WO2015000363A1 - Thermoplastic wood-plastic composite material and method for manufacture thereof - Google Patents
Thermoplastic wood-plastic composite material and method for manufacture thereof Download PDFInfo
- Publication number
- WO2015000363A1 WO2015000363A1 PCT/CN2014/080202 CN2014080202W WO2015000363A1 WO 2015000363 A1 WO2015000363 A1 WO 2015000363A1 CN 2014080202 W CN2014080202 W CN 2014080202W WO 2015000363 A1 WO2015000363 A1 WO 2015000363A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- plastic composite
- wood
- plastic
- biomass
- plant ash
- Prior art date
Links
- 229920001587 Wood-plastic composite Polymers 0.000 title claims abstract description 49
- 239000011155 wood-plastic composite Substances 0.000 title claims abstract description 49
- 239000000463 material Substances 0.000 title claims abstract description 47
- 229920001169 thermoplastic Polymers 0.000 title claims abstract description 47
- 239000004416 thermosoftening plastic Substances 0.000 title claims abstract description 47
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 27
- 239000002028 Biomass Substances 0.000 claims abstract description 76
- 239000000835 fiber Substances 0.000 claims abstract description 55
- 239000000203 mixture Substances 0.000 claims abstract description 38
- 229920003023 plastic Polymers 0.000 claims abstract description 36
- 239000004033 plastic Substances 0.000 claims abstract description 36
- 239000002245 particle Substances 0.000 claims abstract description 23
- 239000007822 coupling agent Substances 0.000 claims abstract description 15
- 238000002156 mixing Methods 0.000 claims abstract description 11
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 7
- 241000196324 Embryophyta Species 0.000 claims description 114
- 239000000843 powder Substances 0.000 claims description 59
- 239000002023 wood Substances 0.000 claims description 49
- 239000003921 oil Substances 0.000 claims description 28
- 239000010902 straw Substances 0.000 claims description 22
- 239000002699 waste material Substances 0.000 claims description 20
- 235000007164 Oryza sativa Nutrition 0.000 claims description 17
- 235000009566 rice Nutrition 0.000 claims description 17
- 238000001125 extrusion Methods 0.000 claims description 16
- 239000010903 husk Substances 0.000 claims description 15
- 229920001155 polypropylene Polymers 0.000 claims description 15
- 239000004800 polyvinyl chloride Substances 0.000 claims description 15
- 229920000915 polyvinyl chloride Polymers 0.000 claims description 15
- 239000004743 Polypropylene Substances 0.000 claims description 14
- 235000013312 flour Nutrition 0.000 claims description 14
- 238000005469 granulation Methods 0.000 claims description 14
- 230000003179 granulation Effects 0.000 claims description 14
- 239000008188 pellet Substances 0.000 claims description 14
- 239000004698 Polyethylene (PE) Substances 0.000 claims description 13
- 229920000573 polyethylene Polymers 0.000 claims description 13
- 239000000654 additive Substances 0.000 claims description 11
- 230000004048 modification Effects 0.000 claims description 9
- 238000006011 modification reaction Methods 0.000 claims description 9
- -1 polyethylene Polymers 0.000 claims description 9
- QIQXTHQIDYTFRH-UHFFFAOYSA-N Stearic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 8
- RTAQQCXQSZGOHL-UHFFFAOYSA-N titanium Chemical group [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 8
- 239000000314 lubricant Substances 0.000 claims description 7
- 239000003063 flame retardant Substances 0.000 claims description 5
- 235000021355 Stearic acid Nutrition 0.000 claims description 4
- 239000003086 colorant Substances 0.000 claims description 4
- 239000003999 initiator Substances 0.000 claims description 4
- 239000012188 paraffin wax Substances 0.000 claims description 4
- 239000008117 stearic acid Substances 0.000 claims description 4
- IQPQWNKOIGAROB-UHFFFAOYSA-N [N-]=C=O Chemical compound [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 claims description 3
- 239000003963 antioxidant agent Substances 0.000 claims description 3
- 159000000007 calcium salts Chemical class 0.000 claims description 3
- 239000004088 foaming agent Substances 0.000 claims description 3
- 239000003112 inhibitor Substances 0.000 claims description 3
- 230000002401 inhibitory effect Effects 0.000 claims description 3
- 150000003112 potassium compounds Chemical class 0.000 claims description 3
- BPQQTUXANYXVAA-UHFFFAOYSA-N silicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 3
- 239000003381 stabilizer Substances 0.000 claims description 3
- 230000003078 antioxidant Effects 0.000 claims description 2
- 230000004927 fusion Effects 0.000 claims description 2
- 240000007594 Oryza sativa Species 0.000 claims 1
- 238000011084 recovery Methods 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 22
- 241000209094 Oryza Species 0.000 description 16
- 238000001035 drying Methods 0.000 description 13
- 238000000034 method Methods 0.000 description 11
- 239000000047 product Substances 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 238000002791 soaking Methods 0.000 description 10
- 238000005452 bending Methods 0.000 description 9
- 239000001301 oxygen Substances 0.000 description 8
- 229910052760 oxygen Inorganic materials 0.000 description 8
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 8
