CN103819801A - Polyolefin wood-plastic composite and preparation method thereof - Google Patents
Polyolefin wood-plastic composite and preparation method thereof Download PDFInfo
- Publication number
- CN103819801A CN103819801A CN201410089582.5A CN201410089582A CN103819801A CN 103819801 A CN103819801 A CN 103819801A CN 201410089582 A CN201410089582 A CN 201410089582A CN 103819801 A CN103819801 A CN 103819801A
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- Prior art keywords
- ethylene
- polyolefin
- plastic composite
- antioxidant
- vinyl alcohol
- Prior art date
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- 229920001587 Wood-plastic composite Polymers 0.000 title claims abstract description 30
- 239000011155 wood-plastic composite Substances 0.000 title claims abstract description 30
- 229920000098 polyolefin Polymers 0.000 title claims abstract description 22
- 238000002360 preparation method Methods 0.000 title abstract description 11
- 229920000219 Ethylene vinyl alcohol Polymers 0.000 claims abstract description 53
- 239000000835 fiber Substances 0.000 claims abstract description 40
- -1 boards Substances 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims abstract description 15
- 238000002156 mixing Methods 0.000 claims abstract description 15
- 239000002994 raw material Substances 0.000 claims abstract description 10
- 239000000314 lubricant Substances 0.000 claims abstract description 7
- 239000004014 plasticizer Substances 0.000 claims abstract description 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 29
- 239000000843 powder Substances 0.000 claims description 26
- 239000000203 mixture Substances 0.000 claims description 25
- 239000003963 antioxidant agent Substances 0.000 claims description 19
- 230000003078 antioxidant effect Effects 0.000 claims description 19
- 235000011187 glycerol Nutrition 0.000 claims description 14
- 239000005977 Ethylene Substances 0.000 claims description 10
- 239000011159 matrix material Substances 0.000 claims description 10
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 9
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 8
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 7
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 7
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 7
- 239000011425 bamboo Substances 0.000 claims description 7
- 239000004698 Polyethylene Substances 0.000 claims description 6
- 239000004743 Polypropylene Substances 0.000 claims description 6
- 239000010445 mica Substances 0.000 claims description 6
- 229910052618 mica group Inorganic materials 0.000 claims description 6
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 6
- 229920000573 polyethylene Polymers 0.000 claims description 6
- 229920001155 polypropylene Polymers 0.000 claims description 6
- 238000011282 treatment Methods 0.000 claims description 6
- 239000000945 filler Substances 0.000 claims description 5
- 230000004048 modification Effects 0.000 claims description 5
- 238000012986 modification Methods 0.000 claims description 5
- KGRVJHAUYBGFFP-UHFFFAOYSA-N 2,2'-Methylenebis(4-methyl-6-tert-butylphenol) Chemical compound CC(C)(C)C1=CC(C)=CC(CC=2C(=C(C=C(C)C=2)C(C)(C)C)O)=C1O KGRVJHAUYBGFFP-UHFFFAOYSA-N 0.000 claims description 4
- PRWJPWSKLXYEPD-UHFFFAOYSA-N 4-[4,4-bis(5-tert-butyl-4-hydroxy-2-methylphenyl)butan-2-yl]-2-tert-butyl-5-methylphenol Chemical compound C=1C(C(C)(C)C)=C(O)C=C(C)C=1C(C)CC(C=1C(=CC(O)=C(C=1)C(C)(C)C)C)C1=CC(C(C)(C)C)=C(O)C=C1C PRWJPWSKLXYEPD-UHFFFAOYSA-N 0.000 claims description 4
- QZCLKYGREBVARF-UHFFFAOYSA-N Acetyl tributyl citrate Chemical compound CCCCOC(=O)CC(C(=O)OCCCC)(OC(C)=O)CC(=O)OCCCC QZCLKYGREBVARF-UHFFFAOYSA-N 0.000 claims description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 4
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims description 4
- 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 claims description 4
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 claims description 4
- ULBTUVJTXULMLP-UHFFFAOYSA-N butyl octadecanoate Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCCCC ULBTUVJTXULMLP-UHFFFAOYSA-N 0.000 claims description 4
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 4
- FLKPEMZONWLCSK-UHFFFAOYSA-N diethyl phthalate Chemical compound CCOC(=O)C1=CC=CC=C1C(=O)OCC FLKPEMZONWLCSK-UHFFFAOYSA-N 0.000 claims description 4
- SSDSCDGVMJFTEQ-UHFFFAOYSA-N octadecyl 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CCCCCCCCCCCCCCCCCCOC(=O)CCC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 SSDSCDGVMJFTEQ-UHFFFAOYSA-N 0.000 claims description 4
- FATBGEAMYMYZAF-KTKRTIGZSA-N oleamide Chemical compound CCCCCCCC\C=C/CCCCCCCC(N)=O FATBGEAMYMYZAF-KTKRTIGZSA-N 0.000 claims description 4
- 150000001282 organosilanes Chemical class 0.000 claims description 4
- 239000004800 polyvinyl chloride Substances 0.000 claims description 4
- 229920000915 polyvinyl chloride Polymers 0.000 claims description 4
- 239000000377 silicon dioxide Substances 0.000 claims description 4
- 235000012239 silicon dioxide Nutrition 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 239000010456 wollastonite Substances 0.000 claims description 4
- 229910052882 wollastonite Inorganic materials 0.000 claims description 4
- VSAWBBYYMBQKIK-UHFFFAOYSA-N 4-[[3,5-bis[(3,5-ditert-butyl-4-hydroxyphenyl)methyl]-2,4,6-trimethylphenyl]methyl]-2,6-ditert-butylphenol Chemical compound CC1=C(CC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)C(C)=C(CC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)C(C)=C1CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 VSAWBBYYMBQKIK-UHFFFAOYSA-N 0.000 claims description 3
- 235000021355 Stearic acid Nutrition 0.000 claims description 3
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 3
- 239000000194 fatty acid Substances 0.000 claims description 3
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 3
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 3
- 239000008117 stearic acid Substances 0.000 claims description 3
- KIHBGTRZFAVZRV-UHFFFAOYSA-N 2-hydroxyoctadecanoic acid Chemical class CCCCCCCCCCCCCCCCC(O)C(O)=O KIHBGTRZFAVZRV-UHFFFAOYSA-N 0.000 claims description 2
- MQWCQFCZUNBTCM-UHFFFAOYSA-N 2-tert-butyl-6-(3-tert-butyl-2-hydroxy-5-methylphenyl)sulfanyl-4-methylphenol Chemical compound CC(C)(C)C1=CC(C)=CC(SC=2C(=C(C=C(C)C=2)C(C)(C)C)O)=C1O MQWCQFCZUNBTCM-UHFFFAOYSA-N 0.000 claims description 2
- 239000005995 Aluminium silicate Substances 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- GHKOFFNLGXMVNJ-UHFFFAOYSA-N Didodecyl thiobispropanoate Chemical compound CCCCCCCCCCCCOC(=O)CCSCCC(=O)OCCCCCCCCCCCC GHKOFFNLGXMVNJ-UHFFFAOYSA-N 0.000 claims description 2
- 239000004793 Polystyrene Substances 0.000 claims description 2
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 claims description 2
- 235000012211 aluminium silicate Nutrition 0.000 claims description 2
- AGXUVMPSUKZYDT-UHFFFAOYSA-L barium(2+);octadecanoate Chemical compound [Ba+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O AGXUVMPSUKZYDT-UHFFFAOYSA-L 0.000 claims description 2
