具有生物可降解性,目前发展迅速且备受工业界和市场的认可。With the continuous improvement of people's awareness of environmental protection, biodegradable environmentally friendly materials will receive more and more attention, and related industrial chains and R & D investment have been formed. It is reported that in 2013, the demand for biodegradable materials in the United States will be There is a market space of 2.6 billion U.S. dollars. China's current demand for degradable plastics is also huge. According to the analysis of related industries, it is 3 million tons. ) and polybutylene succinate (PBS) are very expensive and have a certain gap in performance compared with traditional plastics such as PP and PE, resulting in low market recognition for their development in recent years, while starch-based plastics (mainly It is a composite degradable plastic obtained by filling traditional plastics such as PP, PE and PS with starch), because it is developed on the basis of blending with traditional plastic fillings, it not only has the performance of traditional plastics, but also has the price Inexpensive and biodegradable, it is developing rapidly and has been recognized by the industry and the market.
虽然淀粉是可以完全生物降解的天然高分子化合物,但由于其结构上与塑料存在明显差异,导致两者之间相容性差,因而在这方面也限制其进一步的应用。目前,改善塑料与淀粉相容性的方法主要包括对淀粉的物理改性和化学改性、对塑料的接枝改性以及添加合适的相容剂。相容剂的引入是目前使用最为广泛也是最有效的方法之一。最常使用的相容剂是乙烯-丙烯酸共聚物(EAA)、乙烯-醋酸乙烯的共聚物(EVA)、聚丙烯/缩水甲基丙烯酸甘油酯(PP/GMA)接枝物和淀粉/丙烯酸甲酯接枝共聚物等。湖南大学陈宪宏在引发剂存在下使用缩水甲基丙烯酸甘油酯(GMA)及GMA/淀粉接枝物作为聚丙烯/淀粉共混体系的相容剂,使用双螺杆挤出实现了淀粉的热塑化及淀粉与聚丙烯的共混增容,制备了性能优良的可生物降解的聚丙烯/淀粉共混材料(功能材料2009年第五期(40)卷)。但是该共混材料没有加入增韧剂,共混材料在双螺杆中很难塑化挤出且会非常脆。Although starch is a natural polymer compound that can be completely biodegraded, its further application is limited in this respect because of its obvious structural differences with plastics, resulting in poor compatibility between the two. At present, the methods to improve the compatibility of plastics and starch mainly include physical modification and chemical modification of starch, grafting modification of plastics and adding suitable compatibilizers. The introduction of compatibilizer is one of the most widely used and most effective methods at present. The most commonly used compatibilizers are ethylene-acrylic acid copolymer (EAA), ethylene-vinyl acetate copolymer (EVA), polypropylene/glycidyl methacrylate (PP/GMA) graft and starch/methacrylate Ester graft copolymers, etc. Chen Xianhong of Hunan University used glycidyl methacrylate (GMA) and GMA/starch grafts as compatibilizers for polypropylene/starch blends in the presence of initiators, and realized thermal plasticization of starch by twin-screw extrusion And the blending and compatibilization of starch and polypropylene, a biodegradable polypropylene/starch blend material with excellent performance was prepared (Functional Materials 2009 Fifth Issue (40) Volume). However, no toughening agent is added to the blended material, and the blended material is difficult to be plasticized and extruded in a twin-screw and will be very brittle.
另外在解决淀粉与聚丙烯相容性的同时还需要解决整个复合体系的韧性太差的缺陷,由于淀粉是刚性粒子,一般文献和专利报道均是对其实行塑化填充,采用的方法是加入多元醇、多元胺、醇胺或者单甘酸酯等小分子化合物与淀粉进行熔融共混来进行塑化。Yu等使用尿素和乙醇胺混合物作为制备热塑性淀粉的增塑剂,并在螺杆中进行熔融共混挤出。通过实验发现体系中15wt%尿素和15wt%乙醇胺复配使用后,淀粉塑化后相对于使用甘油塑化淀粉具有更好的热性能和机械性能(Carbohydrate Polymers 64(2006)267-273)。不过采用小分子对淀粉进行塑化,塑化的淀粉性能不稳定,小分子易析出造成塑化淀粉重结晶导致产品性能下降,且小分子塑化的淀粉不耐高温,产品易变黄。公开号为CN 101805463A的中国发明专利申请公开了一种淀粉填充可生物降解聚丙烯及其制备方法,该淀粉填充可生物降解聚丙烯由重量百分比30%~70%的淀粉、5%~15%的增塑剂、10%~50%的聚丙烯、0.5%~1%的分散剂、5%~8%的增韧剂以及0.5%~1%的光降解剂,虽然该淀粉填充可生物降解聚丙烯的力学性能较好,但是使用的增塑剂为山梨醇和甘油中的一种或两种的混合物,山梨醇和甘油均为小分子增塑剂,仍存在上述的问题。In addition, while solving the compatibility between starch and polypropylene, it is also necessary to solve the defect that the toughness of the entire composite system is too poor. Since starch is a rigid particle, general literature and patent reports are plasticized and filled. The method used is to add Small molecular compounds such as polyols, polyamines, alcohol amines or monoglycerides are melt blended with starch for plasticization. Yu et al. used a mixture of urea and ethanolamine as a plasticizer for the preparation of thermoplastic starch, and performed melt blending and extrusion in a screw. It is found through experiments that after the compound use of 15wt% urea and 15wt% ethanolamine in the system, the plasticized starch has better thermal and mechanical properties than glycerol plasticized starch (Carbohydrate Polymers 64 (2006) 267-273). However, small molecules are used to plasticize starch, and the performance of the plasticized starch is unstable. Small molecules are easy to precipitate, resulting in the recrystallization of the plasticized starch, resulting in a decrease in product performance, and the plasticized starch with small molecules is not resistant to high temperatures, and the product is easy to turn yellow. The Chinese invention patent application with the publication number CN 101805463A discloses a starch-filled biodegradable polypropylene and its preparation method. The starch-filled biodegradable polypropylene consists of 30% to 70% by weight of starch, 5% to 15% plasticizer, 10% to 50% polypropylene, 0.5% to 1% dispersant, 5% to 8% toughening agent and 0.5% to 1% photodegradant, although the starch filling is biodegradable The mechanical properties of polypropylene are good, but the plasticizer used is a mixture of one or two of sorbitol and glycerin. Both sorbitol and glycerin are small molecule plasticizers, and the above-mentioned problems still exist.