- 239000002131 composite material Substances 0.000 description 6
- 239000000945 filler Substances 0.000 description 6
- 239000012467 final product Substances 0.000 description 6
- 239000003513 alkali Substances 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- 239000011159 matrix material Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 230000001965 increased Effects 0.000 description 3
- 238000001746 injection moulding Methods 0.000 description 3
- 230000001264 neutralization Effects 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000012075 bio-oil Substances 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000002708 enhancing Effects 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 229920001912 maleic anhydride grafted polyethylene Polymers 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 239000003607 modifier Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 238000004886 process control Methods 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 238000007873 sieving Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- WYTZZXDRDKSJID-UHFFFAOYSA-N (3-Aminopropyl)triethoxysilane Chemical compound CCO[Si](OCC)(OCC)CCCN WYTZZXDRDKSJID-UHFFFAOYSA-N 0.000 description 1
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 230000037408 Distribution ratio Effects 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- 235000009543 Silphium laciniatum Nutrition 0.000 description 1
- 240000003241 Silphium laciniatum Species 0.000 description 1
- LPXPTNMVRIOKMN-UHFFFAOYSA-M Sodium nitrite Chemical compound [Na+].[O-]N=O LPXPTNMVRIOKMN-UHFFFAOYSA-M 0.000 description 1
- 210000001138 Tears Anatomy 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000000996 additive Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive Effects 0.000 description 1
- 239000002154 agricultural waste Substances 0.000 description 1
- 230000000111 anti-oxidant Effects 0.000 description 1
- 230000003064 anti-oxidating Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000000903 blocking Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 235000019197 fats Nutrition 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N fumaric acid Chemical compound OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 238000009775 high-speed stirring Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 229920001911 maleic anhydride grafted polypropylene Polymers 0.000 description 1
- 230000003000 nontoxic Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 230000036961 partial Effects 0.000 description 1
- 239000001814 pectin Substances 0.000 description 1
- 229920001277 pectin Polymers 0.000 description 1
- 235000010987 pectin Nutrition 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000010908 plant waste Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000002829 reduced Effects 0.000 description 1
- 230000003014 reinforcing Effects 0.000 description 1
- 230000002441 reversible Effects 0.000 description 1
- 235000021003 saturated fats Nutrition 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000004642 transportation engineering Methods 0.000 description 1
- 239000003039 volatile agent Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L97/00—Compositions of lignin-containing materials
- C08L97/02—Lignocellulosic material, e.g. wood, straw or bagasse
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/04—Reinforcing macromolecular compounds with loose or coherent fibrous material
- C08J5/045—Reinforcing macromolecular compounds with loose or coherent fibrous material with vegetable or animal fibrous material
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/04—Reinforcing macromolecular compounds with loose or coherent fibrous material
- C08J5/06—Reinforcing macromolecular compounds with loose or coherent fibrous material using pretreated fibrous materials
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/04—Carbon
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/06—Polyethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/10—Homopolymers or copolymers of propene
- C08L23/12—Polypropene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
- C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L27/04—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
- C08L27/06—Homopolymers or copolymers of vinyl chloride
Abstract
Disclosed are a thermoplastic wood-plastic composite material and method for manufacture thereof. The components and weight percent of the material are as follows: 20-70 % plant fiber, 20-70 % plastics, 5-25 % biomass power plant ash or biomass oil mill ash, and 1-10 % auxiliary agent. The manufacturing method comprises: 1) pretreating the plant fiber, 2) modifying the plant fiber: modifying the surface of the plant fiber by using one or more of biomass power plant ash, biomass oil mill ash and coupling agent, 3) mixing: mixing the modified plant fiber, plastic particle, biomass power plant ash, or oil mill biomass ash, and auxiliary agent uniformly in ratio, 4) granulating: the mixture being plasticized at 110-180℃, extruded and granulated, 5) hot press forming: the granular being hot press formed to obtain thermoplastic wood-plastic composite material. The invention can achieve resources recovery and obtain a thermoplastic wood-plastic composite material having good mechanical performance and weatherability at the same time.