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 claims description 2
- 235000013539 calcium stearate Nutrition 0.000 claims description 2
- 239000008116 calcium stearate Substances 0.000 claims description 2
- 239000006229 carbon black Substances 0.000 claims description 2
- 239000004927 clay Substances 0.000 claims description 2
- 229910052570 clay Inorganic materials 0.000 claims description 2
- FPAFDBFIGPHWGO-UHFFFAOYSA-N dioxosilane;oxomagnesium;hydrate Chemical compound O.[Mg]=O.[Mg]=O.[Mg]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O FPAFDBFIGPHWGO-UHFFFAOYSA-N 0.000 claims description 2
- 239000011521 glass Substances 0.000 claims description 2
- 238000005469 granulation Methods 0.000 claims description 2
- 230000003179 granulation Effects 0.000 claims description 2
- 229910002804 graphite Inorganic materials 0.000 claims description 2
- 239000010439 graphite Substances 0.000 claims description 2
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 2
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims description 2
- 239000000347 magnesium hydroxide Substances 0.000 claims description 2
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 2
- 239000000395 magnesium oxide Substances 0.000 claims description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 2
- 229920001296 polysiloxane Polymers 0.000 claims description 2
- 229920002223 polystyrene Polymers 0.000 claims description 2
- 229920002635 polyurethane Polymers 0.000 claims description 2
- 239000004814 polyurethane Substances 0.000 claims description 2
- 229920002545 silicone oil Polymers 0.000 claims description 2
- 239000004408 titanium dioxide Substances 0.000 claims description 2
- 239000011787 zinc oxide Substances 0.000 claims description 2
- 235000013311 vegetables Nutrition 0.000 claims 6
- 239000004902 Softening Agent Substances 0.000 claims 3
- 235000006708 antioxidants Nutrition 0.000 claims 3
- 239000003112 inhibitor Substances 0.000 claims 3
- 230000003647 oxidation Effects 0.000 claims 3
- 238000007254 oxidation reaction Methods 0.000 claims 3
- VBICKXHEKHSIBG-UHFFFAOYSA-N 1-monostearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(O)CO VBICKXHEKHSIBG-UHFFFAOYSA-N 0.000 claims 2
- 150000002148 esters Chemical class 0.000 claims 2
- 239000010903 husk Substances 0.000 claims 2
- 238000001291 vacuum drying Methods 0.000 claims 2
- IHLDEDLAZNFOJB-UHFFFAOYSA-N 6-octoxy-6-oxohexanoic acid Chemical compound CCCCCCCCOC(=O)CCCCC(O)=O IHLDEDLAZNFOJB-UHFFFAOYSA-N 0.000 claims 1
- 241000345998 Calamus manan Species 0.000 claims 1
- 235000013162 Cocos nucifera Nutrition 0.000 claims 1
- 244000060011 Cocos nucifera Species 0.000 claims 1
- 240000007594 Oryza sativa Species 0.000 claims 1
- 235000007164 Oryza sativa Nutrition 0.000 claims 1
- 235000014676 Phragmites communis Nutrition 0.000 claims 1
- 244000082204 Phyllostachys viridis Species 0.000 claims 1
- 230000004913 activation Effects 0.000 claims 1
- 229910021502 aluminium hydroxide Inorganic materials 0.000 claims 1
- 238000011109 contamination Methods 0.000 claims 1
- JBSLOWBPDRZSMB-FPLPWBNLSA-N dibutyl (z)-but-2-enedioate Chemical compound CCCCOC(=O)\C=C/C(=O)OCCCC JBSLOWBPDRZSMB-FPLPWBNLSA-N 0.000 claims 1
- 229940075507 glyceryl monostearate Drugs 0.000 claims 1
- VLHZUYUOEGBBJB-UHFFFAOYSA-N hydroxy stearic acid Natural products OCCCCCCCCCCCCCCCCCC(O)=O VLHZUYUOEGBBJB-UHFFFAOYSA-N 0.000 claims 1
- 239000001788 mono and diglycerides of fatty acids Substances 0.000 claims 1
- LYRFLYHAGKPMFH-UHFFFAOYSA-N octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(N)=O LYRFLYHAGKPMFH-UHFFFAOYSA-N 0.000 claims 1
- 229940113162 oleylamide Drugs 0.000 claims 1
- 235000012950 rattan cane Nutrition 0.000 claims 1
- 235000009566 rice Nutrition 0.000 claims 1
- 229960001866 silicon dioxide Drugs 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 26
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- 239000004715 ethylene vinyl alcohol Substances 0.000 abstract description 6
- 238000012545 processing Methods 0.000 abstract description 5
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- 239000002131 composite material Substances 0.000 description 21
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- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 11
- 238000004519 manufacturing process Methods 0.000 description 10
- 239000002023 wood Substances 0.000 description 10
- 229920000642 polymer Polymers 0.000 description 9
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 8
- 241001330002 Bambuseae Species 0.000 description 6
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 6
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- 239000004628 starch-based polymer Substances 0.000 description 5
- 239000010902 straw Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical compound OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 239000007822 coupling agent Substances 0.000 description 4
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 4
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 4
- 238000011160 research Methods 0.000 description 4
- LDVVTQMJQSCDMK-UHFFFAOYSA-N 1,3-dihydroxypropan-2-yl formate Chemical compound OCC(CO)OC=O LDVVTQMJQSCDMK-UHFFFAOYSA-N 0.000 description 3
- 229920002261 Corn starch Polymers 0.000 description 3
- MTUBBMSQXXJFQP-UHFFFAOYSA-N OC(CCCCCCCCCCCCCCCCC(=O)OCC(O)CO)(O)O Chemical compound OC(CCCCCCCCCCCCCCCCC(=O)OCC(O)CO)(O)O MTUBBMSQXXJFQP-UHFFFAOYSA-N 0.000 description 3
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- XNGIFLGASWRNHJ-UHFFFAOYSA-L phthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC=C1C([O-])=O XNGIFLGASWRNHJ-UHFFFAOYSA-L 0.000 description 1
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- FHALLNHVVFMRCA-UHFFFAOYSA-N propane-1,2,3-triol 18,18,18-trihydroxyoctadecanoic acid Chemical compound OC(CCCCCCCCCCCCCCCCC(=O)O)(O)O.OCC(O)CO FHALLNHVVFMRCA-UHFFFAOYSA-N 0.000 description 1
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Abstract
本发明公开了一种聚烯烃基木塑复合材料及其制备方法,采用聚烯烃和乙烯-乙烯醇共聚物(EVOH)改性的植物纤维为主要原料,添加增塑剂、稳定剂、润滑剂等通过塑料加工中通用的熔融共混方法制备出机械性能良好、环境友好的木塑复合材料。本发明的木塑复合材料可用于如建材、装饰材料、发泡材料、板材、包装材料、玩具、汽车零件等常规领域,拓宽了乙烯-乙烯醇共聚物的应用范围。The invention discloses a polyolefin-based wood-plastic composite material and a preparation method thereof. Plant fibers modified by polyolefin and ethylene-vinyl alcohol copolymer (EVOH) are used as main raw materials, and plasticizers, stabilizers and lubricants are added. prepared wood-plastic composites with good mechanical properties and environmental friendliness through the common melt blending method in plastic processing. The wood-plastic composite material of the present invention can be used in conventional fields such as building materials, decorative materials, foaming materials, boards, packaging materials, toys, auto parts, etc., which broadens the application range of the ethylene-vinyl alcohol copolymer.