发明内容 Contents of the invention
本发明提供了一种淀粉/聚丙烯可降解复合材料,淀粉与聚丙烯在相容剂和植物油增塑剂的改善下,力学性能优异,抗褶皱能力强,植物油增塑剂不易析出。The invention provides a starch/polypropylene degradable composite material. Under the improvement of a compatibilizer and a vegetable oil plasticizer, the starch and polypropylene have excellent mechanical properties and strong wrinkle resistance, and the vegetable oil plasticizer is not easy to separate out.
一种淀粉/聚丙烯可降解复合材料,由以下重量百分含量的原料制成:A starch/polypropylene degradable composite material is made of the following raw materials in percentage by weight:
淀粉 50%~70%;Starch 50%~70%;
植物油增塑剂 5%~15%;Vegetable oil plasticizer 5% to 15%;
聚丙烯或改性聚丙烯 15%~30%;Polypropylene or modified polypropylene 15% to 30%;
相容剂 5%~30%。Compatibilizer 5% to 30%.
本发明通过相容剂改善淀粉与聚丙烯的相容性,通过植物油增塑剂对淀粉进行塑化,塑化的淀粉性能稳定,四种原料能够相互作用,使得本发明淀粉/聚丙烯可降解复合材料在淀粉含量比较高的前提下,体现出优异的力学性能。The present invention improves the compatibility of starch and polypropylene through a compatibilizer, plasticizes the starch through a vegetable oil plasticizer, and the performance of the plasticized starch is stable, and the four raw materials can interact, so that the starch/polypropylene of the present invention is degradable The composite material exhibits excellent mechanical properties under the premise of relatively high starch content.
作为优选,所述的淀粉/聚丙烯可降解复合材料,由以下重量百分含量的原料制成:As a preference, the starch/polypropylene degradable composite material is made of the following raw materials in percentage by weight:
淀粉 50%~60%;Starch 50%~60%;
植物油增塑剂 8%~12%;Vegetable oil plasticizer 8% to 12%;
聚丙烯或改性聚丙烯 15%~25%;Polypropylene or modified polypropylene 15% to 25%;
相容剂 15%~25%。Compatibilizer 15% to 25%.
所述的淀粉为天然淀粉、改性淀粉中的一种或两种。所述的天然淀粉为玉米淀粉、木薯淀粉、绿豆淀粉、甘薯淀粉、红薯淀粉、马铃薯淀粉、麦类淀粉、菱角淀粉、藕淀粉中的一种或两种以上。所述的改性淀粉为马来酸酐接枝改性淀粉、磷酸酯双淀粉、乙酰化二淀粉磷酸酯、乙酰化双淀粉己二酸酯、羟丙基二淀粉磷酸酯中的一种或两种以上。所述的马来酸酐接枝改性淀粉可具体选用马来酸酐接枝玉米淀粉。淀粉可以生物降解,天然淀粉是可以完全生物降解的天然高分子化合物,从淀粉/聚丙烯可降解复合材料的成本和可降解性上考虑,选用天然淀粉不但成本较低,而且可降解性好,从淀粉/聚丙烯可降解复合材料的力学性能上考虑,改性淀粉在保证复合材料一定的降解性能的同时更有利于淀粉/聚丙烯可降解复合材料力学性能的提高。The starch is one or both of natural starch and modified starch. The natural starch is one or more of corn starch, tapioca starch, mung bean starch, sweet potato starch, sweet potato starch, potato starch, wheat starch, water chestnut starch and lotus root starch. The modified starch is one or both of maleic anhydride grafted modified starch, phosphate distarch, acetylated distarch phosphate, acetylated distarch adipate, hydroxypropyl distarch phosphate more than one species. The maleic anhydride grafted modified starch can be specifically selected from maleic anhydride grafted cornstarch. Starch can be biodegradable. Natural starch is a natural polymer compound that can be completely biodegradable. Considering the cost and degradability of starch/polypropylene degradable composite materials, natural starch is not only low in cost, but also has good degradability. Considering the mechanical properties of starch/polypropylene degradable composites, modified starch is more conducive to the improvement of mechanical properties of starch/polypropylene degradable composites while ensuring a certain degradation performance of the composites.
本发明选用大分子植物油增塑剂对淀粉进行塑化,塑化的淀粉性能稳定,大分子植物油增塑剂不易析出,有利于淀粉/聚丙烯可降解复合材料力学性能的提高,特别是复合材料的韧性,并且大分子植物油增塑剂塑化的淀粉耐高温,产品不易变黄。所述的植物油增塑剂为大豆油、花生油、椰子油、棕榈油、亚麻油、棉籽油、玉米油、葵花籽油、松子油、桐油、蓖麻油中的一种或两种以上。进一步优选,所述的植物油增塑剂为大豆油,大豆油的重量百分含量为10%,采用重量百分含量为10%的大豆油不但能够制备出性能优异的淀粉/聚丙烯可降解复合材料,而且大豆油相对其他油成本较低,使得淀粉/聚丙烯可降解复合材料的生产成本大大降低。The present invention uses a macromolecular vegetable oil plasticizer to plasticize the starch, and the plasticized starch has stable properties, and the macromolecular vegetable oil plasticizer is not easy to separate out, which is beneficial to the improvement of the mechanical properties of the starch/polypropylene degradable composite material, especially the composite material. Toughness, and the starch plasticized by macromolecular vegetable oil plasticizer is resistant to high temperature, and the product is not easy to turn yellow. The vegetable oil plasticizer is one or more of soybean oil, peanut oil, coconut oil, palm oil, linseed oil, cottonseed oil, corn oil, sunflower oil, pine nut oil, tung oil, and castor oil. Further preferably, the vegetable oil plasticizer is soybean oil, and the weight percentage of soybean oil is 10%, and the use of soybean oil with a weight percentage of 10% can not only prepare a starch/polypropylene degradable composite Materials, and the cost of soybean oil is relatively low compared to other oils, which greatly reduces the production cost of starch/polypropylene degradable composite materials.
所述的聚丙烯可以采用市售产品,选用市售的通用牌号即可。改性聚丙烯也可选用市售的通用牌号,具体可采用马来酸酐接枝聚丙烯,经过马来酸酐改性的聚丙烯,与淀粉有较好相容性,改善了聚丙烯与淀粉的相容性。The polypropylene can be a commercially available product, and a commercially available general brand can be used. Modified polypropylene can also choose commercially available general grades. Specifically, maleic anhydride grafted polypropylene can be used. Polypropylene modified with maleic anhydride has better compatibility with starch, which improves the compatibility between polypropylene and starch. compatibility.