Description
热塑性木塑复合材料及其生产方法 Thermoplastic wood-plastic composite material and production method thereof
技术领域 Technical field
本发明涉及高分子复合材料, 具体地指一种热塑性木塑复合材料及其生产方法。 背景技术 The invention relates to a polymer composite material, in particular to a thermoplastic wood-plastic composite material and a production method thereof. Background technique
随着工业的发展, 大量废旧塑料和废弃粉灰对环境造成的污染越来越严重, 生物质 灰和废旧塑料被人们称为"黑白垃圾", 不仅严重影响了人们的生活质量, 而且制约了国 民经济的发展, 因此, 如何综合利用废旧塑料、 生物质电厂灰和生物质油厂灰渣, 使其 变废为宝已成为环境保护重要的课题之一。 With the development of industry, a large amount of waste plastics and waste ash have become more and more serious to the environment. Biomass ash and waste plastics are known as "black and white garbage", which not only seriously affects people's quality of life, but also restricts The development of the national economy, therefore, how to comprehensively use waste plastics, biomass power plant ash and biomass oil plant ash, making it a waste has become one of the important issues of environmental protection.
另外, 随着全球资源日趋枯竭, 社会环保意识的提高, 近年国内外对木材和石化产 品提出了更高要求, 在这样的背景下, 热塑性木塑复合材料应运而生, 热塑性木塑复合 材料是一类新型复合材料, 指利用聚乙烯、 聚丙烯和聚氯乙烯等代替通常的树脂胶粘剂 与废植物纤维混合, 再经挤压、模压、注射成型等塑料加工工艺, 生产出的板材或型材。 热塑性木塑复合材料克服了木材强度低、 变异性大及有机材料弹性模量低等造成的使用 局限性, 兼备木材与塑料的优点, 与木质材料相比, 其吸水率低, 不易变形开裂, 具有 较高机械性能, 可用于汽车, 建材, 家具, 及物流包装等行业, 市场应用前景广泛。 然 而, 热塑性木塑复合材料在使用环境及运输过程中往往需承受较高的冲击负荷, 而且湿 度、 温度、 光照, 及细菌等环境因素会对材料的物理性能及力学性能造成一定影响, 因 此, 如何不断提高热塑性木塑复合材料的力学性能和耐候性便成为热塑性木塑复合材料 发展过程中亟待解决的问题。 发明内容 In addition, with the increasing depletion of global resources and the improvement of social environmental awareness, in recent years, higher demands have been placed on wood and petrochemical products at home and abroad. In this context, thermoplastic wood-plastic composite materials have emerged. Thermoplastic wood-plastic composite materials are A new type of composite material refers to a sheet or profile produced by using polyethylene, polypropylene and polyvinyl chloride instead of the usual resin adhesive and waste plant fiber, and then being subjected to extrusion, molding, injection molding and other plastic processing techniques. Thermoplastic wood-plastic composite material overcomes the limitation of use caused by low strength, high variability and low elastic modulus of organic materials. It has the advantages of wood and plastic. Compared with wood materials, its water absorption rate is low and it is not easy to be deformed and cracked. With high mechanical properties, it can be used in industries such as automobiles, building materials, furniture, and logistics packaging. However, thermoplastic wood-plastic composites often have to withstand high impact loads during use and transportation, and environmental factors such as humidity, temperature, light, and bacteria have an impact on the physical and mechanical properties of the materials. How to continuously improve the mechanical properties and weather resistance of thermoplastic wood-plastic composite materials has become an urgent problem to be solved in the development of thermoplastic wood-plastic composite materials. Summary of the invention
本发明的目的就是要提供一种热塑性木塑复合材料及其生产方法, 实现废弃物资源 化的同时, 使得该热塑性木塑复合材料具有良好的力学性能和耐候性。 The object of the present invention is to provide a thermoplastic wood-plastic composite material and a production method thereof, which realizes the recycling of waste materials and makes the thermoplastic wood-plastic composite material have good mechanical properties and weather resistance.
为实现上述目的, 本发明采用的技术方案是: 一种热塑性木塑复合材料, 该材料的 组分及其重量百分比如下: In order to achieve the above object, the technical solution adopted by the present invention is: A thermoplastic wood-plastic composite material, the composition of which is as follows:
植物纤维 20〜70%;
塑料 20〜70% ; Plant fiber 20~70%; Plastic 20~70%;
生物质电厂灰渣或生物质油厂灰渣 5〜25%; Biomass power plant ash or biomass oil plant ash 5~25%;
助剂 1〜10%。 Additives 1~10%.