Description
技术领域 technical field
本发明属于聚合物加工技术领域,具体涉及一种聚烯烃基木塑复合材料及其制备方法。 The invention belongs to the technical field of polymer processing, and in particular relates to a polyolefin-based wood-plastic composite material and a preparation method thereof. the
背景技术 Background technique
木塑复合材料是以植物纤维为主要组分与热塑性塑料通过一定的成型加工方法复合而形成的一种新型材料,其兼具天然纤维与塑料的双重特性,能弥补两者的不足、克服木材的强度低和变异性大等使用局限性,具有价格低廉、力学性能好、耐酸碱腐蚀、可回收利用等特点,可在多种场合替代木材使用,它的研制和推广将有效缓解我国石油和森林资源供应紧缺的矛盾,减少塑料和农业废弃物焚烧对环境的污染。 Wood-plastic composite material is a new type of material formed by compounding plant fiber as the main component and thermoplastic plastic through certain molding and processing methods. It has the dual characteristics of natural fiber and plastic, and can make up for the shortcomings of both and overcome wood It has low strength and large variability and other limitations in use. It has the characteristics of low price, good mechanical properties, acid and alkali corrosion resistance, and recyclability. It can be used instead of wood in many occasions. Its development and promotion will effectively relieve my country's petroleum Contradictions with the shortage of forest resource supply, reduce environmental pollution caused by plastic and agricultural waste incineration. the
然而,尽管发展木塑复合材料的意义重大,但它的开发与应用也面临着许多问题。由于植物纤维表面含有大量的醇羟基和酚羟基,这些羟基易形成分子间或分子内氢键,具有强极性和吸水性;而热塑性聚合物表面一般为非极性或弱极性,当两者复合时植物纤维在聚合物基体中的分散性不佳,易发生团聚,两者相容性差,界面咬合力较弱。当材料受到外力作用时,应力在界面处不能得到有效传递,容易发生界面脱粘使得材料发生破坏。因此,提高植物纤维与聚合物间的界面相容性,是制备木塑复合材料要解决的关键问题。 However, although the development of wood-plastic composite materials is of great significance, its development and application are also facing many problems. Since the surface of plant fibers contains a large number of alcoholic and phenolic hydroxyl groups, these hydroxyl groups are easy to form intermolecular or intramolecular hydrogen bonds, which have strong polarity and water absorption; while the surface of thermoplastic polymers is generally non-polar or weakly polar, when the two When compounding, the dispersion of plant fibers in the polymer matrix is not good, agglomeration is easy to occur, the compatibility between the two is poor, and the interfacial occlusal force is weak. When the material is subjected to external force, the stress cannot be effectively transmitted at the interface, and the interface debonding is prone to occur and the material will be damaged. Therefore, improving the interfacial compatibility between plant fibers and polymers is a key issue to be solved in the preparation of wood-plastic composites. the
国内许多学者对如何提高植物纤维与聚合物基体的相容性进行了大量的研究,一般采取通过物理或化学的手段处理植物纤维或添加相容剂来改善纤维与基体之间的相容性,如采用碱处理、酰化、醚化植物纤维或添加硅烷偶联剂、异氰酸酯偶联剂、马来酸酐接枝聚合物等作为相容剂,以期改善植物纤维与聚合物基体的相容性,但这些方法均有一些不足之处。如用碱处理植物纤维主要是通过溶解植物纤维中的果胶、木质素等,增加植物纤维与聚合物基体的接触面来提高界面咬合力,属于物理机械咬合作用,对制品性能的提高有限;而且碱处理方法过程繁琐,处理的废液会对环境造成严重的污染,一般较少采用。偶联剂是一类处理效果较好的相容剂,但由于偶联剂价格比较昂贵,限制了它在工业上的应用。接枝聚合物是目前研究最多的一类相容剂,其中以马来酸酐接枝聚合物最为普遍。但马来酸酐接枝聚合物的生产需要另外的工序,而且生产过程中马来酸酐等小分子接枝单体的挥发对操作人员的呼吸道和眼睛产生严重的刺激,危害环境和操作人员身体健康。虽然使用马来酸酐接枝聚合物作为相容剂的原理是基于马来酸酐可与植物纤维上醇羟基和酚羟基发生酯化反应,但是由于马来酸酐接枝聚合物与植物纤维之间的酯化反应是大分子间反应,反应较为困难,现有资料并没有明确充分的实验事实证明酸酐基团与植物纤维发生了化学作用,因此它们之间的作用是物理的氢键作用还是化学结合还有待进一步的科学探索;而且由于马来酸酐接枝聚合物的接枝率较低,一般仅为0.4%~1%,因此要达到处理目的,需要的马来酸酐接枝聚合物用量较大。因此接枝聚合物作为相容剂使用首先要解决相容剂接枝率低的问题,但目前尚无较好的解决方法。近几年来,不少学者一直致力于聚烯烃多元接枝共聚物的研究(如中国专利申请号02118793,200510035486.3),以提高相容剂中极性基团的接枝率,但此方法类似于马来酸酐接枝聚合物的生产。制备方法及操作工艺较复杂,成本高,且同样存在小分子接枝单体对操作人员身体健康和环境的危害。 Many domestic scholars have done a lot of research on how to improve the compatibility between plant fibers and polymer matrix. Generally, physical or chemical means are used to treat plant fibers or add compatibilizers to improve the compatibility between fibers and the matrix. Such as using alkali treatment, acylation, etherification of plant fibers or adding silane coupling agents, isocyanate coupling agents, maleic anhydride grafted polymers, etc. as compatibilizers, in order to improve the compatibility between plant fibers and polymer matrix, But these methods have some shortcomings. For example, the treatment of plant fibers with alkali mainly dissolves pectin and lignin in plant fibers to increase the contact surface between plant fibers and polymer matrix to improve interfacial occlusal force, which belongs to physical and mechanical occlusion, and has limited improvement in product performance; Moreover, the process of the alkali treatment method is cumbersome, and the treated waste liquid will cause serious pollution to the environment, so it is generally seldom used. Coupling agent is a kind of compatibilizer with better treatment effect, but its application in industry is limited due to the high price of coupling agent. Graft polymers are the most researched class of compatibilizers, among which maleic anhydride graft polymers are the most common. However, the production of maleic anhydride grafted polymers requires another process, and the volatilization of small molecule grafted monomers such as maleic anhydride during the production process