由于淀粉与聚丙烯两种在结构上存在明显差异导致两者之间相容性不佳,本发明通过相容剂改善淀粉与聚丙烯的相容性,所述的相容剂为乙烯-醋酸乙烯的共聚物(EVA)、乙烯-丙烯酸共聚物(EAA)中的一种或两种。进一步优选,所述的相容剂为乙烯-醋酸乙烯的共聚物,乙烯-醋酸乙烯的共聚物能够非常好地改善淀粉与聚丙烯的相容性。Due to the obvious difference in structure between starch and polypropylene, the compatibility between the two is not good. The present invention improves the compatibility of starch and polypropylene through a compatibilizer, and the compatibilizer is ethylene-acetic acid One or both of ethylene copolymer (EVA), ethylene-acrylic acid copolymer (EAA). Further preferably, the compatibilizer is an ethylene-vinyl acetate copolymer, which can very well improve the compatibility of starch and polypropylene.
本发明还提供了一种淀粉/聚丙烯可降解复合材料的制备方法,制备简单,易于实施,易于操作和控制。The invention also provides a preparation method of the starch/polypropylene degradable composite material, which is simple in preparation, easy in implementation, easy in operation and control.
所述的淀粉/聚丙烯可降解复合材料的制备方法,包括以下步骤:The preparation method of described starch/polypropylene degradable composite material comprises the following steps:
将淀粉、植物油增塑剂、聚丙烯和相容剂混合均匀,得到混合后的物料;或者将淀粉、植物油增塑剂、改性聚丙烯和相容剂混合均匀,得到混合后的物料;将混合后的物料加入至双螺杆挤出机中熔融共混后拉条、切粒,得到颗粒状混合树脂;颗粒状混合树脂经干燥处理后,得到淀粉/聚丙烯可降解复合材料。Mix starch, vegetable oil plasticizer, polypropylene and compatibilizer uniformly to obtain a mixed material; or mix starch, vegetable oil plasticizer, modified polypropylene and compatibilizer uniformly to obtain a mixed material; The mixed material is fed into a twin-screw extruder for melting and blending, and then drawn and pelletized to obtain a granular mixed resin; the granular mixed resin is dried to obtain a starch/polypropylene degradable composite material.
所述的双螺杆挤出机的螺杆长径比为35∶1~45∶1;所述的熔融共混的温度为160℃~180℃,植物油增塑剂对淀粉进行塑化,塑化的淀粉性能稳定,植物油增塑剂不易析出,原料可以在160℃~180℃较高温度下熔融挤塑。The screw length-to-diameter ratio of the twin-screw extruder is 35:1 to 45:1; the temperature of the melt blending is 160°C to 180°C, and the vegetable oil plasticizer plasticizes the starch, and the plasticized The performance of starch is stable, the vegetable oil plasticizer is not easy to precipitate, and the raw material can be melted and extruded at a relatively high temperature of 160°C to 180°C.
本发明淀粉/聚丙烯可降解复合材料适用于塑料包装材料、农用地膜及一次性餐具等领域,以淀粉/聚丙烯可降解复合材料为原材料,通过现有的加工技术生产塑料包装膜、农用地膜及一次性餐具。The starch/polypropylene degradable composite material of the present invention is suitable for fields such as plastic packaging materials, agricultural mulch films and disposable tableware, and the starch/polypropylene degradable composite material is used as a raw material to produce plastic packaging films and agricultural mulch films through existing processing technologies And disposable tableware.
与现有技术相比,本发明具有如下优点:Compared with prior art, the present invention has following advantage:
本发明淀粉/聚丙烯可降解复合材料中,淀粉含量较高,使得本发明淀粉/聚丙烯可降解复合材料具有较好的可降解性,采用廉价、易于获取的天然淀粉时,本发明淀粉/聚丙烯可降解复合材料仍具有较好的力学性能和耐高温性,同时可降解性更好。植物油增塑剂在特定的条件下能被微生物分解,可生物降解。因而,本发明淀粉/聚丙烯可降解复合材料中主要原料淀粉和植物油增塑剂均可降解,使得本发明淀粉/聚丙烯可降解复合材料具有较好的可降解性。In the starch/polypropylene degradable composite material of the present invention, the starch content is relatively high, so that the starch/polypropylene degradable composite material of the present invention has better degradability. Polypropylene degradable composites still have good mechanical properties and high temperature resistance, while better degradability. Vegetable oil plasticizers can be decomposed by microorganisms under certain conditions and are biodegradable. Therefore, both the main raw material starch and the vegetable oil plasticizer in the starch/polypropylene degradable composite material of the present invention can be degraded, so that the starch/polypropylene degradable composite material of the present invention has better degradability.
本发明淀粉/聚丙烯可降解复合材料,通过相容剂改善淀粉与聚丙烯的相容性,通过植物油增塑剂对淀粉进行塑化,塑化的淀粉性能稳定,植物油增塑剂不易析出,并且植物油增塑剂塑化的淀粉耐高温,使得原料可以在160℃~180℃较高温度下熔融挤塑,产品不易变黄,使得本发明淀粉/聚丙烯可降解复合材料的韧性和抗冲击性大大增强,同时性能稳定。本发明四种原料能够相互作用,使得本发明淀粉/聚丙烯可降解复合材料在淀粉含量比较高的前提下,体现出优异的力学性能和一定的耐高温性。The starch/polypropylene degradable composite material of the present invention improves the compatibility of starch and polypropylene through a compatibilizer, plasticizes the starch through a vegetable oil plasticizer, and the performance of the plasticized starch is stable, and the vegetable oil plasticizer is not easy to separate out, And the starch plasticized by the vegetable oil plasticizer is resistant to high temperature, so that the raw material can be melted and extruded at a relatively high temperature of 160°C to 180°C, and the product is not easy to turn yellow, which makes the starch/polypropylene degradable composite material of the present invention tough and impact resistant The performance is greatly enhanced, and the performance is stable at the same time. The four raw materials of the present invention can interact with each other, so that the starch/polypropylene degradable composite material of the present invention exhibits excellent mechanical properties and certain high temperature resistance under the premise of relatively high starch content.
本发明淀粉/聚丙烯复合材料不但可以适用于塑料包装材料、农用地膜及一次性餐具等领域,而且本发明淀粉/聚丙烯复合材料最后大部分能被土壤中的微生物分解和吸收,对环境污染小,具有良好的环境效益和社会价值。The starch/polypropylene composite material of the present invention can not only be applicable to fields such as plastic packaging material, agricultural mulch film and disposable tableware, and the final part of the starch/polypropylene composite material of the present invention can be decomposed and absorbed by microorganisms in the soil, which is harmful to environmental pollution. Small, with good environmental benefits and social value.