进一步地, 所述各组分的重量百分比如下: Further, the weight percentage of each component is as follows:
植物纤维 50〜65%; Plant fiber 50~65%;
塑料 20〜40%; Plastic 20~40%;
生物质电厂灰渣或生物质油厂灰渣 5〜10%; Biomass power plant ash or biomass oil plant ash 5~10%;
助剂 1〜10%。 Additives 1~10%.
进一步地, 所述各组分的重量百分比如下: Further, the weight percentage of each component is as follows:
植物纤维 35〜53%; Plant fiber 35~53%;
塑料 40〜45%; Plastic 40~45%;
生物质电厂灰渣或生物质油厂灰渣 5〜15%; Biomass power plant ash or biomass oil plant ash 5~15%;
助剂 1〜5%。 Additives 1 to 5%.
进一步地, 所述植物纤维与所述塑料的重量比为 9: 10。 Further, the weight ratio of the plant fiber to the plastic is 9:10.
进一步地, 所述生物质电厂灰渣或生物质油厂灰渣的主要成分为硅酸盐、 钙盐, 以 及钾的化合物, 其粒度为 1000〜5000 目, 长径比为 3〜6。 所述生物质电厂灰渣或生物 质油厂灰渣用作辅助填充料。 Further, the main components of the biomass power plant ash or biomass oil plant ash are silicate, calcium salt, and potassium compound, and have a particle size of 1000 to 5000 mesh and an aspect ratio of 3 to 6. The biomass power plant ash or biomass oil plant ash is used as an auxiliary filler.
进一步地, 所述植物纤维为木粉、 稻壳、 秸秆粉, 及林业三剩物粉中一种或几种任 意比例的组合。植物纤维用于提高材料的韧性, 拉伸性和防撕裂性; 植物纤维含量过低, 则韧性降低, 植物纤维含量过高, 则塑性变差, 材料生产过程中易堵死不能挤出。 Further, the plant fiber is a combination of one or more of wood flour, rice husk, straw powder, and forestry three remnant powder. Plant fiber is used to improve the toughness, stretchability and tear resistance of the material; if the plant fiber content is too low, the toughness is lowered, and if the plant fiber content is too high, the plasticity is deteriorated, and the material is easily blocked and cannot be extruded during the production process.
进一步地, 所述塑料为废旧的聚乙烯、 聚丙烯, 及聚氯乙烯中一种或几种任意比例 的组合。 塑料作为基体, 用于提高复合材料的热塑性。 Further, the plastic is a combination of one or more of any of waste polyethylene, polypropylene, and polyvinyl chloride. Plastic is used as a matrix to increase the thermoplastic properties of the composite.
进一步地, 所述助剂为偶联剂、 发泡剂、 引发剂、 抗氧化剂、 着色剂、 阻燃剂、 稳 定剂、 防霉剂, 及润滑剂中的一种或几种。 复合材料的生产过程中, 可根据需要添加适 当量的助剂。 Further, the auxiliary agent is one or more of a coupling agent, a foaming agent, an initiator, an antioxidant, a colorant, a flame retardant, a stabilizer, a mold inhibitor, and a lubricant. In the production process of the composite material, an appropriate amount of auxiliary agent may be added as needed.
上述热塑性木塑复合材料的生产方法, 包括以下步骤: The above method for producing a thermoplastic wood-plastic composite material comprises the following steps:
1 )植物纤维的预处理:将植物纤维粉碎并筛分出粒度为 80〜300目的颗粒后对其进 行干燥, 使植物纤维的含水率 < 5% ;
2) 植物纤维的改性处理: 用质量浓度为 3〜7%的生物质电厂灰渣溶液、 质量浓度 为 3〜7%的生物质油厂灰渣溶液,及占植物纤维重量 0.5%~3%的偶联剂中的一种或几种 对植物纤维表面进行改性处理; 1) Pretreatment of plant fiber: the plant fiber is pulverized and sieved to a particle size of 80 to 300 mesh, and then dried to make the water content of the plant fiber <5%; 2) Modification of plant fiber: Biomass power plant ash solution with mass concentration of 3~7%, biomass oil plant ash solution with mass concentration of 3~7%, and plant fiber weight 0.5%~3 One or more of the % coupling agents modify the surface of the plant fiber;
3 )混合: 将改性后的植物纤维, 塑料粒子, 生物质电厂灰渣或生物质油厂灰渣, 及 助剂按所述配比进行混合均匀, 备用; 3) mixing: mixing the modified plant fiber, plastic particles, biomass power plant ash or biomass oil plant ash, and auxiliaries according to the ratio, and reserve;
4) 造粒: 将混合物料在 110〜180°C下充分熔合塑化后挤出造粒; 4) granulation: the mixture is fully fused and plasticized at 110~180 ° C, and then extruded and granulated;
5 ) 热压成型: 将挤出造粒后的粒料用热压成型的方式制得热塑性木塑复合材料。 其中, 生物质电厂灰渣溶液或生物质油厂灰渣溶液与偶联剂处理相结合, 效果比单 独处理效果好。 5) Hot press forming: A thermoplastic wood-plastic composite material is obtained by hot press forming the pellets after extrusion granulation. Among them, the combination of biomass power plant ash solution or biomass oil plant ash solution and coupling agent treatment has better effect than single treatment.
