CN1357563A - Prepn of biodegradable film of ternary starch-PVA-polyester system material - Google Patents
Prepn of biodegradable film of ternary starch-PVA-polyester system material Download PDFInfo
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- CN1357563A CN1357563A CN 01143500 CN01143500A CN1357563A CN 1357563 A CN1357563 A CN 1357563A CN 01143500 CN01143500 CN 01143500 CN 01143500 A CN01143500 A CN 01143500A CN 1357563 A CN1357563 A CN 1357563A
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- 229920000728 polyester Polymers 0.000 title claims abstract description 17
- 239000000463 material Substances 0.000 title abstract description 12
- 229920002472 Starch Polymers 0.000 claims abstract description 31
- 239000008107 starch Substances 0.000 claims abstract description 31
- 235000019698 starch Nutrition 0.000 claims abstract description 30
- 229920002451 polyvinyl alcohol Polymers 0.000 claims abstract description 23
- 239000004014 plasticizer Substances 0.000 claims abstract description 17
- 229920000515 polycarbonate Polymers 0.000 claims abstract description 11
- 239000004417 polycarbonate Substances 0.000 claims abstract description 11
- 229920006242 ethylene acrylic acid copolymer Polymers 0.000 claims abstract description 9
- 229920002554 vinyl polymer Polymers 0.000 claims abstract description 9
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 8
- 229920001610 polycaprolactone Polymers 0.000 claims abstract description 8
- 239000004632 polycaprolactone Substances 0.000 claims abstract description 8
- 229920000331 Polyhydroxybutyrate Polymers 0.000 claims abstract description 6
- 239000012744 reinforcing agent Substances 0.000 claims abstract description 6
- 229920001397 Poly-beta-hydroxybutyrate Polymers 0.000 claims abstract description 5
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical group OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 49
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- -1 dodecyl alcohol ester Chemical class 0.000 claims description 23
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 13
- 150000002148 esters Chemical class 0.000 claims description 9
- 229910021538 borax Inorganic materials 0.000 claims description 7
- 239000004328 sodium tetraborate Substances 0.000 claims description 7
- 235000010339 sodium tetraborate Nutrition 0.000 claims description 7
- LQZZUXJYWNFBMV-UHFFFAOYSA-N ethyl butylhexanol Natural products CCCCCCCCCCCCO LQZZUXJYWNFBMV-UHFFFAOYSA-N 0.000 claims description 6
- STCOOQWBFONSKY-UHFFFAOYSA-N tributyl phosphate Chemical group CCCCOP(=O)(OCCCC)OCCCC STCOOQWBFONSKY-UHFFFAOYSA-N 0.000 claims description 6
- 229920005906 polyester polyol Polymers 0.000 claims description 5
- 229920002545 silicone oil Polymers 0.000 claims description 5
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 4
- UMHKOAYRTRADAT-UHFFFAOYSA-N [hydroxy(octoxy)phosphoryl] octyl hydrogen phosphate Chemical compound CCCCCCCCOP(O)(=O)OP(O)(=O)OCCCCCCCC UMHKOAYRTRADAT-UHFFFAOYSA-N 0.000 claims description 4
- 239000013530 defoamer Substances 0.000 claims description 4
- KDYFGRWQOYBRFD-UHFFFAOYSA-N succinic acid Chemical compound OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- 239000004115 Sodium Silicate Substances 0.000 claims description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- GRLPQNLYRHEGIJ-UHFFFAOYSA-J potassium aluminium sulfate Chemical group [Al+3].[K+].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O GRLPQNLYRHEGIJ-UHFFFAOYSA-J 0.000 claims description 3
- 229920001592 potato starch Polymers 0.000 claims description 3
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 claims description 3
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 3
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 3
- 229920002261 Corn starch Polymers 0.000 claims description 2
- 240000002853 Nelumbo nucifera Species 0.000 claims description 2
- 235000006508 Nelumbo nucifera Nutrition 0.000 claims description 2
- PXKPLWLAZFIOMO-UHFFFAOYSA-K P(=O)([O-])([O-])[O-].C(CCCCCCC)[Ti+3]CCCCCCCC Chemical compound P(=O)([O-])([O-])[O-].C(CCCCCCC)[Ti+3]CCCCCCCC PXKPLWLAZFIOMO-UHFFFAOYSA-K 0.000 claims description 2
- 125000003545 alkoxy group Chemical group 0.000 claims description 2
- 239000008120 corn starch Substances 0.000 claims description 2
- QCHWBGRKGNYJSM-UHFFFAOYSA-N ethene Chemical group C=C.C=C.C=C QCHWBGRKGNYJSM-UHFFFAOYSA-N 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- 239000001384 succinic acid Substances 0.000 claims description 2
- 239000011206 ternary composite Substances 0.000 claims description 2
- 240000003183 Manihot esculenta Species 0.000 claims 1
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 claims 1
- 229940099112 cornstarch Drugs 0.000 claims 1