本发明淀粉/聚丙烯可降解复合材料的制备方法,制备简单,易于实施,易于操作和控制,制备成本低廉,产品性能优异和稳定,易于工业化生产并具有很好的经济效益,具有广阔的应用前景。The preparation method of the starch/polypropylene degradable composite material of the present invention has the advantages of simple preparation, easy implementation, easy operation and control, low preparation cost, excellent and stable product performance, easy industrial production, good economic benefits, and wide application prospect.
具体实施方式 Detailed ways
以下实施例进一步描述本发明,但本发明并不限于这些实施例。The following examples further describe the invention, but the invention is not limited to these examples.
制备例1Preparation Example 1
将60g的玉米淀粉(水分的重量百分含量为4.1%,诸城兴贸玉米开发有限公司)、2.6g的马来酸酐(国药试剂)、100mL的N,N-二甲基乙酰胺(DMAc,国药试剂)和20mL甲苯(国药试剂)加入至250mL三口烧瓶中搅拌均匀,于130℃下机械搅拌1h,静止除去上层溶剂,然后加入丙酮搅拌洗去未反应的马来酸酐,静止除去上层溶剂,再次加入丙酮静止除去上层溶剂,加入丙酮除去上层溶剂总共进行3次后,过滤,再用丙酮反复冲洗3次,把得到的改性玉米淀粉放入真空干燥箱于80℃下干燥12h,得到60g马来酸酐接枝玉米淀粉。With 60g of cornstarch (the weight percentage of moisture is 4.1%, Zhucheng Xingmao Corn Development Co., Ltd.), 2.6g of maleic anhydride (National Medicine Reagent), 100mL of N,N-dimethylacetamide (DMAc, Chinese medicine reagent) and 20mL toluene (Chinese medicine reagent) were added to a 250mL three-necked flask and stirred evenly, mechanically stirred at 130°C for 1h, and the upper solvent was removed at rest, then acetone was added to stir to wash away unreacted maleic anhydride, and the upper solvent was removed at rest, Add acetone again to remove the upper layer solvent, add acetone to remove the upper layer solvent for a total of 3 times, filter, then rinse with acetone repeatedly 3 times, put the obtained modified cornstarch in a vacuum drying oven at 80°C for 12 hours to obtain 60g Maize starch grafted with maleic anhydride.
实施例1Example 1
称取以下重量份的原料:Weigh the following raw materials in parts by weight:
制备例1制备的马来酸酐接枝玉米淀粉55重量份,大豆油(阿拉丁试剂)10重量份,马来酸酐接枝聚丙烯(通用级,宁波能之光新材料科技有限公司,型号为GPM200A)10重量份,乙烯-醋酸乙烯酯共聚物(韩国韩华,型号为1317型)25重量份。55 parts by weight of maleic anhydride grafted cornstarch prepared by Preparation Example 1, 10 parts by weight of soybean oil (Aladdin's reagent), maleic anhydride grafted polypropylene (general grade, Ningbo Nengzhiguang New Material Technology Co., Ltd., model is GPM200A) 10 parts by weight, ethylene-vinyl acetate copolymer (Korean Hanwha, model is 1317 type) 25 parts by weight.
将马来酸酐接枝玉米淀粉55重量份、大豆油10重量份、马来酸酐接枝聚丙烯10重量份和乙烯-醋酸乙烯酯共聚物25重量份混合均匀后,然后将混合后的物料加入至双螺杆挤出机中熔融共混(混合后的物料依次经过温度为160℃,170℃,170℃,170℃,175℃,170℃,170℃,160℃的熔融共混各区间)后拉条,切粒,得到颗粒状混合树脂;颗粒状混合树脂经除水干燥处理后,得到淀粉/聚丙烯可降解复合材料。选用的双螺杆挤出机的螺杆长径比为40∶1。Mix 55 parts by weight of cornstarch grafted with maleic anhydride, 10 parts by weight of soybean oil, 10 parts by weight of grafted polypropylene with maleic anhydride and 25 parts by weight of ethylene-vinyl acetate copolymer, and then add the mixed materials After melting and blending in a twin-screw extruder (the mixed materials pass through the melt blending sections at temperatures of 160°C, 170°C, 170°C, 170°C, 175°C, 170°C, 170°C, and 160°C) Stranding and cutting into pellets to obtain granular mixed resin; the granular mixed resin is dehydrated and dried to obtain a starch/polypropylene degradable composite material. The selected twin-screw extruder has a screw length-to-diameter ratio of 40:1.
将上述得到的淀粉/聚丙烯可降解复合材料加入至注塑机中注塑成型,得到制品样条。注塑区温度200℃,模板区温度45℃。Add the starch/polypropylene degradable composite material obtained above into an injection molding machine for injection molding to obtain a product sample. The temperature in the injection molding area is 200°C, and the temperature in the template area is 45°C.
实施例2Example 2
称取以下重量份的原料:Weigh the following raw materials in parts by weight:
制备例1制备的马来酸酐接枝玉米淀粉55重量份,大豆油(阿拉丁试剂)10重量份,马来酸酐接枝聚丙烯(通用级,宁波能之光新材料科技有限公司,型号为GPM200A)20重量份,乙烯-醋酸乙烯酯共聚物(韩国韩华,型号为1317型)15重量份。55 parts by weight of maleic anhydride grafted cornstarch prepared by Preparation Example 1, 10 parts by weight of soybean oil (Aladdin's reagent), maleic anhydride grafted polypropylene (general grade, Ningbo Nengzhiguang New Material Technology Co., Ltd., model is GPM200A) 20 parts by weight, 15 parts by weight of ethylene-vinyl acetate copolymer (Hanwha, Korea, type 1317).