will cause serious irritation to the respiratory tract and eyes of operators, endangering the environment and the health of operators . Although the principle of using the maleic anhydride grafted polymer as a compatibilizer is based on the esterification reaction between the maleic anhydride grafted polymer and the phenolic hydroxyl group on the plant fiber, but due to the interaction between the maleic anhydride grafted polymer and the plant fiber The esterification reaction is a reaction between macromolecules, and the reaction is relatively difficult. There are no clear and sufficient experimental facts to prove that the acid anhydride group has a chemical interaction with the plant fiber, so the interaction between them is physical hydrogen bonding or chemical combination. Further scientific exploration is still needed; and because the grafting rate of maleic anhydride grafted polymers is low, generally only 0.4% to 1%, so to achieve the purpose of treatment, the amount of maleic anhydride grafted polymers required is relatively large . Therefore, the use of graft polymer as a compatibilizer must first solve the problem of low grafting rate of the compatibilizer, but there is no better solution at present. In recent years, many scholars have been committed to the research of polyolefin multi-graft copolymers (such as Chinese patent application No. 02118793, 200510035486.3), in order to increase the grafting rate of polar groups in the compatibilizer, but this method is similar to Production of maleic anhydride grafted polymers. The preparation method and operation process are relatively complicated, the cost is high, and there are also hazards to the health of operators and the environment caused by the small-molecule grafted monomer. the
针对现有技术存在的问题,本发明采用商品化的乙烯-乙烯醇共聚物(EVOH)改性植物纤维。由于乙烯-乙烯醇共聚物中高达70-30 %摩尔含量的乙烯醇结构单元,可与植物纤维表面含有的大量醇羟基和酚羟基产生氢键作用,天然地使其与植物纤维存在良好的相容性;且乙烯-乙烯醇共聚物中高达30-70%摩尔含量的乙烯结构单元与基体聚合物有良好的亲和性,可产生二者间大分子链缠绕,因此乙烯-乙烯醇共聚物作为替代上文中提及的常见相容剂、偶联剂等改性手段,可以很好地改善植物纤维与聚合物基体间的相容性,从而赋予聚烯烃基木塑复合材料良好的力学性能。这种改性方法目前尚无相关文献和专利报道。 Aiming at the problems existing in the prior art, the present invention adopts commercialized ethylene-vinyl alcohol copolymer (EVOH) to modify plant fibers. Since the vinyl alcohol structural unit in the ethylene-vinyl alcohol copolymer has a molar content of up to 70-30%, it can generate hydrogen bonds with a large number of alcoholic and phenolic hydroxyl groups on the surface of plant fibers, naturally making it have a good phase with plant fibers. Capacitance; and the ethylene structural unit with a molar content of up to 30-70% in the ethylene-vinyl alcohol copolymer has good affinity with the matrix polymer, which can produce macromolecular chain entanglement between the two, so the ethylene-vinyl alcohol copolymer As an alternative to the common compatibilizers and coupling agents mentioned above, it can well improve the compatibility between plant fibers and polymer matrix, thus endowing polyolefin-based wood-plastic composites with good mechanical properties . There are no relevant literature and patent reports on this modification method at present. the
检索大量的专利文献和公开发表的相关研究论文,仅发现张玉军等人在《黑龙江大学自然科学学报》上(2006, 23 (1 ): 124-127)发表了“EVOH /蒙脱土插层复合材料的制备与结构表征”,该研究以聚乙烯吡咯烷酮改性蒙脱土 (MMT)为无机相, 以乙烯- 乙烯醇共聚物为基体树脂, 通过熔融插层制备出了EVOH /蒙脱土复合材料,减少复合材料的吸湿性,并改善性价比。唐忠柱等人在《功能高分子学报》(2005, 18 (3): 368-372)上发表了“热塑性淀粉/乙烯-乙烯醇共聚物复合材料的制备与性能”,该研究用乙烯-乙烯醇共聚物与热塑性淀粉共混制备淀粉基生物降解材料,通过控制复合体系中乙烯-乙烯醇共聚物与热塑性淀粉的配比来控制复合体系的降解性能,乙烯-乙烯醇共聚物的加入量在10-40%之间,类似的研究还有张美洁等人在《塑料工业》(2003, 31( 1) : 27- 29)发表的“TPS/ EVOH 共混物的制备及性能研究”。上述文中都只是把乙烯-乙烯醇共聚物作为与热塑性淀粉的共混原料以提高淀粉/乙烯-乙烯醇共聚物复合材料的降解性能,配方中价格昂贵的乙烯-乙烯醇共聚物的用量大,也没有明确指出把乙烯-乙烯醇共聚物作为热塑性淀粉的表面改性剂。同时检索到1篇有关乙烯-乙烯醇共聚物基复合材料的授权专利(ZL 201110189511.9),该专利提供了一种利用硫酸钙和玉米淀粉制造乙烯-乙烯醇共聚物基复合材料及其制备工艺,其目的是为了降低乙烯-乙烯醇共聚物基复合材料的成本,并赋予复合材料一定的降解性。该专利通过加入硬脂酸对硫酸钙进行表面活化改性,以提高硫酸钙、玉米淀粉与乙烯-乙烯醇共聚物的相容性, 同时改善熔体的流动性和复合材料的表面光滑度,可见该专利权人并未认识到乙烯-乙烯醇共聚物对硫酸钙和玉米淀粉存在的相容作用,而且专利ZL 201110189511.9所涉及的添加物硫酸钙和玉米淀粉与本申请中植物纤维在科学分类中属于两类完全不同的物质,即该专利对本发明无启示作用。本发明直接利用乙烯-乙烯醇共聚物作为改善木塑复合材料中聚合物基体和植物纤维间的相容性,这一改性原理和改性方法系本申请人首次提出。 Searching a large number of patent documents and published related research papers only found that Zhang Yujun and others published "EVOH/montmorillonite intercalation composite Preparation and structural characterization of materials", the study used polyvinylpyrrolidone modified montmorillonite (MMT) as the inorganic phase, ethylene-vinyl alcohol copolymer as the matrix resin, and prepared EVOH/montmorillonite composite by melt intercalation materials, reducing the moisture absorption of composites and improving cost performance. Tang Zhongzhu and others published "Preparation and Properties of Thermoplastic Starch/Ethylene-Vinyl Alcohol Copolymer Composite Materials" in "Journal of Functional Polymers" (2005, 18 (3): 368-372). The study used ethylene-vinyl alcohol The copolymer and thermoplastic starch are blended to prepare starch-based biodegradable materials. The degradation performance