- 238000006068 polycondensation reaction Methods 0.000 claims 1
- 238000002360 preparation method Methods 0.000 claims 1
- 238000007664 blowing Methods 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 238000005453 pelletization Methods 0.000 abstract description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 abstract 1
- 238000012856 packing Methods 0.000 abstract 1
- 238000003756 stirring Methods 0.000 description 27
- 238000000071 blow moulding Methods 0.000 description 14
- 235000011187 glycerol Nutrition 0.000 description 11
- 239000007864 aqueous solution Substances 0.000 description 8
- 238000005469 granulation Methods 0.000 description 8
- 230000003179 granulation Effects 0.000 description 8
- 239000004698 Polyethylene Substances 0.000 description 6
- 238000000576 coating method Methods 0.000 description 6
- 239000011259 mixed solution Substances 0.000 description 6
- 229920000573 polyethylene Polymers 0.000 description 6
- 239000011248 coating agent Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 238000006065 biodegradation reaction Methods 0.000 description 4
- 239000004800 polyvinyl chloride Substances 0.000 description 4
- 229920000915 polyvinyl chloride Polymers 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- FZWBABZIGXEXES-UHFFFAOYSA-N ethane-1,2-diol;hexanedioic acid Chemical compound OCCO.OC(=O)CCCCC(O)=O FZWBABZIGXEXES-UHFFFAOYSA-N 0.000 description 3
- IHEDBVUTTQXGSJ-UHFFFAOYSA-M 2-[bis(2-oxidoethyl)amino]ethanolate;titanium(4+);hydroxide Chemical compound [OH-].[Ti+4].[O-]CCN(CC[O-])CC[O-] IHEDBVUTTQXGSJ-UHFFFAOYSA-M 0.000 description 2
- IUPHTVOTTBREAV-UHFFFAOYSA-N 3-hydroxybutanoic acid;3-hydroxypentanoic acid Chemical compound CC(O)CC(O)=O.CCC(O)CC(O)=O IUPHTVOTTBREAV-UHFFFAOYSA-N 0.000 description 2
- 229920013642 Biopol™ Polymers 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 229940103272 aluminum potassium sulfate Drugs 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229920006238 degradable plastic Polymers 0.000 description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000002362 mulch Substances 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 235000005985 organic acids Nutrition 0.000 description 2
- 238000001782 photodegradation Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- PAALZGOZEUHCET-UHFFFAOYSA-N 1,4-dioxecane-5,10-dione Chemical compound O=C1CCCCC(=O)OCCO1 PAALZGOZEUHCET-UHFFFAOYSA-N 0.000 description 1
- JRHWHSJDIILJAT-UHFFFAOYSA-N 2-hydroxypentanoic acid Chemical compound CCCC(O)C(O)=O JRHWHSJDIILJAT-UHFFFAOYSA-N 0.000 description 1
- SJZRECIVHVDYJC-UHFFFAOYSA-N 4-hydroxybutyric acid Chemical compound OCCCC(O)=O SJZRECIVHVDYJC-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- KMHZPJNVPCAUMN-UHFFFAOYSA-N Erbon Chemical compound CC(Cl)(Cl)C(=O)OCCOC1=CC(Cl)=C(Cl)C=C1Cl KMHZPJNVPCAUMN-UHFFFAOYSA-N 0.000 description 1
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical compound OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 1
- 244000017020 Ipomoea batatas Species 0.000 description 1
- 235000002678 Ipomoea batatas Nutrition 0.000 description 1
- 229920000562 Poly(ethylene adipate) Polymers 0.000 description 1
- 229920006266 Vinyl film Polymers 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- WNLRTRBMVRJNCN-UHFFFAOYSA-L adipate(2-) Chemical compound [O-]C(=O)CCCCC([O-])=O WNLRTRBMVRJNCN-UHFFFAOYSA-L 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229940037003 alum Drugs 0.000 description 1
- 229920000704 biodegradable plastic Polymers 0.000 description 1
- VJVOPINBJQWMNY-UHFFFAOYSA-N butanedioic acid;ethane-1,2-diol Chemical compound OCCO.OC(=O)CCC(O)=O VJVOPINBJQWMNY-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 150000007942 carboxylates Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- DDLKPTZZDDZLQN-UHFFFAOYSA-N decanedioic acid;ethane-1,2-diol Chemical compound OCCO.OC(=O)CCCCCCCCC(O)=O DDLKPTZZDDZLQN-UHFFFAOYSA-N 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 125000003438 dodecyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000010096 film blowing Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000000411 inducer Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000007539 photo-oxidation reaction Methods 0.000 description 1
- 239000013502 plastic waste Substances 0.000 description 1
- 239000004626 polylactic acid Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000003516 soil conditioner Substances 0.000 description 1
Landscapes
- Biological Depolymerization Polymers (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
技术领域:本发明涉及一种可完全生物降解的膜及使用电磁动态挤出机或普通吹塑机吹塑成膜的方法。Technical Field: The present invention relates to a fully biodegradable film and a method for blowing it into a film using an electromagnetic dynamic extruder or a common blow molding machine.