将马来酸酐接枝玉米淀粉55重量份、大豆油10重量份、马来酸酐接枝聚丙烯20重量份和乙烯-醋酸乙烯酯共聚物15重量份混合均匀后,然后将混合后的物料加入至双螺杆挤出机中熔融共混(混合后的物料依次经过温度为160℃,170℃,175℃,170℃,170℃,170℃,170℃,160℃的熔融共混各区间)后拉条,切粒,得到颗粒状混合树脂;颗粒状混合树脂经除水干燥处理后,得到淀粉/聚丙烯可降解复合材料。选用的双螺杆挤出机的螺杆长径比为40∶1。After mixing 55 parts by weight of corn starch grafted with maleic anhydride, 10 parts by weight of soybean oil, 20 parts by weight of grafted polypropylene with maleic anhydride and 15 parts by weight of ethylene-vinyl acetate copolymer, the mixed materials were added After melting and blending in a twin-screw extruder (the mixed materials pass through the melt blending sections at temperatures of 160°C, 170°C, 175°C, 170°C, 170°C, 170°C, 170°C, and 160°C) Stranding and cutting into pellets to obtain granular mixed resin; the granular mixed resin is dehydrated and dried to obtain a starch/polypropylene degradable composite material. The selected twin-screw extruder has a screw length-to-diameter ratio of 40:1.
将上述得到的淀粉/聚丙烯可降解复合材料加入至注塑机中注塑成型,得到制品样条。注塑区温度200℃,模板区温度45℃。Add the starch/polypropylene degradable composite material obtained above into an injection molding machine for injection molding to obtain a product sample. The temperature in the injection molding area is 200°C, and the temperature in the template area is 45°C.
实施例3Example 3
称取以下重量份的原料:Weigh the following raw materials in parts by weight:
制备例1制备的马来酸酐接枝玉米淀粉55重量份,大豆油(阿拉丁试剂)10重量份,聚丙烯20(埃克森美孚,型号为7684KN)重量份,乙烯-醋酸乙烯酯共聚物(韩国韩华,型号为1317型)15重量份。55 parts by weight of maleic anhydride grafted cornstarch prepared by Preparation Example 1, 10 parts by weight of soybean oil (Aladdin's reagent), 20 parts by weight of polypropylene (ExxonMobil, model is 7684KN), ethylene-vinyl acetate copolymer (Korean Hanwha, model is 1317 type) 15 parts by weight.
将马来酸酐接枝玉米淀粉55重量份、大豆油10重量份、聚丙烯20重量份和乙烯-醋酸乙烯酯共聚物15重量份混合均匀后,然后将混合后的物料加入至双螺杆挤出机中熔融共混(混合后的物料依次经过温度为160℃,170℃,175℃,180℃,185℃,175℃,170℃,160℃的熔融共混各区间)后拉条,切粒,得到颗粒状混合树脂;颗粒状混合树脂经除水干燥处理后,得到淀粉/聚丙烯可降解复合材料。选用的双螺杆挤出机的螺杆长径比为40∶1。After mixing 55 parts by weight of cornstarch grafted with maleic anhydride, 10 parts by weight of soybean oil, 20 parts by weight of polypropylene and 15 parts by weight of ethylene-vinyl acetate copolymer, the mixed material is then added to the twin-screw extruder Melt blending in the machine (the mixed materials pass through the melt blending sections at temperatures of 160°C, 170°C, 175°C, 180°C, 185°C, 175°C, 170°C, and 160°C in sequence) and then slivered and pelletized to obtain a granular mixed resin; the granular mixed resin is dehydrated and dried to obtain a starch/polypropylene degradable composite material. The selected twin-screw extruder has a screw length-to-diameter ratio of 40:1.
将上述得到的淀粉/聚丙烯可降解复合材料加入至注塑机中注塑成型,得到制品样条。注塑区温度200℃,模板区温度45℃。Add the starch/polypropylene degradable composite material obtained above into an injection molding machine for injection molding to obtain a product sample. The temperature in the injection molding area is 200°C, and the temperature in the template area is 45°C.
实施例4Example 4
称取以下重量份的原料:Weigh the following raw materials in parts by weight:
制备例1制备的马来酸酐接枝玉米淀粉60重量份,大豆油(阿拉丁试剂)10重量份,聚丙烯(埃克森美孚,型号为7684KN)15重量份,乙烯-醋酸乙烯酯共聚物(韩国韩华,型号为1317型)15重量份。60 parts by weight of maleic anhydride grafted cornstarch prepared by Preparation Example 1, 10 parts by weight of soybean oil (Aladdin's reagent), 15 parts by weight of polypropylene (ExxonMobil, model is 7684KN), ethylene-vinyl acetate copolymer (Korean Hanwha, model is 1317 type) 15 parts by weight.
将马来酸酐接枝玉米淀粉60重量份、大豆油10重量份、聚丙烯15重量份和乙烯-醋酸乙烯酯共聚物15重量份混合均匀后,然后将混合后的物料加入至双螺杆挤出机中熔融共混(混合后的物料依次经过温度为160℃,170℃,175℃,170℃,175℃,170℃,160℃,160℃的熔融共混各区间)后拉条,切粒,得到颗粒状混合树脂;颗粒状混合树脂经除水干燥处理后,得到淀粉/聚丙烯可降解复合材料。选用的双螺杆挤出机的螺杆长径比为40∶1。After mixing 60 parts by weight of maleic anhydride grafted cornstarch, 10 parts by weight of soybean oil, 15 parts by weight of polypropylene and 15 parts by weight of ethylene-vinyl acetate copolymer, the mixed material is then added to the twin-screw extruder Melt blending in the machine (the mixed material passes through the melt blending sections with temperatures of 160°C, 170°C, 175°C, 170°C, 175°C, 170°C, 160°C, 160°C in sequence) and then strands, pelletized to obtain a granular mixed resin; the granular mixed resin is dehydrated and dried to obtain a starch/polypropylene degradable composite material. The selected twin-screw extruder has a screw length-to-diameter ratio of 40:1.
将上述得到的淀粉/聚丙烯可降解复合材料加入至注塑机中注塑成型,得到制品样条。注塑区温度200℃,模板区温度45℃。Add the starch/polypropylene degradable composite material obtained above into an injection molding machine for injection molding to obtain a product sample. The temperature in the injection molding area is 200°C, and the temperature in the template area is 45°C.
实施例5Example 5
称取以下重量份的原料:Weigh the following raw materials in parts by weight:
制备例1制备的马来酸酐接枝玉米淀粉60重量份,大豆油(阿拉丁试剂)10重量份,聚丙烯(埃克森美孚,型号为7684KN)20重量份,乙烯-醋酸乙烯酯共聚物(韩国韩华,型号为1317型)10重量份。60 parts by weight of maleic anhydride grafted cornstarch prepared by Preparation Example 1, 10 parts by weight of soybean oil (Aladdin's reagent), 20 parts by weight of polypropylene (ExxonMobil, model is 7684KN), ethylene-vinyl acetate copolymer (Korean Hanwha, model is 1317 type) 10 parts by weight.