of the composite system is controlled by controlling the ratio of ethylene-vinyl alcohol copolymer and thermoplastic starch in the composite system. The amount of ethylene-vinyl alcohol copolymer added is 10 Between -40%, similar studies include "Preparation and Performance Research of TPS/EVOH Blends" published by Zhang Meijie et al. in "Plastic Industry" (2003, 31(1): 27-29). In the above-mentioned papers, only the ethylene-vinyl alcohol copolymer is used as a blending material with thermoplastic starch to improve the degradation performance of the starch/ethylene-vinyl alcohol copolymer composite material, and the expensive ethylene-vinyl alcohol copolymer is used in a large amount in the formula. There is also no clear indication that ethylene-vinyl alcohol copolymer is used as a surface modifier for thermoplastic starch. At the same time, 1 authorized patent (ZL 201110189511.9) related to ethylene-vinyl alcohol copolymer-based composite materials was retrieved. This patent provides a method for manufacturing ethylene-vinyl alcohol copolymer-based composite materials using calcium sulfate and corn starch and its preparation process. Its purpose is to reduce the cost of ethylene-vinyl alcohol copolymer-based composite materials and endow the composite materials with certain degradability. This patent activates the surface of calcium sulfate by adding stearic acid to improve the compatibility of calcium sulfate, corn starch and ethylene-vinyl alcohol copolymer, and at the same time improve the fluidity of the melt and the surface smoothness of the composite material. It can be seen that the patentee did not realize the compatibility effect of ethylene-vinyl alcohol copolymer on calcium sulfate and corn starch, and the additives involved in patent ZL 201110189511.9 and the plant fiber in the scientific classification belong to two completely different substances, that is, the patent has no enlightening effect on the present invention. The present invention directly uses ethylene-vinyl alcohol copolymer to improve the compatibility between the polymer matrix and plant fibers in the wood-plastic composite material. This modification principle and modification method are proposed by the applicant for the first time. the
发明内容 Contents of the invention
本发明的目的在于提供一种聚烯烃基木塑复合材料及其制备方法,工艺简单,操作方便,生产效率高,制品生产成本低,得到的木塑复合材料具有价廉无毒、环境友好、良好的机械性能和材料可回收利用等优点,可用于如食品包装、玩具、建材、装饰材料、发泡材料、板材、汽车零件等领域,扩大了乙烯-乙烯醇共聚物的应用范围, The purpose of the present invention is to provide a polyolefin-based wood-plastic composite material and its preparation method, which has simple process, convenient operation, high production efficiency, low product production cost, and the obtained wood-plastic composite material is cheap, non-toxic, environmentally friendly, Good mechanical properties and recyclable materials can be used in fields such as food packaging, toys, building materials, decorative materials, foam materials, plates, auto parts, etc., expanding the application range of ethylene-vinyl alcohol copolymers,
为实现上述目的,本发明采用如下技术方案: To achieve the above object, the present invention adopts the following technical solutions:
按重量份计的原料配方为: The formula of raw materials in parts by weight is:
所述的聚烯烃为所述的塑料包括以下热塑性塑料:聚乙烯、聚丙烯、聚氯乙烯、聚苯乙烯、聚乙烯-醋酸乙烯酯,或是由它们组成的混合物。 The said polyolefin is said plastic including the following thermoplastics: polyethylene, polypropylene, polyvinyl chloride, polystyrene, polyethylene-vinyl acetate, or a mixture thereof.
所述的植物纤维原料包括木粉、竹粉及其它木质植物的茎叶、秆、壳等任何一种粉碎后的纤维或者它们的混合物。其纤维的平均粒径优选为20目以上,含水量优选在5%以下。 The plant fiber raw material includes wood powder, bamboo powder and any kind of pulverized fiber such as stems, leaves, stalks and shells of other woody plants or a mixture thereof. The average particle size of the fibers is preferably above 20 mesh, and the water content is preferably below 5%. the
所述的乙烯-乙烯醇共聚物的乙烯摩尔含量为30-70%。 The ethylene molar content of the ethylene-vinyl alcohol copolymer is 30-70%. the
所述的增塑剂是邻苯二甲酸辛十三酯、邻苯二甲酸辛十四酯、邻苯二甲酸二乙酯、乙酰柠檬酸三丁酯、氯化石蜡、顺丁烯二酸二丁酯、硬脂酸、硬脂酸锌、硬脂酸钙、硬脂酸钡、己二酸二辛酯或聚氨酯增塑剂,或是由它们组成的混合物。 The plasticizer is octyl tridecyl phthalate, octyl tetradecyl phthalate, diethyl phthalate, acetyl tributyl citrate, chlorinated paraffin, dimaleic acid Butyl esters, stearic acid, zinc stearate, calcium stearate, barium stearate, dioctyl adipate or polyurethane plasticizers, or mixtures thereof. the
所述的抗氧剂是抗氧剂330、抗氧剂3114、抗氧剂1076、抗氧剂1010、抗氧剂CA、抗氧剂DLTP、抗氧剂2246、抗氧剂2246-S或抗氧剂300,或是由它们组成的混合物。 Described antioxidant is antioxidant 330, antioxidant 3114, antioxidant 1076, antioxidant 1010, antioxidant CA, antioxidant DLTP, antioxidant 2246, antioxidant 2246-S or antioxidant Oxygen 300, or a mixture of them. the
所述的润滑剂是指所述润滑剂为聚乙烯蜡、羟基硬脂酸、硬脂酸正丁酯、硬脂酸单甘油酯、油酰胺、硅油、硅酮、有机硅烷、液体石蜡、甘油三羟硬脂酸酯、N,N-乙撑双硬脂酸酰胺或极性基团改性的乙撑双脂肪酸酰胺,或是由它们组成的混合物。 Described lubricant means that described lubricant is polyethylene wax, hydroxystearic acid, n-butyl stearate, monoglyceride stearate, oleamide, silicone oil, silicone, organosilane, liquid paraffin, glycerin Trihydroxystearate, N,N-ethylene bisstearic acid amide or polar group modified ethylene bis fatty acid amide, or a mixture of them. the