背景技术:在人们寻找可降解的地膜及包装材料以挽救日趋严重的聚乙烯等不降解塑料废弃物所带来的‘白色污染’时,最初的试探就是将可生物降解的淀粉及有机酸或酯引入到通常的聚乙烯膜中去或通过光氧化的途径达到此目的。因为无论是光降解,生物降解或光/生物双降解都是一个氧化的过程,其最终是变成酸或酯而分解为CO2和水以回归自然。所以聚乙烯/淀粉型、淀粉-聚乙烯丙烯酸-聚乙烯型降解膜及光降解膜相继问世。但发现,这类膜仅仅淀粉能降解而聚乙烯是不能被微生物分解的,因此这类膜经历了降温的过程,而代之为一系列有机酸或酯的研究和开发,如Biopol,此为羟基丁酸与羟基戊酸的共聚物,再如聚乳酸(PLA)、聚己内酯(PCL)、聚碳酸酯以及脂肪族二元羧酸与二元醇缩聚的酯,如日本的‘Bionolle’等相继问世,也确实很有成效。唯一不足之处是价格太贵,不能用于一般的包装材料和地膜。Background technology: When people are looking for degradable mulch and packaging materials to save the increasingly serious "white pollution" caused by non-degradable plastic waste such as polyethylene, the initial attempt is to use biodegradable starch and organic acids or The esters are incorporated into conventional polyethylene films or by photo-oxidation for this purpose. Because no matter it is photodegradation, biodegradation or photo/biodegradation, it is an oxidation process, which eventually turns into acid or ester and decomposes into CO2 and water to return to nature. Therefore, polyethylene/starch type, starch-polyethylene acrylic acid-polyethylene type degradable film and photodegradable film have come out one after another. However, it was found that this type of film can only be degraded by starch and polyethylene cannot be decomposed by microorganisms. Therefore, this type of film has undergone a cooling process and replaced it with the research and development of a series of organic acids or esters, such as Biopol, which is Copolymers of hydroxybutyric acid and hydroxyvaleric acid, such as polylactic acid (PLA), polycaprolactone (PCL), polycarbonate, and polycondensed esters of aliphatic dicarboxylic acids and dihydric alcohols, such as Japan's 'Bionolle ' and so on have come out one after another, and they are indeed very effective. The only downside is that it is too expensive to use for general wrapping materials and mulches.