将马来酸酐接枝玉米淀粉60重量份、大豆油10重量份、聚丙烯20重量份和乙烯-醋酸乙烯酯共聚物10重量份混合均匀后,然后将混合后的物料加入至双螺杆挤出机中熔融共混(混合后的物料依次经过温度为160℃,170℃,175℃,170℃,175℃,175℃,160℃,160℃的熔融共混各区间)后拉条,切粒,得到颗粒状混合树脂;颗粒状混合树脂经除水干燥处理后,得到淀粉/聚丙烯可降解复合材料。选用的双螺杆挤出机的螺杆长径比为40∶1。After mixing 60 parts by weight of cornstarch grafted with maleic anhydride, 10 parts by weight of soybean oil, 20 parts by weight of polypropylene and 10 parts by weight of ethylene-vinyl acetate copolymer, the mixed material is then added to the twin-screw extruder Melt blending in the machine (the mixed material passes through the melt blending sections with temperatures of 160°C, 170°C, 175°C, 170°C, 175°C, 175°C, 160°C, 160°C in sequence) and then strands, pelletized to obtain a granular mixed resin; the granular mixed resin is dehydrated and dried to obtain a starch/polypropylene degradable composite material. The selected twin-screw extruder has a screw length-to-diameter ratio of 40:1.
将上述得到的淀粉/聚丙烯可降解复合材料加入至注塑机中注塑成型,得到制品样条。注塑区温度200℃,模板区温度45℃。Add the starch/polypropylene degradable composite material obtained above into an injection molding machine for injection molding to obtain a product sample. The temperature in the injection molding area is 200°C, and the temperature in the template area is 45°C.
实施例6Example 6
称取以下重量份的原料:Weigh the following raw materials in parts by weight:
磷酸酯双淀粉(张家口神洲淀粉科技有限公司)60重量份,大豆油(阿拉丁试剂)10重量份,聚丙烯(埃克森美孚,型号为7684KN)15重量份,乙烯-醋酸乙烯酯共聚物(韩国韩华,型号为1317型)15重量份。Distarch phosphate (Zhangjiakou Shenzhou Starch Technology Co., Ltd.) 60 parts by weight, soybean oil (Aladdin reagent) 10 parts by weight, polypropylene (Exxon Mobil, model is 7684KN) 15 parts by weight, ethylene-vinyl acetate copolymer Thing (Korean Hanwha, model is 1317 type) 15 parts by weight.
将磷酸酯双淀粉60重量份、大豆油10重量份、聚丙烯15重量份和乙烯-醋酸乙烯酯共聚物15重量份混合均匀后,然后将混合后的物料加入至双螺杆挤出机中熔融共混(混合后的物料依次经过温度为160℃,170℃,175℃,170℃,175℃,175℃,160℃,160℃的熔融共混各区间)后拉条,切粒,得到颗粒状混合树脂;颗粒状混合树脂经除水干燥处理后,得到淀粉/聚丙烯可降解复合材料。选用的双螺杆挤出机的螺杆长径比为40∶1。Mix 60 parts by weight of distarch phosphate, 10 parts by weight of soybean oil, 15 parts by weight of polypropylene and 15 parts by weight of ethylene-vinyl acetate copolymer, and then add the mixed material into a twin-screw extruder to melt Blending (the mixed materials pass through the melt blending zones at temperatures of 160°C, 170°C, 175°C, 170°C, 175°C, 175°C, 160°C, and 160°C in turn) and then draw strands, pelletize, and obtain granules The granular mixed resin is dehydrated and dried to obtain a starch/polypropylene degradable composite material. The selected twin-screw extruder has a screw length-to-diameter ratio of 40:1.
将上述得到的淀粉/聚丙烯可降解复合材料加入至注塑机中注塑成型,得到制品样条。注塑区温度200℃,模板区温度45℃。Add the starch/polypropylene degradable composite material obtained above into an injection molding machine for injection molding to obtain a product sample. The temperature in the injection molding area is 200°C, and the temperature in the template area is 45°C.
实施例7Example 7
称取以下重量份的原料:Weigh the following raw materials in parts by weight:
乙酰化双淀粉己二酸酯(张家口神洲淀粉科技有限公司)60重量份,大豆油(阿拉丁试剂)10重量份,聚丙烯(埃克森美孚,型号为7684KN)15重量份,乙烯-醋酸乙烯酯共聚物(韩国韩华,型号为1317型)15重量份。Acetylated distarch adipate (Zhangjiakou Shenzhou Starch Technology Co., Ltd.) 60 parts by weight, soybean oil (Aladdin reagent) 10 parts by weight, polypropylene (Exxon Mobil, model is 7684KN) 15 parts by weight, ethylene- Vinyl acetate copolymer (Korea Hanwha, model is 1317 type) 15 parts by weight.
将乙酰化双淀粉己二酸酯60重量份、大豆油10重量份、聚丙烯15重量份和乙烯-醋酸乙烯酯共聚物15重量份混合均匀后,然后将混合后的物料加入至双螺杆挤出机中熔融共混(混合后的物料依次经过温度为160℃,170℃,175℃,170℃,175℃,175℃,160℃,160℃的熔融共混各区间)后拉条,切粒,得到颗粒状混合树脂;颗粒状混合树脂经除水干燥处理后,得到淀粉/聚丙烯可降解复合材料。选用的双螺杆挤出机的螺杆长径比为40∶1。Mix 60 parts by weight of acetylated distarch adipate, 10 parts by weight of soybean oil, 15 parts by weight of polypropylene and 15 parts by weight of ethylene-vinyl acetate copolymer, and then add the mixed material to the twin-screw extruder. Melt blending in the discharge machine (the mixed materials pass through the melt blending sections with temperatures of 160°C, 170°C, 175°C, 170°C, 175°C, 175°C, 160°C, and 160°C in sequence) and then pull the strips, cut granules to obtain a granular mixed resin; the granular mixed resin is dehydrated and dried to obtain a starch/polypropylene degradable composite material. The selected twin-screw extruder has a screw length-to-diameter ratio of 40:1.
将上述得到的淀粉/聚丙烯可降解复合材料加入至注塑机中注塑成型,得到制品样条。注塑区温度200℃,模板区温度45℃。Add the starch/polypropylene degradable composite material obtained above into an injection molding machine for injection molding to obtain a product sample. The temperature in the injection molding area is 200°C, and the temperature in the template area is 45°C.