所述的填料是碳酸钙、硅灰石、高岭土、粘土、云母、二氧化硅、玻璃微珠、石墨、碳黑、滑石粉、二氧化钛、氢氧化镁、氢氧化铝、氧化镁、氧化铝、硫酸钡、氧化锌,或是它们组成的混合物。 Described filler is calcium carbonate, wollastonite, kaolin, clay, mica, silicon dioxide, glass microspheres, graphite, carbon black, talcum powder, titanium dioxide, magnesium hydroxide, aluminum hydroxide, magnesium oxide, aluminum oxide, Barium sulfate, zinc oxide, or a mixture thereof. the
将以上所述的组分包括塑料、植物纤维、增塑剂、稳定剂、润滑剂和填料等通过塑料加工中通用的熔融共混方法而制得所述的木塑复合材料。 The above-mentioned components, including plastics, plant fibers, plasticizers, stabilizers, lubricants and fillers, etc., are prepared by the general melt blending method in plastic processing to prepare the wood-plastic composite material. the
具体方法是先将植物纤维原料清除杂质、粉碎、过筛,在温度为80-100℃的条件下真空干燥2 h。将乙烯-乙烯醇共聚物粉碎成粉体后在90-92℃真空烘箱中干燥8 h。 The specific method is to first remove impurities from the plant fiber raw material, crush it, sieve it, and dry it under vacuum for 2 hours at a temperature of 80-100°C. The ethylene-vinyl alcohol copolymer was crushed into powder and dried in a vacuum oven at 90-92°C for 8 h. the
将上述组分按配比先进行预混,使用的设备为通常塑料加工中所用的混料设备,如高速混合机、捏合机等。预混时可以视物料情况适当加温,此混合温度一般应低于100℃。将预混后的物料使用通用的橡塑共混设备进行熔融共混,再经过挤出造粒等步骤而得到本发明所述的木塑复合材料。共混设备为橡塑加工业中的通用共混设备,可以是双螺杆挤出机、单螺杆挤出机及密炼机等,转速为30-60 r/min。 The above-mentioned components are pre-mixed according to the ratio, and the equipment used is the mixing equipment commonly used in plastic processing, such as high-speed mixers, kneaders, etc. When premixing, it can be heated appropriately according to the material condition, and the mixing temperature should generally be lower than 100°C. The pre-mixed materials are melt-blended using general-purpose rubber-plastic blending equipment, and then subjected to steps such as extrusion and granulation to obtain the wood-plastic composite material of the present invention. The blending equipment is a general blending equipment in the rubber and plastic processing industry, which can be a twin-screw extruder, a single-screw extruder, an internal mixer, etc., and the speed is 30-60 r/min. the
本发明的有益效果在于:(1)乙烯-乙烯醇共聚物中的乙烯醇结构单元可与植物纤维上的醇羟基和酚羟基产生良好的界面结合,无需另加界面相容剂。如果该技术得到大规模推广应用,可替代目前普遍使用的木塑复合材料改性方法,从而减轻因生产常规相容剂而带来的环境污染。因为商品化乙烯-乙烯醇共聚物是由具有严格环保措施的现代化大型化工企业生产,这与在一般塑料加工厂生产马来酸酐类接枝聚合物过程相比,环境污染小且便于集中治理。(2)乙烯-乙烯醇共聚物种类繁多,乙烯醇摩尔含量30-70 %,改性剂选择余地大。乙烯-乙烯醇共聚物分子结构中乙烯和乙烯醇两种结构单元的比例可调,这为种类繁多及填充量迥异的聚合物基植物纤维复合材料的制备提供了广泛的选择余地。(3)可直接处理植物纤维,操作方便,工艺简单,生产效率高,制品生产成本低。(4)乙烯-乙烯醇共聚物本身无毒,用其处理植物纤维过程中对环境无污染。乙烯-乙烯醇共聚物为大分子改性剂,在制品使用过程中不存在析出、迁移等污染和失效问题。 The beneficial effects of the present invention are: (1) The vinyl alcohol structural unit in the ethylene-vinyl alcohol copolymer can form a good interface bond with the alcoholic hydroxyl group and the phenolic hydroxyl group on the plant fiber, without additional interfacial compatibilizer. If this technology is popularized and applied on a large scale, it can replace the commonly used modification method of wood-plastic composite materials, thereby reducing the environmental pollution caused by the production of conventional compatibilizers. Because commercial ethylene-vinyl alcohol copolymers are produced by modern large-scale chemical companies with strict environmental protection measures, compared with the production of maleic anhydride graft polymers in general plastic processing plants, the environmental pollution is small and it is convenient for centralized management. (2) There are many kinds of ethylene-vinyl alcohol copolymers, the molar content of vinyl alcohol is 30-70%, and there is a large choice of modifiers. The proportion of ethylene and vinyl alcohol structural units in the molecular structure of ethylene-vinyl alcohol copolymer can be adjusted, which provides a wide range of options for the preparation of a wide variety of polymer-based plant fiber composites with different fillings. (3) Plant fibers can be directly processed, with convenient operation, simple process, high production efficiency and low product production cost. (4) Ethylene-vinyl alcohol copolymer itself is non-toxic, and it has no pollution to the environment during the process of treating plant fibers. Ethylene-vinyl alcohol copolymer is a macromolecular modifier, and there are no pollution and failure problems such as precipitation and migration during the use of the product. the
具体实施方式 Detailed ways
实施例1Example 1
原料组分按重量计为:高密度聚乙烯100份,乙烯-乙烯醇共聚物0.1份(乙烯摩尔含量为70%),甘油0.5份,木粉10份,抗氧剂1076 1份,抗氧剂330 2份,聚乙烯蜡1份,液体石蜡2份,碳酸钙20份。 The raw material components are by weight: 100 parts of high-density polyethylene, 0.1 part of ethylene-vinyl alcohol copolymer (the molar content of ethylene is 70%), 0.5 parts of glycerin, 10 parts of wood flour, 1 part of antioxidant 1076, 1 part of antioxidant 2 parts of agent 330, 1 part of polyethylene wax, 2 parts of liquid paraffin, 20 parts of calcium carbonate.