美国F、H、Otey等研制了一种聚乙烯醇-淀粉-聚氯乙烯类型的膜(Ind,Eng、Chem、Prod、Res、Dev、1980,19,592-595),该膜含淀粉60%,聚乙烯醇15%左右,将聚氯乙烯溶胶涂复于聚乙烯醇-淀粉膜之上来提高膜的耐水能力。这种膜在不涂复聚氯乙烯的情况下,几乎没有湿强度,而聚氯乙烯的引入对降解是不利的。意大利Ferruxxi公司使用其相对量为70%的淀粉与30%的变性聚乙烯醇来制备的生物降解膜(MPI 1991,100,9,P7),称为Mater-Bi,具有完全降解的能力,且价格相对较低,被列为国际上驰名的三大可完全生物降解塑料品牌之一,另两类为英国ICI的Biopol,美国的Novon(近乎全淀粉)。但Mater-Bi有一个最大的弱点是耐温性,耐候性及耐水性不够而严重地限制了它的使用范围,如它不能在0-50℃以外,相对湿度30-80%以外的低温、高温及高湿环境条件下使用。U.S. F, H, Otey etc. have developed a kind of film of polyvinyl alcohol-starch-polyvinyl chloride type (Ind, Eng, Chem, Prod, Res, Dev, 1980,19,592-595), and this film contains starch 60 %, about 15% polyvinyl alcohol, the polyvinyl chloride sol is coated on the polyvinyl alcohol-starch film to improve the water resistance of the film. The film has little wet strength without a PVC coating, and the introduction of PVC is detrimental to degradation. The biodegradable film (MPI 1991,100,9,P7) prepared by Italian Ferruxxi company using its relative amount of 70% starch and 30% denatured polyvinyl alcohol, called Mater-Bi, has the ability of complete degradation, and The price is relatively low, and it is listed as one of the three most well-known brands of fully biodegradable plastics in the world. The other two are Biopol from the British ICI and Novon from the United States (nearly full starch). However, one of the biggest weaknesses of Mater-Bi is that its temperature resistance, weather resistance and water resistance are not enough, which seriously limits its scope of use. Use under high temperature and high humidity environment.
发明内容:本发明的目的是提供一种淀粉-聚乙烯醇-聚酯类三元体系生物降解膜的制备方法,该方法克服Mater-Bi在耐候、耐温及耐水方面的缺陷,以拓宽该类膜的使用范围,又可在短期内完全生物降解的膜,使用新型电磁动态吹塑机吹塑成膜,使膜的性能得到提高。Summary of the invention: The object of the present invention is to provide a method for preparing a starch-polyvinyl alcohol-polyester ternary system biodegradable film, which overcomes the defects of Mater-Bi in terms of weather resistance, temperature resistance and water resistance, so as to broaden the The scope of use of similar films, and films that can be completely biodegraded in a short period of time, are blown into films by using a new type of electromagnetic dynamic blow molding machine, so that the performance of the film is improved.
本发明的配方含有淀粉、聚乙烯醇、聚酯、主要选择聚碳酸酯、聚己内酯、聚乙烯丙烯酸酯、聚β-羟基丁酸酯或乙烯-丙烯酸共聚物、复配增塑剂、补强剂、湿强剂,经共混反应,造粒,吹塑成膜,也可通过T型头挤出成膜。The formula of the present invention contains starch, polyvinyl alcohol, polyester, mainly selected polycarbonate, polycaprolactone, polyethylene acrylate, poly β-hydroxybutyrate or ethylene-acrylic acid copolymer, compound plasticizer, Reinforcing agent, wet strength agent, through blending reaction, granulation, blow molding to form film, can also be extruded into film through T-shaped head.
本发明中以淀粉及聚乙烯醇为膜的主体。淀粉是生物降解的诱导剂,并可通过其在膜中含量来控制膜的降解时间及速率。但纯淀粉膜强度不够,聚乙烯醇具有生物可降解性,且可作为土壤改良剂,膜强度也好。但淀粉-聚乙烯醇膜湿强度差,耐水性不好,引入聚碳酸酯涂覆、聚己内酯、聚乙烯丙烯酸酯、聚β-羟基丁酸酯或乙烯-丙烯酸共聚物是为了提高膜的耐水性,特别是耐高温水的性能。如在淀粉-聚乙烯醇膜上涂覆聚碳酸酯后,可耐90℃以上的热水。而采用乙二醇∶甘油∶聚酯多元醇或含羟基的羧酸酯的三元复配增塑剂体系则有三大作用,一是起增塑作用、润滑作用;二是为了改善膜的耐候性,特别是改善膜的低温性能;三是为了提高所引入的聚酯与淀粉-聚乙烯醇体系的相容性,使它可接纳其它聚酯或乙烯-丙烯酸共聚物、聚乙烯丙烯酸酯等。同时补强剂及湿强剂的引入使膜的拉伸强度及湿强度均有很大提高,其拉伸强度最高可达24Mpa,比Mater-Bi要高,以上这些措施的实施使淀粉-聚乙烯醇膜无论在耐候性、耐温性及耐水性方面均比Mater-Bi有很大改善,使它接近聚乙烯膜的使用范围。