实施例8Example 8
实施例8中植物油增塑剂采用花生油,其他同实施例7。Vegetable oil plasticizer adopts peanut oil among the embodiment 8, other is the same as embodiment 7.
实施例7与实施例8相比,采用大豆油作为植物油增塑剂制备的淀粉/聚丙烯可降解复合材料具有更好的性能,并且从市场化和工业化的角度来看,采用大豆油也更为廉价,淀粉/聚丙烯可降解复合材料的生产成本更低。Example 7 Compared with Example 8, the starch/polypropylene degradable composite material prepared by using soybean oil as a vegetable oil plasticizer has better performance, and from the perspective of marketization and industrialization, using soybean oil is also more efficient. Being cheap, starch/polypropylene biodegradable composites are cheaper to produce.
实施例9Example 9
称取以下重量份的原料:Weigh the following raw materials in parts by weight:
乙酰化双淀粉己二酸酯(张家口神洲淀粉科技有限公司)58重量份,大豆油(阿拉丁试剂)12重量份,聚丙烯(埃克森美孚,型号为7684KN)15重量份,乙烯-醋酸乙烯酯共聚物(韩国韩华,型号为1317型)15重量份。Acetylated distarch adipate (Zhangjiakou Shenzhou Starch Technology Co., Ltd.) 58 parts by weight, soybean oil (Aladdin reagent) 12 parts by weight, polypropylene (Exxon Mobil, model is 7684KN) 15 parts by weight, ethylene- Vinyl acetate copolymer (Korea Hanwha, model is 1317 type) 15 parts by weight.
将乙酰化双淀粉己二酸酯58重量份、大豆油12重量份、聚丙烯15重量份和乙烯-醋酸乙烯酯共聚物15重量份混合均匀后,然后将混合后的物料加入至双螺杆挤出机中熔融共混(混合后的物料依次经过温度为160℃,170℃,175℃,170℃,175℃,175℃,160℃,160℃的熔融共混各区间)后拉条,切粒,得到颗粒状混合树脂;颗粒状混合树脂经除水干燥处理后,得到淀粉/聚丙烯可降解复合材料。选用的双螺杆挤出机的螺杆长径比为40∶1。Mix 58 parts by weight of acetylated distarch adipate, 12 parts by weight of soybean oil, 15 parts by weight of polypropylene and 15 parts by weight of ethylene-vinyl acetate copolymer, and then add the mixed material to the twin-screw extruder. Melt blending in the discharge machine (the mixed materials pass through the melt blending sections with temperatures of 160°C, 170°C, 175°C, 170°C, 175°C, 175°C, 160°C, and 160°C in sequence) and then pull the strips, cut granules to obtain a granular mixed resin; the granular mixed resin is dehydrated and dried to obtain a starch/polypropylene degradable composite material. The selected twin-screw extruder has a screw length-to-diameter ratio of 40:1.
将上述得到的淀粉/聚丙烯可降解复合材料加入至注塑机中注塑成型,得到制品样条。注塑区温度200℃,模板区温度45℃。Add the starch/polypropylene degradable composite material obtained above into an injection molding machine for injection molding to obtain a product sample. The temperature in the injection molding area is 200°C, and the temperature in the template area is 45°C.
实施例10Example 10
称取以下重量份的原料:Weigh the following raw materials in parts by weight:
乙酰化双淀粉己二酸酯(张家口神洲淀粉科技有限公司)58重量份,大豆油(阿拉丁试剂)8重量份,聚丙烯(埃克森美孚,型号为7684KN)19重量份,乙烯-醋酸乙烯酯共聚物(韩国韩华,型号为1317型)15重量份。Acetylated distarch adipate (Zhangjiakou Shenzhou Starch Technology Co., Ltd.) 58 parts by weight, soybean oil (Aladdin reagent) 8 parts by weight, polypropylene (Exxon Mobil, model is 7684KN) 19 parts by weight, ethylene- Vinyl acetate copolymer (Korea Hanwha, model is 1317 type) 15 parts by weight.
将乙酰化双淀粉己二酸酯58重量份、大豆油12重量份、聚丙烯15重量份和乙烯-醋酸乙烯酯共聚物15重量份混合均匀后,然后将混合后的物料加入至双螺杆挤出机中熔融共混(混合后的物料依次经过温度为160℃,170℃,175℃,170℃,175℃,175℃,160℃,160℃的熔融共混各区间)后拉条,切粒,得到颗粒状混合树脂;颗粒状混合树脂经除水干燥处理后,得到淀粉/聚丙烯可降解复合材料。选用的双螺杆挤出机的螺杆长径比为40∶1。Mix 58 parts by weight of acetylated distarch adipate, 12 parts by weight of soybean oil, 15 parts by weight of polypropylene and 15 parts by weight of ethylene-vinyl acetate copolymer, and then add the mixed material to the twin-screw extruder. Melt blending in the discharge machine (the mixed materials pass through the melt blending sections with temperatures of 160°C, 170°C, 175°C, 170°C, 175°C, 175°C, 160°C, and 160°C in sequence) and then pull the strips, cut granules to obtain a granular mixed resin; the granular mixed resin is dehydrated and dried to obtain a starch/polypropylene degradable composite material. The selected twin-screw extruder has a screw length-to-diameter ratio of 40:1.
将上述得到的淀粉/聚丙烯可降解复合材料加入至注塑机中注塑成型,得到制品样条。注塑区温度200℃,模板区温度45℃。Add the starch/polypropylene degradable composite material obtained above into an injection molding machine for injection molding to obtain a product sample. The temperature in the injection molding area is 200°C, and the temperature in the template area is 45°C.
实施例9、实施例10与实施例7相比,主要区别在于大豆油的重量份,可见在大豆油的重量百分含量为10%时,制备的淀粉/聚丙烯可降解复合材料具有更好的性能。Embodiment 9, embodiment 10 compared with embodiment 7, main difference is the weight part of soybean oil, as seen when the weight percentage of soybean oil is 10%, the starch/polypropylene degradable composite material of preparation has better performance.
实施例11Example 11
称取以下重量份的原料:Weigh the following raw materials in parts by weight:
玉米淀粉(水分的重量百分含量为4.1%,诸城兴贸玉米开发有限公司)50重量份,大豆油(阿拉丁试剂)10重量份,聚丙烯(埃克森美孚,型号为7684KN)20重量份,乙烯-醋酸乙烯酯共聚物(韩国韩华,型号为1317型)20重量份。Cornstarch (the weight percentage of moisture is 4.1%, Zhucheng Xingmao Corn Development Co., Ltd.) 50 parts by weight, soybean oil (Aladdin's reagent) 10 parts by weight, polypropylene (ExxonMobil, model is 7684KN) 20 parts by weight Parts, 20 parts by weight of ethylene-vinyl acetate copolymer (Korea Hanwha, model is 1317 type).