所述步骤 2) 中, 所述偶联剂为钛酸酯、 硬脂酸、 石蜡、 异氰酸酯, 及马来酸配接 枝聚乙烯中的一种或几种任意比例的组合。 用偶联剂对植物纤维表面进行改性处理, 以 改善木塑界面相容性及混合均匀性, 偶联剂用量不能太多, 过剩反而会使材料的拉伸性 能和抗冲击性能下降, 当然, 量太少则包覆不完全, 影响处理效果; 其中, 钛酸酯本身 既是偶联剂, 也是分散剂, 润滑剂, 粘合剂, 交联剂, 催化剂, 还兼具防锈, 抗氧化和 阻燃等多种功能。 In the step 2), the coupling agent is a combination of one or more of titanate, stearic acid, paraffin, isocyanate, and maleic acid grafted polyethylene. The surface of the plant fiber is modified with a coupling agent to improve the compatibility of the wood-plastic interface and the mixing uniformity. The amount of the coupling agent should not be too much, and the excess may cause the tensile properties and impact resistance of the material to decrease. If the amount is too small, the coating is incomplete, which affects the treatment effect; wherein, the titanate itself is not only a coupling agent but also a dispersant, a lubricant, a binder, a crosslinking agent, a catalyst, and also has anti-rust and anti-oxidation. And a variety of functions such as flame retardant.
所述步骤 4)中, 先采用双螺杆塑料挤出机进行熔合塑化, 温度设定为 110〜170°C, 然后再采用单螺杆挤出机挤出造粒, 单螺杆机头温度控制为 115〜180°C, 控制挤出压力 为 7〜12MPa。 在挤出工艺控制方面, 根据废旧塑料的熔融和分解温度、 以及植物纤维 所能承受的温度范围进行设定各料筒区温度值,双螺杆挤出机的温度设定从 110~170°C, 并且在整个生产过程中保持其不变; 单螺杆机头的温度控制 115~180°C温度范围内, 并 保持较高的熔体压力。 另外, 为防止温度过高, 出现纤维烧焦现象, 不同塑料的温度设 定也有一定区别, 优选双螺杆挤出机选用 PE 时温度优选设定为 110~120°C, PP 优选 140~150°C , PVC优选 150~170°C ; 单螺杆挤出机选用 PE时温度优选设定为 115~125°C, PP为 170~180°C, PVC为 165~178°C。 同时, 视挤出过程中出现的实际问题及时调整温 度, 螺杆转速, 喂料速度, 牵引速率等主要工艺参数。 In the step 4), the twin-screw plastic extruder is first used for fusion plasticization, the temperature is set to 110~170 ° C, and then the single-screw extruder is used for extrusion granulation, and the temperature of the single-screw head is controlled to 115 to 180 ° C, the extrusion pressure is controlled to 7 to 12 MPa. In the extrusion process control, the temperature of each barrel is set according to the melting and decomposition temperature of the waste plastic and the temperature range that the plant fiber can withstand. The temperature of the twin-screw extruder is set from 110 to 170 °C. And keep it unchanged throughout the production process; the temperature of the single screw head is controlled within the temperature range of 115~180 °C, and maintains a high melt pressure. In addition, in order to prevent the temperature from being too high, the phenomenon of fiber charring occurs, and the temperature setting of different plastics is also different. It is preferable to set the temperature of the twin-screw extruder to be 110 to 120 ° C, and the PP to be 140 to 150 °. C, PVC is preferably 150~170°C; when the single screw extruder is used, the temperature is preferably set to 115~125°C, PP is 170~180°C, and PVC is 165~178°C. At the same time, depending on the actual problems occurring during the extrusion process, the main process parameters such as temperature, screw speed, feed speed and traction rate are adjusted in time.