In the present invention, starch and polyvinyl alcohol are used as the main body of the film. Starch is an inducer of biodegradation, and its content in the film can control the degradation time and rate of the film. However, the film strength of pure starch is not enough, polyvinyl alcohol is biodegradable, and can be used as a soil conditioner, and the film strength is also good. However, the starch-polyvinyl alcohol film has poor wet strength and poor water resistance. The introduction of polycarbonate coating, polycaprolactone, polyethylene acrylate, poly-β-hydroxybutyrate or ethylene-acrylic acid copolymer is to improve the film Excellent water resistance, especially the performance of high temperature water resistance. For example, after coating polycarbonate on the starch-polyvinyl alcohol film, it can withstand hot water above 90°C. The ternary compound plasticizer system using ethylene glycol: glycerin: polyester polyol or hydroxyl-containing carboxylate has three major functions, one is plasticizing and lubricating; the other is to improve the weather resistance of the film. The third is to improve the compatibility of the introduced polyester and starch-polyvinyl alcohol system, so that it can accept other polyesters or ethylene-acrylic acid copolymers, polyethylene acrylates, etc. . At the same time, the introduction of reinforcing agent and wet strength agent greatly improves the tensile strength and wet strength of the film, and its tensile strength can reach up to 24Mpa, which is higher than Mater-Bi. The implementation of the above measures makes the starch-polymer Vinyl alcohol film is much improved than Mater-Bi in terms of weather resistance, temperature resistance and water resistance, making it close to the use range of polyethylene film.
本发明选择的原料按重量百分含量:The raw material that the present invention selects is by weight percentage:
淀粉:30-65%, 聚乙烯醇:15-40%,Starch: 30-65%, Polyvinyl alcohol: 15-40%,
聚酯类:0-10%, 增塑剂:10-20%, Polyesters: 0-10%, Plasticizers: 10-20%,
补强剂:≤0.4%, 湿强剂:0.5-1.5%,Reinforcement agent: ≤0.4%, Wet strength agent: 0.5-1.5%,
消泡剂:≤0.4%, Defoamer: ≤0.4%,
其中淀粉为玉米淀粉、土豆淀粉、甘薯淀粉或藕粉;Wherein the starch is corn starch, potato starch, sweet potato starch or lotus root starch;
聚乙烯醇为聚乙烯醇-1799或聚乙烯醇-1999;Polyvinyl alcohol is polyvinyl alcohol-1799 or polyvinyl alcohol-1999;
聚酯为聚碳酸酯,聚己内酯、聚乙烯-丙烯酸酯,聚β-羟基丁酸酯或乙烯-丙烯酸共聚物;The polyester is polycarbonate, polycaprolactone, polyethylene-acrylate, poly-beta-hydroxybutyrate or ethylene-acrylic acid copolymer;
增塑剂按重量比为乙二醇∶甘油∶聚酯多元醇=1-3∶9-15∶3-6三元复合体系及水;聚酯多元醇为丁二酸至葵二酸的乙二醇、一缩乙二醇的缩聚酯或十二碳醇酯;The plasticizer is ethylene glycol: glycerol: polyester polyol = 1-3: 9-15: 3-6 ternary composite system and water by weight; polyester polyol is ethylene glycol from succinic acid to sebacic acid Glycols, condensed esters of ethylene glycol or lauryl esters;
补强剂为硫酸铝钾、碱式氧化铝、硼砂或硅酸钠;The reinforcing agent is aluminum potassium sulfate, basic alumina, borax or sodium silicate;
湿强剂为β-烷氧乙羧基二(焦磷酸二辛酯)钛、乙二撑烷氧基磷酸二辛酯钛或双异丙氧基三乙醇胺基钛酸酯;The wet strength agent is β-alkoxy ethyl carboxyl bis(dioctyl pyrophosphate) titanium, ethylene diethylene alkoxy phosphate dioctyl titanium or bisisopropoxy triethanolamine titanate;
消泡剂为磷酸三丁酯或硅油;The defoamer is tributyl phosphate or silicone oil;
本发明所使用的吹塑机为新型电磁动态吹塑机。具有长径比短及加热均匀的特点,使得它更适合于淀粉类降解塑料的加工,所制得的膜质均匀、亮丽。也可使用T型头加工成膜或片材。The blow molding machine used in the present invention is a novel electromagnetic dynamic blow molding machine. It has the characteristics of short length-to-diameter ratio and uniform heating, which makes it more suitable for the processing of starch-degradable plastics, and the obtained film is uniform and bright. It can also be processed into film or sheet using T-shaped head.