将木粉清除杂质、粉碎、过筛,在温度为80℃的条件下真空干燥2 h。同时将乙烯-乙烯醇共聚物粉碎后在92℃真空烘箱中干燥8 h。将干燥后的乙烯-乙烯醇共聚物粉体与甘油混合均匀后,对干燥后的木粉在150℃的高混机中以3000 r/min进行活化处理5 min,即得表面改性的木粉。然后在另一高混机中加入高密度聚乙烯、抗氧剂1076、抗氧剂330、聚乙烯蜡、液体石蜡、改性木粉和碳酸钙再混5min。取出混合料,投入双螺杆挤出机中,调节双螺杆挤出机螺杆转速为30 r/min,加料口到机头口模的温度依次为160,180,183,188,192,198,202℃,螺杆混炼后挤出拉条,经水冷、干燥、切粒即得聚烯烃基木塑复合材料。在注射成型机(一至三区温度依次为:180、190、200 ℃)制得木塑复合托盘,可用于食品级快餐盒或者托盘。 The wood flour was cleaned of impurities, crushed, sieved, and dried in vacuum at 80 °C for 2 h. At the same time, the ethylene-vinyl alcohol copolymer was pulverized and dried in a vacuum oven at 92 °C for 8 h. After mixing the dried ethylene-vinyl alcohol copolymer powder and glycerin evenly, the dried wood powder was activated in a high mixer at 150°C at 3000 r/min for 5 min to obtain surface-modified wood powder. pink. Then add high-density polyethylene, antioxidant 1076, antioxidant 330, polyethylene wax, liquid paraffin, modified wood powder and calcium carbonate into another high-mixer and mix for another 5 minutes. Take out the compound, put it into the twin-screw extruder, adjust the screw speed of the twin-screw extruder to 30 r/min, and the temperature from the feeding port to the die of the machine head is 160, 180, 183, 188, 192, 198, 202 ℃, extrude the strands after screw mixing, water cooling, drying, and pelletizing to obtain polyolefin-based wood-plastic composite materials. The wood-plastic composite tray is made in the injection molding machine (the temperature in the first to the third zone is: 180, 190, 200 ℃), which can be used for food-grade fast food boxes or trays. the
使用万能材料试验机测试所得复合材料的力学性能,拉伸强度为31.79 MPa,弯曲模量为3629 MPa。 The mechanical properties of the obtained composites were tested by a universal testing machine, the tensile strength was 31.79 MPa, and the flexural modulus was 3629 MPa. the
实施例2Example 2
原料组分按重量计为:聚氯乙烯100份,乙烯-乙烯醇共聚物3.6份(乙烯摩尔含量为30%),甘油18份,竹粉60份,复合热稳定剂5份,邻苯二甲酸辛十三酯5份,乙酰柠檬酸三丁酯5份,抗氧剂1010 3份,抗氧剂300 4份,硬脂酸正丁酯9份,油酰胺6份,二氧化硅10份。 The raw material components are by weight: 100 parts of polyvinyl chloride, 3.6 parts of ethylene-vinyl alcohol copolymer (the molar content of ethylene is 30%), 18 parts of glycerin, 60 parts of bamboo powder, 5 parts of composite heat stabilizer, phthalate 5 parts of octyl tridecyl formate, 5 parts of acetyl tributyl citrate, 3 parts of antioxidant 1010, 4 parts of antioxidant 300, 9 parts of n-butyl stearate, 6 parts of oleamide, 10 parts of silicon dioxide .
将竹粉清除杂质、粉碎、过筛,在温度为100℃的条件下真空干燥2 h。同时将乙烯-乙烯醇共聚物粉碎后在90℃真空烘箱中干燥8 h。将干燥后的乙烯-乙烯醇共聚物粉体与甘油混合均匀后,对干燥后的竹粉在190℃的高混机中以6000 r/min进行活化处理10 min,即得表面改性的竹粉。然后在另一高混机中加入聚氯乙烯、复合热稳定剂、邻苯二甲酸辛十三酯、乙酰柠檬酸三丁酯、抗氧剂1010、抗氧剂300、硬脂酸正丁酯、油酰胺、改性竹粉和二氧化硅以4000 r/min再混10 min。将混料倒入190℃的密炼机中在60 r/min下混合10 min,最后在190℃的平板硫化机上10 MPa下热压10 min后在室温下冷压15 min制得木塑复合板材,可用于天花板或地板。 Bamboo powder was cleaned of impurities, crushed, sieved, and vacuum-dried at 100 °C for 2 h. At the same time, the ethylene-vinyl alcohol copolymer was crushed and dried in a vacuum oven at 90 °C for 8 h. After mixing the dried ethylene-vinyl alcohol copolymer powder and glycerin evenly, the dried bamboo powder was activated in a high mixer at 190 °C at 6000 r/min for 10 min to obtain surface-modified bamboo powder. pink. Then add polyvinyl chloride, composite heat stabilizer, octyl tridecyl phthalate, acetyl tributyl citrate, antioxidant 1010, antioxidant 300, n-butyl stearate in another high mixer , oleamide, modified bamboo powder and silicon dioxide were mixed at 4000 r/min for another 10 min. Pour the mixture into an internal mixer at 190°C and mix at 60 r/min for 10 minutes, and finally hot press at 10 MPa on a flat vulcanizer at 190°C for 10 minutes and then cold press at room temperature for 15 minutes to obtain a wood-plastic composite. Panels, available for ceiling or floor. the
使用万能材料试验机测试所得复合材料的力学性能,拉伸强度为34.86 MPa,弯曲模量为4562MPa。 The mechanical properties of the obtained composite materials were tested by a universal testing machine, the tensile strength was 34.86 MPa, and the flexural modulus was 4562 MPa. the
实施例3Example 3
原料组分按重量计为:聚丙烯100份,乙烯-乙烯醇共聚物2.4份(乙烯摩尔含量为44%),甘油12份,麦秆40份,抗氧剂CA 3份,抗氧剂2246 2份,硬脂酸单甘油酯3份,有机硅烷6份,硅灰石10份。 The raw material components are by weight: 100 parts of polypropylene, 2.4 parts of ethylene-vinyl alcohol copolymer (the molar content of ethylene is 44%), 12 parts of glycerin, 40 parts of wheat straw, 3 parts of antioxidant CA, and 2246 parts of antioxidant 2 parts, 3 parts of monoglyceride stearate, 6 parts of organosilane, 10 parts of wollastonite.