所述步骤 1 ) 中, 粉碎筛分后的植物纤维粒度为 80〜 120目。 In the step 1), the plant fiber size after pulverization and sieving is 80 to 120 mesh.
与现有木塑材料相比, 本发明具有如下优点: Compared with the existing wood plastic materials, the present invention has the following advantages:
其一, 本发明以聚乙烯 (PE), 聚丙烯 (PP), 或聚氯乙烯 (PVC) 等废旧塑料为基体树
脂, 以木粉, 稻壳, 或秸秆等废弃植物纤维为填料, 以生物质电厂灰渣或生物质油厂灰 渣为辅助填料生产热塑性木塑复合材料, 生物质电厂灰渣或生物质油厂灰渣特殊的颗粒 结构和粒径范围,使其成为木塑复合材料的极好辅助填充料,与植物纤维填充料相配合, 一起提高了材料的韧性。 First, the present invention is based on waste plastics such as polyethylene (PE), polypropylene (PP), or polyvinyl chloride (PVC). Fat, using waste plant fiber such as wood flour, rice husk, or straw as filler, and producing thermoplastic wood-plastic composite material, biomass power plant ash or biomass oil with biomass power plant ash or biomass oil plant ash as auxiliary filler. The special particle structure and particle size range of the plant ash slag make it an excellent auxiliary filler for wood-plastic composites, which cooperates with the plant fiber filler to improve the toughness of the material.
其二, 生物质电厂灰渣或生物质油厂灰渣的溶液为碱性溶液, 用作植物纤维的改性 剂, 能对纤维素碱化处理, 有利于植物纤维改性; 并能对植物纤维中的杂质小分子进行 溶解, 使植物纤维中的部分果胶、 木质素和半纤维素等低分子杂质被溶解除去, 使得植 物纤维表面变得粗糙, 使植物纤维与塑料粒子界面之间结合能力增强; 能打开植物纤维 表面的氢键, 使纤维表面变得疏松, 形成许多空腔, 这些空腔增强聚合物母体与植物纤 维填料的"锁紧力"; 该碱性溶液中既有极性离子又有非极性离子, 可以对极性植物纤维 和非极性聚合物母体的结合起到偶联剂作用, 使得最终生产出的热塑性木塑复合材料具 有良好的抗压、 抗弯、 耐冲击等力学性能和物理性能, 且具有很好的耐水性, 不易被虫 蛀, 不易长真菌, 耐酸碱和抗腐蚀性强, 使用寿命长。 Second, the solution of biomass power plant ash or biomass oil plant ash is an alkaline solution, used as a modifier of plant fiber, can alkalize cellulose, and is beneficial to plant fiber modification; Small molecules of impurities in the fiber are dissolved, so that some of the low-molecular impurities such as pectin, lignin and hemicellulose in the plant fiber are dissolved and removed, so that the surface of the plant fiber becomes rough, and the interface between the plant fiber and the plastic particle interface is combined. The ability to enhance the hydrogen bond on the surface of the plant fiber, loosening the surface of the fiber, forming a number of cavities that enhance the "locking force" of the polymer matrix and the plant fiber filler; the alkaline solution has both poles The ions also have non-polar ions, which can act as a coupling agent for the combination of polar plant fibers and non-polar polymer matrix, so that the finally produced thermoplastic wood-plastic composite material has good compression resistance, bending resistance, It has mechanical properties and physical properties such as impact resistance, and has good water resistance, is not easy to be infected by insects, is not prone to long fungi, and is resistant to acid and alkali and corrosion. Long.
其三, 生物质电厂灰渣内含硅和钙, 可起到补强剂和润滑剂的作用; 生物质油厂灰 渣含饱和脂肪垸基烃, 可提高材料的蓄热保温功能; 生物质电厂灰渣具有多孔结构, 可 以吸附有害气体, 进而生产出的木塑复合材料无毒, 无污染, 无辐射, 可以 100%回收 再生, 符合环保要求。 Third, the biomass power plant ash contains silicon and calcium, which can act as a reinforcing agent and lubricant; the biomass oil plant ash contains saturated fat sulfhydryl hydrocarbon, which can improve the heat storage and heat preservation function of the material; The power plant ash has a porous structure, which can absorb harmful gases, and the wood-plastic composite material produced is non-toxic, non-polluting, non-radiative, and can be recycled 100%, which meets environmental protection requirements.