本发明所制得的膜,机械性能为拉伸强度在16MPa--24MPa,断裂伸长为140-200%;杨氏模量为130-400MPa;这类膜在淀粉含量为30%左右时,经二氧化碳释放量测定法测定,在四个月时的生物降解率最高可达85%以上,而淀粉含量为60%左右的膜在田间试铺,两个月时其表面已完全被细菌和微生物所侵蚀而变黑,半年左右已基本降解掉。The prepared film of the present invention has a mechanical property of tensile strength of 16MPa--24MPa, elongation at break of 140-200%; Young's modulus of 130-400MPa; when the starch content of this type of film is about 30%, According to the measurement method of carbon dioxide emission, the biodegradation rate can reach more than 85% in four months, and the film with a starch content of about 60% is tested in the field, and its surface has been completely covered by bacteria and microorganisms in two months. It was eroded and turned black, and it has basically degraded in about half a year.
Mater-Bi一般不能在0-50℃以外,相对湿度在30-80%以外的低温、高温及高湿环境下使用,而本发明所制得的膜在涂覆聚碳酸酯后一般可在聚乙烯膜所能用到的环境条件下使用,其耐水性、耐温性及耐候性比Mater-Bi好。本发明所制得的膜主要可用做购物袋、垃圾袋及包装袋,并可用做地膜。Mater-Bi generally cannot be used in low temperature, high temperature and high humidity environments other than 0-50 °C and relative humidity outside 30-80%, and the film prepared by the present invention can generally be used on polycarbonate after coating polycarbonate. Vinyl film can be used under the environmental conditions that can be used, and its water resistance, temperature resistance and weather resistance are better than Mater-Bi. The film prepared by the invention can be mainly used as shopping bags, garbage bags and packaging bags, and can also be used as mulching film.
具体实施方式如下:The specific implementation is as follows:
实施例1:按重量份称取PVA350份,淀粉500份,在混料机中搅匀。称取水230份,在水中加入硫酸铝钾3份,β-烷氧乙羧基二(焦磷酸二辛酯)钛10份,磷酸三丁酯3份,在搅拌下,将此水溶液加入混料机中同淀粉及PVA混合均匀。再称取乙二醇、甘油及十二碳醇酯之比为2∶15∶3的混合液200份,搅拌下,加入有上述物料的混料机中,搅匀,高速搅拌2分钟。在长径比为25∶1的45型单螺杆挤出机中造粒。在电磁动态挤出机或普通吹塑机上吹塑成膜。所制得的膜在涂覆机上用聚碳酸酯液涂覆用于制袋。Embodiment 1: Weigh 350 parts of PVA and 500 parts of starch by weight, and stir them evenly in a mixer. Weigh 230 parts of water, add 3 parts of aluminum potassium sulfate, 10 parts of β-alkoxyethyl carboxyl bis(dioctyl pyrophosphate)titanium, and 3 parts of tributyl phosphate into the water, and add this aqueous solution to the mixer under stirring Mix well with starch and PVA. Then weigh 200 parts of a mixture of ethylene glycol, glycerin and dodecyl alcohol ester in a ratio of 2:15:3, add the above-mentioned materials into a mixer under stirring, stir evenly, and stir at high speed for 2 minutes. Pelletization was performed in a single-screw extruder type 45 with an aspect ratio of 25:1. Blow molding into film on electromagnetic dynamic extruder or ordinary blow molding machine. The resulting film was coated with a polycarbonate solution on a coating machine for bag making.
实施例2:称取PVA250份,淀粉580份,在混料机中搅匀。称取水220份,水中加入3份硼砂及12份β-烷氧乙羧基二(焦磷酸二辛酯)钛,3份磷酸三丁酯,将此水溶液加入混料机中,同上述物料搅拌均匀。再称取乙二醇、甘油、己二酸乙二醇聚酯之比为2∶12∶4的增塑剂180份,加入混料机中,物料在搅拌下充分混合均匀,然后造粒,吹塑成膜。在涂复机上涂上聚碳酸酯溶液。其造粒、吹塑及涂覆过程大致同例1。所得之膜在2Kg/cm2压力,温度为150-160℃的封口机上制袋。Example 2: Weigh 250 parts of PVA and 580 parts of starch, and stir them evenly in a mixer. Weigh 220 parts of water, add 3 parts of borax, 12 parts of β-alkoxyethyl carboxyl bis(dioctyl pyrophosphate)titanium, and 3 parts of tributyl phosphate into the water, add this aqueous solution into the mixer, and stir with the above materials evenly . Then weigh 180 parts of plasticizers whose ratio of ethylene glycol, glycerin and adipic acid ethylene glycol polyester is 2:12:4, add in the mixer, the material is fully mixed under stirring, and then granulated, Blown into film. Apply the polycarbonate solution on a coater. Its granulation, blow molding and coating process are roughly the same as Example 1. The obtained film is made into bags on a sealing machine with a pressure of 2Kg/ cm2 and a temperature of 150-160°C.