将玉米淀粉50重量份、大豆油10重量份、聚丙烯20重量份和乙烯-醋酸乙烯酯共聚物20重量份混合均匀后,然后将混合后的物料加入至双螺杆挤出机中熔融共混(混合后的物料依次经过温度为165℃,165℃,170℃,170℃,170℃,165℃,160℃,160℃的熔融共混各区间)后拉条,切粒,得到颗粒状混合树脂;颗粒状混合树脂经除水干燥处理后,得到淀粉/聚丙烯可降解复合材料。选用的双螺杆挤出机的螺杆长径比为40∶1。After mixing 50 parts by weight of cornstarch, 10 parts by weight of soybean oil, 20 parts by weight of polypropylene and 20 parts by weight of ethylene-vinyl acetate copolymer, the mixed material is then added to a twin-screw extruder for melt blending (The mixed material passes through the melt blending zones with temperatures of 165°C, 165°C, 170°C, 170°C, 170°C, 165°C, 160°C, and 160°C in turn) and then draws, pelletizes, and obtains a granular mixture Resin; the granular mixed resin is dehydrated and dried to obtain a starch/polypropylene degradable composite material. The selected twin-screw extruder has a screw length-to-diameter ratio of 40:1.
将上述得到的淀粉/聚丙烯可降解复合材料加入至注塑机中注塑成型,得到制品样条。注塑区温度200℃,模板区温度45℃。Add the starch/polypropylene degradable composite material obtained above into an injection molding machine for injection molding to obtain a product sample. The temperature in the injection molding area is 200°C, and the temperature in the template area is 45°C.
实施例12Example 12
称取以下重量份的原料:Weigh the following raw materials in parts by weight:
玉米淀粉(水分的重量百分含量为4.1%,诸城兴贸玉米开发有限公司)55重量份,大豆油(阿拉丁试剂)10重量份,聚丙烯20重量份(埃克森美孚,型号为7684KN),乙烯-醋酸乙烯酯共聚物(韩国韩华,型号为1317型)15重量份。Cornstarch (the weight percentage of moisture is 4.1%, Zhucheng Xingmao Corn Development Co., Ltd.) 55 parts by weight, soybean oil (Aladdin's reagent) 10 parts by weight, polypropylene 20 parts by weight (Exxon Mobil, model is 7684KN ), ethylene-vinyl acetate copolymer (Korean Hanwha, model is 1317 type) 15 parts by weight.
将玉米淀粉55重量份、大豆油10重量份、聚丙烯20重量份和乙烯-醋酸乙烯酯共聚物15重量份混合均匀后,然后将混合后的物料加入至双螺杆挤出机中熔融共混(混合后的物料依次经过温度为165℃,165℃,170℃,170℃,170℃,165℃,160℃,160℃的熔融共混各区间)后拉条,切粒,得到颗粒状混合树脂;颗粒状混合树脂经除水干燥处理后,得到淀粉/聚丙烯可降解复合材料。选用的双螺杆挤出机的螺杆长径比为40∶1。After mixing 55 parts by weight of cornstarch, 10 parts by weight of soybean oil, 20 parts by weight of polypropylene and 15 parts by weight of ethylene-vinyl acetate copolymer, the mixed material is then added to a twin-screw extruder for melt blending (The mixed material passes through the melt blending zones with temperatures of 165°C, 165°C, 170°C, 170°C, 170°C, 165°C, 160°C, and 160°C in turn) and then draws, pelletizes, and obtains a granular mixture Resin; the granular mixed resin is dehydrated and dried to obtain a starch/polypropylene degradable composite material. The selected twin-screw extruder has a screw length-to-diameter ratio of 40:1.
将上述得到的淀粉/聚丙烯可降解复合材料加入至注塑机中注塑成型,得到制品样条。注塑区温度200℃,模板区温度45℃。Add the starch/polypropylene degradable composite material obtained above into an injection molding machine for injection molding to obtain a product sample. The temperature in the injection molding area is 200°C, and the temperature in the template area is 45°C.
将实施例1~10制备的淀粉/聚丙烯可降解复合材料按照ASTM D256-2006进行冲击性能测试(切口冲击试验,摆锤5.5J,四组实验取平均值),其测试结果如表1所示。将实施例11~12所制备的淀粉/聚丙烯可降解复合材料按照ASTM D 256-2006进行抗冲击性测试(切口冲击试验,摆锤5.5J,四组实验取平均值),按照GB1040-2006进行断裂伸长率和拉伸强度的测试(四组实验取平均值),其测试结果如表2所示。The starch/polypropylene degradable composite material prepared in Examples 1 to 10 was subjected to an impact performance test according to ASTM D256-2006 (notched impact test, pendulum 5.5J, average value of four groups of experiments), and the test results are shown in Table 1. Show. The starch/polypropylene degradable composite material prepared in Examples 11-12 is subjected to impact resistance test according to ASTM D 256-2006 (notch impact test, pendulum 5.5J, average value of four groups of experiments), according to GB1040-2006 Carry out the test of elongation at break and tensile strength (four groups of experiments take the average value), and its test results are shown in Table 2.
表1Table 1
表2Table 2
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Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1184822A (en) * | 1996-12-08 | 1998-06-17 | 柏柳青 | Degradable plastic made of chemically linked systhetic high molecule-natural high molecle |
CN101735483A (en) * | 2009-11-25 | 2010-06-16 | 马永亭 | Material for environmentally-friendly comb toothbrush and manufacturing process |
-
2012
- 2012-04-25 CN CN201210123934.5A patent/CN102634073B/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1184822A (en) * | 1996-12-08 | 1998-06-17 | 柏柳青 | Degradable plastic made of chemically linked systhetic high molecule-natural high molecle |
CN101735483A (en) * | 2009-11-25 | 2010-06-16 | 马永亭 | Material for environmentally-friendly comb toothbrush and manufacturing process |
Non-Patent Citations (2)
Title |
---|
《功能材料》 20090520 陈宪宏等 相容剂对可生物降解聚丙烯/淀粉共混材料的影响 第40卷, 第5期 * |
陈宪宏等: "相容剂对可生物降解聚丙烯/淀粉共混材料的影响", 《功能材料》 * |
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