其四, 本发明用废旧塑料粒子作为基体树脂, 通过设计合理配比, 是的生产出的热 塑性木塑复合材料可用性强, 可锯、 刨、 钉, 根据需要制作出各种规格产品, 产品的局 部损坏可维修再造。 Fourthly, the invention uses waste plastic particles as a matrix resin, and by designing a reasonable ratio, the thermoplastic wood-plastic composite material produced is highly usable, can be sawed, planed, nailed, and can be manufactured according to requirements. Partial damage can be repaired and rebuilt.
其五, 本发明利用植物纤维, 废旧塑料, 生物质电厂灰渣或生物质油厂灰渣这些廉 价原材料, 通过选择合理组分配比和添加相关助剂, 生产出一种可逆性循环利用优质代 木型材, 实现废弃物资源化而取得显著经济效益的同时, 也大幅减少了废弃物带来的环 境污染, 提高了木塑材料的附加值。 Fifth, the invention utilizes low-cost raw materials such as plant fiber, waste plastic, biomass power plant ash or biomass oil plant ash, and produces a reversible recycling quality by selecting a reasonable group distribution ratio and adding related additives. Wood profiles, while achieving waste resources and achieving significant economic benefits, have also significantly reduced environmental pollution caused by waste and increased the added value of wood-plastic materials.
其六, 本发明的生产方法中, 除利用前述碱性溶液和偶联剂对植物纤维表面进行了 改性处理, 有效改善了木塑界面相容性及混合均匀性外, 还在挤出工艺控制方面, 根据 原料性质优化工艺参数, 避免了烧焦现象和堵死现象。
附图说明 Sixth, in the production method of the present invention, in addition to modifying the surface of the plant fiber by using the alkaline solution and the coupling agent, the compatibility of the wood-plastic interface and the mixing uniformity are effectively improved, and the extrusion process is also performed. In terms of control, the process parameters are optimized according to the nature of the raw materials, avoiding charring and blocking. DRAWINGS
图 1为一种热塑性木塑复合材料的生产流程示意图。 Figure 1 is a schematic view showing the production process of a thermoplastic wood-plastic composite material.
图 2为生物质油厂灰渣的扫描电镜照片。 Figure 2 is a scanning electron micrograph of the ash of the biomass oil plant.
图 3为生物质电厂灰渣的扫描电镜照片。 具体实施方式 Figure 3 is a scanning electron micrograph of the biomass power plant ash. detailed description
以下结合附图和具体实施例对本发明作进一步的说明, 但是本发明并不限于下述实 施例。 The present invention will be further described below in conjunction with the drawings and specific embodiments, but the invention is not limited to the embodiments described below.
一种热塑性木塑复合材料的生产过程总体上如图 1所示, 首先将废木料, 稻壳或秸 秆等植物纤维用粉碎机进行粉碎, 并用电厂蒸汽余热进行干燥使其含水率 <5%; 然后加 入改性剂对植物纤维进行表面改性处理, 并按配比将改性后的植物纤维, 生物质电厂灰 渣或生物质油厂灰渣, 塑料粒子 (PE、 PP、 PVC), 及适量的助剂放入混合机中混匀; 接着, 用双螺杆挤出机和单螺杆挤出机挤压造粒, 挤出机加工热能也可利用生物质电厂 蒸汽余热; 最后通过模具成型制得型材, 包装产品完成整个生产过程。 The production process of a thermoplastic wood-plastic composite material is generally as shown in Fig. 1. First, the plant fibers such as waste wood, rice husk or straw are pulverized by a pulverizer, and dried by steam heat of the power plant to make the water content <5%; Then, the surface modification of the plant fiber is carried out by adding a modifier, and the modified plant fiber, the biomass power plant ash or the biomass oil plant ash, the plastic particles (PE, PP, PVC), and the appropriate amount are added according to the ratio. The auxiliaries are mixed in a mixer; then, the granulation is performed by a twin-screw extruder and a single-screw extruder, and the heat energy of the extruder can also utilize the waste heat of the biomass power plant; Profiles, packaging products complete the entire production process.