实施例3:称取PVA250份,淀粉580份,在混料机中搅匀。再称取230份水,水中加入3份碱式氧化铝及双异丙氧基三乙醇胺基钛酸酯10份,硅油2份,水溶液一并加入混料机中。称取乙二醇、甘油及己二酸乙二醇聚酯之比为3∶10∶5的增塑剂180份,此中加入聚己内酯30份,一并加入混料机中,将物料搅匀。造粒及吹塑过程同例2。Embodiment 3: Weigh 250 parts of PVA and 580 parts of starch, and stir them evenly in a mixer. Then weigh 230 parts of water, add 3 parts of basic alumina, 10 parts of bisisopropoxy triethanolamine titanate, 2 parts of silicone oil into the water, and add the aqueous solution into the mixer. Weigh 180 parts of plasticizers whose ratio of ethylene glycol, glycerin and adipate glycol polyester is 3: 10: 5, add 30 parts of polycaprolactone to it, add in the mixer together, and Stir the material well. Granulation and blow molding process are the same as Example 2.
实施例4:称取PVA 250份,淀粉550份,在混料机中搅匀,再称取220份水,水中加入硼砂3份,双异丙氧基三乙醇胺基钛酸酯10份,磷酸三丁酯2份,将此水溶液加入混料机中,称取乙二醇、甘油∶十二碳醇之比为2∶11∶5的增塑剂180份,此中加入乙烯-丙烯酸共聚物30份,一并加入混料机中,物料搅匀,造粒及吹塑过程同例1。Example 4: Weigh 250 parts of PVA, 550 parts of starch, stir in a mixer, then weigh 220 parts of water, add 3 parts of borax, 10 parts of diisopropoxy triethanolamine titanate, phosphoric acid 2 parts of tributyl ester, add this aqueous solution into the mixer, weigh 180 parts of plasticizer with the ratio of ethylene glycol, glycerol: dodecyl alcohol of 2:11:5, add ethylene-acrylic acid copolymer 30 parts, add in the mixer together, the material is stirred evenly, granulation and blow molding process are the same as Example 1.
实施例5:称取聚乙烯醇220份,淀粉580份置于混料机中,搅匀,称取水220份,加入明矾3份,乙二撑烷氧基磷酸二辛酯钛10份,磷酸三丁酯2份于水中,在低速搅拌下加入混料机中,称取乙二醇、甘油、己二酸一缩乙二醇聚酯之比为3∶10∶4的混和液170份,加入聚乙烯---丙烯酸酯60份于此增塑剂体系中。在搅拌下,将其加入混料机中,物料搅匀后进行造粒及吹塑,造粒及吹塑过程同例1。Example 5: Weigh 220 parts of polyvinyl alcohol, 580 parts of starch and place them in a mixer, stir well, weigh 220 parts of water, add 3 parts of alum, 10 parts of dioctyl ethylene glycol phosphate titanium, phosphoric acid Put 2 parts of tributyl ester in water, add it into the mixer under low-speed stirring, weigh 170 parts of the mixed solution of ethylene glycol, glycerin and adipic acid ethylene glycol polyester in a ratio of 3:10:4, Add 60 parts of polyethylene --- acrylate to this plasticizer system. Under stirring, it is added in the mixer, and after the material is stirred evenly, it is granulated and blow-molded. The granulation and blow-molding process is the same as Example 1.