将麦秆清除杂质、粉碎、过筛,在温度为80℃的条件下真空干燥2 h。同时将乙烯-乙烯醇共聚物粉碎后在91℃真空烘箱中干燥8h。将干燥后的乙烯-乙烯醇共聚物粉体与甘油混合均匀后,对干燥后的麦秆在175℃的高混机中以4500 r/min进行活化处理7 min,即得表面改性的麦秆。然后在另一高混机中加入聚丙烯、抗氧剂CA、抗氧剂2246、硬脂酸单甘油酯、有机硅烷、改性麦秆和硅灰石再混5min。取出混合料,投入双螺杆挤出机中,调节双螺杆挤出机螺杆转速为40 r/min,加料口到机头口模的温度依次为163,183,186,191,195,200,204℃,螺杆混炼后挤出、切粒即得改性木粉。将混料在单螺杆挤出机上(一至七区的温度依次为:165、185、188、192、196、201、205℃)中挤出制备木塑复合管材。 The wheat straw was cleaned of impurities, crushed, sieved, and vacuum-dried at 80 °C for 2 h. At the same time, the ethylene-vinyl alcohol copolymer was pulverized and dried in a vacuum oven at 91° C. for 8 hours. After mixing the dried ethylene-vinyl alcohol copolymer powder with glycerol evenly, the dried wheat straw was activated in a high-mixer at 175°C at 4500 r/min for 7 minutes to obtain the surface-modified wheat straw. stalk. Then add polypropylene, antioxidant CA, antioxidant 2246, monoglyceride stearate, organosilane, modified wheat straw and wollastonite to another high mixer and mix for another 5 minutes. Take out the compound, put it into the twin-screw extruder, adjust the screw speed of the twin-screw extruder to 40 r/min, and the temperature from the feeding port to the die of the machine head is 163, 183, 186, 191, 195, 200, 204 ℃, extrude and pelletize after screw mixing to obtain modified wood flour. Extrude the compounded material on a single-screw extruder (the temperatures of zones 1 to 7 are: 165, 185, 188, 192, 196, 201, 205°C) to prepare wood-plastic composite pipes. the
使用万能材料试验机测试所得复合材料的力学性能,拉伸强度为33.15 MPa,弯曲模量为4321 MPa。 The mechanical properties of the obtained composite materials were tested by a universal testing machine, the tensile strength was 33.15 MPa, and the flexural modulus was 4321 MPa. the
实施例4Example 4
原料组分按重量计为:乙烯-醋酸乙烯酯共聚物100份,乙烯-乙烯醇共聚物2.0份(乙烯摩尔含量为58%),甘油8份,糠壳粉50份,3份抗氧剂3114,3份抗氧剂300,云母10份,甘油三羟硬脂酸酯12份。 The raw material components are by weight: 100 parts of ethylene-vinyl acetate copolymer, 2.0 parts of ethylene-vinyl alcohol copolymer (the molar content of ethylene is 58%), 8 parts of glycerin, 50 parts of chaff powder, and 3 parts of antioxidant 3114, 3 parts of antioxidant 300, 10 parts of mica, 12 parts of glycerol trihydroxystearate.
将糠壳粉清除杂质、粉碎、过筛,在温度为80℃的条件下真空干燥2 h。同时将乙烯-乙烯醇共聚物粉碎后在92℃真空烘箱中干燥8h。将干燥后的乙烯-乙烯醇共聚物粉体与甘油混合均匀后,对干燥后的糠壳粉在170℃的高混机中以5000 r/min进行活化处理8 min,即得表面改性的糠壳粉。然后在另一高混机中加入聚丙烯、抗氧剂3114、抗氧剂300、甘油三羟硬脂酸酯、云母和改性糠壳粉再混5min。将混料倒入170℃的密炼机中在40 r/min下混合10 min,最后将混合物175℃的平板硫化机上10 MPa下热压10 min后在室温下冷压15 min制得木塑复合板材。 The chaff powder was cleaned of impurities, crushed, sieved, and dried in vacuum at 80°C for 2 h. At the same time, the ethylene-vinyl alcohol copolymer was pulverized and dried in a vacuum oven at 92° C. for 8 hours. After mixing the dried ethylene-vinyl alcohol copolymer powder and glycerin evenly, the dried bran shell powder was activated in a high mixer at 170°C at 5000 r/min for 8 minutes to obtain surface-modified Chaff powder. Then add polypropylene, antioxidant 3114, antioxidant 300, glycerol trihydroxystearate, mica and modified chaff powder into another high mixer and mix for another 5 minutes. Pour the mixture into an internal mixer at 170°C and mix it at 40 r/min for 10 minutes, and finally heat press the mixture on a flat vulcanizer at 175°C at 10 MPa for 10 minutes and then cold press it at room temperature for 15 minutes to obtain wood-plastic Composite panels. the
使用万能材料试验机测试所得复合材料的力学性能,拉伸强度为32.85 MPa,弯曲模量为4812MPa。 The mechanical properties of the obtained composite materials were tested by a universal testing machine, the tensile strength was 32.85 MPa, and the flexural modulus was 4812 MPa. the
对比例1Comparative example 1
原料组分按重量计为:乙烯-醋酸乙烯酯共聚物100份,甘油8份,糠壳粉50份,3份抗氧剂3114,3份抗氧剂300,云母10份,甘油三羟硬脂酸酯12份。 The raw material components are by weight: 100 parts of ethylene-vinyl acetate copolymer, 8 parts of glycerin, 50 parts of chaff powder, 3 parts of antioxidant 3114, 3 parts of antioxidant 300, 10 parts of mica, trihydroxyhard glycerin 12 parts of fatty acid ester.
将糠壳粉清除杂质、粉碎、过筛,在温度为80℃的条件下真空干燥2 h。同时将乙烯-乙烯醇共聚物粉碎后在92℃真空烘箱中干燥8h。将糠壳粉和甘油依次投入170℃的高混机中,以5000 r/min混合10 min后出料制得改性糠壳粉。然后在另一高混机中加入聚丙烯、抗氧剂3114、抗氧剂300、甘油三羟硬脂酸酯、云母和改性糠壳粉再混5min。将混料倒入170℃的密炼机中在40 r/min下混合10 min,最后在将混合物175℃的平板硫化机上10 MPa下热压10 min后在室温下冷压15 min制得木塑复合板材。 The chaff powder was cleaned of impurities, crushed, sieved, and dried in vacuum at 80°C for 2 h. At the same time, the ethylene-vinyl alcohol copolymer was pulverized and dried in a vacuum oven at 92° C. for 8 hours. Put chaff powder and glycerin into a high-speed mixer at 170°C in turn, mix at 5000 r/min for 10 min, and then discharge to obtain modified chaff powder. Then add polypropylene, antioxidant 3114, antioxidant 300, glycerol trihydroxystearate, mica and modified chaff powder into another high mixer and mix for another 5 minutes. Pour the mixture into an internal mixer at 170°C and mix it at 40 r/min for 10 minutes, and finally heat press the mixture at 10 MPa on a flat vulcanizer at 175°C for 10 minutes and then cold press it at room temperature for 15 minutes to obtain wood. Plastic composite panels. the
使用万能材料试验机测试所得复合材料的力学性能,拉伸强度为16.35 MPa,弯曲模量为1328MPa。 The mechanical properties of the obtained composite materials were tested by a universal testing machine, the tensile strength was 16.35 MPa, and the flexural modulus was 1328 MPa. the
以上所述仅为本发明的较佳实施例,凡依本发明申请专利范围所做的均等变化与修饰,皆应属本发明的涵盖范围。 The above descriptions are only preferred embodiments of the present invention, and all equivalent changes and modifications made according to the scope of the patent application of the present invention shall fall within the scope of the present invention. the
Claims (9)
Priority Applications (1)
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