实施例6:称取PVA280份,淀粉520份,置与混料机中,称取水240份,加入硅酸钠3份,乙二撑烷氧基磷酸二辛酯钛12份,磷酸三丁酯2份于水中,在低速搅拌下,将此水溶液加入混料机中,称取乙二醇∶甘油∶葵二酸乙二醇酯比为5∶6∶5的增塑剂混合液160份,加入乙烯-丙烯酸共聚物30份于此增塑剂中,将加有聚乙烯---丙烯酸酯的增塑剂混合液加入混料机中,物料搅匀,其造粒及吹塑过程同上。Example 6: Weigh 280 parts of PVA, 520 parts of starch, put them in a mixer, weigh 240 parts of water, add 3 parts of sodium silicate, 12 parts of dioctyl ethylene glycol phosphate titanium, tributyl phosphate 2 parts in water, under low-speed stirring, this aqueous solution was added in the mixer, and ethylene glycol: glycerol: ethylene glycol sebacate ratio was weighed 160 parts of the plasticizer mixed liquid of 5: 6: 5, Add 30 parts of ethylene-acrylic acid copolymer to the plasticizer, put the plasticizer mixture with polyethylene-acrylic acid ester into the mixer, stir the materials evenly, and the granulation and blow molding process are the same as above.
实施例7:称取PVA200份,淀粉620份,置与混料机中,搅匀,称取水220份,在水中加入硼砂3份,乙二撑烷氧基磷酸二辛酯钛10份,硅油2份,将此水溶液加入混料机中,搅匀,称取甘油∶乙二醇∶己二酸乙二醇聚酯之比为1∶10∶5的混合液160份,此中加入EV A(VA含量为33%)50份,在搅拌下,将此混合液加入混料机中,物料搅匀,造粒与吹膜过程同上。Example 7: Weigh 200 parts of PVA, 620 parts of starch, put them in a mixer, stir well, weigh 220 parts of water, add 3 parts of borax, 10 parts of dioctyl ethylene glycol phosphate titanium, silicone oil 2 parts, add this aqueous solution into the mixer, stir well, weigh 160 parts of the mixed solution of glycerin: ethylene glycol: ethylene adipate glycol polyester ratio of 1: 10: 5, add EVA (VA content is 33%) 50 parts, under stirring, put this mixed solution into the mixer, stir the materials evenly, the process of granulation and film blowing is the same as above.
实施例8:称取PVA260份,淀粉560份,PHB20份于混料机中搅匀,称取水220份,在水中加入硼砂3份,乙二撑烷氧基磷酸二辛酯钛12份,硅油1份,将此水溶液加入混料机中,称取甘油∶己二酸乙二醇酯∶十二碳醇之比为12∶4∶3的增塑剂混合液190份,在搅拌下加入混料机中,物料搅匀后,其造粒及吹塑过程同上。Example 8: Weigh 260 parts of PVA, 560 parts of starch, and 20 parts of PHB in a mixer, stir well, weigh 220 parts of water, add 3 parts of borax to the water, 12 parts of ethylene glycol dioctyl phosphate titanium, silicone oil 1 part, add this aqueous solution into the mixer, weigh 190 parts of the plasticizer mixed solution with the ratio of glycerin: ethylene glycol adipate: dodecyl alcohol of 12:4:3, and add the mixed solution under stirring. In the feeder, after the material is stirred evenly, the granulation and blow molding process is the same as above.
实施例9:称取PVA250份,淀粉550份,在混料机中搅匀,加入水230份,在水中加入硼砂3份,乙二撑烷氧基磷酸二辛酯钛12份,磷酸三丁酯2份,在搅拌下,将此水溶液加入混料机中,搅匀,称取乙二醇∶甘油∶丁二酸乙二醇聚酯之比为3∶9∶6的混合液180份,加入聚乙烯丙烯酸酯共聚物∶乙烯-丙烯酸共聚物为2∶1的混合物60份于增塑剂中,搅拌下将此增塑剂混合液加入混料机中,搅匀,造粒及吹塑过程同上。Example 9: Weigh 250 parts of PVA, 550 parts of starch, stir well in a mixer, add 230 parts of water, add 3 parts of borax to the water, 12 parts of dioctyl ethylene glycol phosphate titanium, tributyl phosphate 2 parts of ester, under stirring, add this aqueous solution in the mixer, stir evenly, weigh 180 parts of the mixed solution whose ratio of ethylene glycol: glycerol: succinic acid ethylene glycol polyester is 3: 9: 6, Add 60 parts of a mixture of polyethylene acrylate copolymer: ethylene-acrylic acid copolymer at a ratio of 2:1 to the plasticizer, and add the plasticizer mixture to the mixer under stirring, stir well, granulate and blow molding The process is the same as above.
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