其中, 生物质电厂灰渣或生物质油厂灰渣的主要成分为硅酸盐、 钙盐, 以及钾的化 合物, 其粒度为 1000〜5000 目, 长径比为 3〜6, 通常长径比在 5左右, 生物质油厂灰 渣的形貌和结构如图 2所示, 生物质电厂灰渣的形貌和结构如图 3所示。 Among them, the main components of biomass power plant ash or biomass oil plant ash are silicate, calcium salt, and potassium compound, the particle size is 1000~5000 mesh, the aspect ratio is 3~6, usually the aspect ratio At about 5, the morphology and structure of the ash and slag of the biomass oil plant are shown in Figure 2. The morphology and structure of the biomass ash slag are shown in Figure 3.
实施例 1 Example 1
热塑性木塑复合材料的组分及其重量百分含量如下: 木粉 70%, PE20%, 生物质电 厂灰渣 9%, 助剂 1%。 The composition of the thermoplastic wood-plastic composite and its weight percentage are as follows: wood powder 70%, PE 20%, biomass power plant ash 9%, auxiliary 1%.
具体生产过程如下: The specific production process is as follows:
1)对木粉进行预处理 1) Pretreatment of wood flour
用粉碎机粉碎后用标准筛筛出 80目的木粉,然后将其放于恒温鼓风干燥室连续干燥 4-7 小时, 干燥温度控制在 105°C, 干燥过程中定时对木粉进行称重, 直到两次称重结 果基本相等时结束干燥, 取出木粉置于密封袋中备用。 After pulverizing with a pulverizer, the 80-mesh wood powder is sieved with a standard sieve, and then it is continuously dried in a constant temperature blast drying chamber for 4-7 hours, the drying temperature is controlled at 105 ° C, and the wood powder is regularly weighed during the drying process. , until the two weighing results are basically equal, the drying is finished, and the wood powder is taken out and placed in a sealed bag for use.
2)对木粉进行改性处理 2) Modification of wood flour
a、 碱溶液处理木粉: 用质量浓度为 4%的生物质电厂灰溶液作为浸泡液, 用量以刚 好浸没木粉为宜, 浸泡时间为 48小时, 然后用水将木粉洗呈中性后抽滤并烘干;
b、 用钛酸酯处理木粉: 将木粉放入 105°C的恒温鼓风干燥室干燥 5小时, 将干燥后 的木粉放入高速混合机中搅拌, 温度升高到 90°C, 称取占木粉重量 0.5%的钛酸酯放入 高混机中, 当温度升高到 10CTC放出, 冷却备用。 a. Alkali solution treatment of wood powder: Use 4% mass concentration of biomass power plant ash solution as soaking liquid, the amount should be just immersed in wood powder, soaking time is 48 hours, then wash the wood powder with neutral water and then pump Filter and dry; b. Treating wood powder with titanate: The wood powder is placed in a constant temperature blast drying chamber at 105 ° C for 5 hours, and the dried wood powder is placed in a high-speed mixer and stirred, and the temperature is raised to 90 ° C. The titanate, which accounts for 0.5% of the weight of the wood flour, is weighed into a high-mixer. When the temperature rises to 10 CTC, it is cooled and ready for use.
3 ) 将在 105°C下干燥 5h后的生物质电厂灰渣 (KD-1 ) 与改性后的木粉, PE粒子, 及抗氧化剂和阻燃剂等助剂按配比一起放入混合机中以 1200 r/min的转速混合均匀。 3) The biomass power plant ash (KD-1) after drying at 105 °C for 5 hours is added to the mixer together with the modified wood powder, PE particles, and antioxidants and flame retardants. Mix well at 1200 r/mi n .
4)将混合料放入平行双螺杆挤出机内进行塑化造粒,然后再进入单螺杆挤出机挤出, 粒料在挤出机内被混合均化。 在挤出工艺控制方面, 根据 PE 的熔融和分解温度, 以及 木粉所能承受的温度范围进行设定各料筒区温度值, 双螺杆挤出机的温度设定为 115°C, 并且在整个生产过程中保持恒定; 单螺杆机头的温度控制 12CTC温度范围内, 保持了较 高的熔体压力, 同时视挤出过程中出现的具体问题可适当调整设备的工艺参数。 4) The mixture is placed in a parallel twin-screw extruder for plasticizing and granulation, and then extruded into a single-screw extruder, and the pellets are mixed and homogenized in the extruder. In the extrusion process control, the temperature of each barrel is set according to the melting and decomposition temperature of PE and the temperature range that the wood powder can withstand. The temperature of the twin-screw extruder is set to 115 ° C, and It is kept constant throughout the production process; the temperature of the single screw head is controlled within the temperature range of 12CTC, and the higher melt pressure is maintained. At the same time, the process parameters of the equipment can be appropriately adjusted depending on the specific problems occurring during the extrusion process.
5) 将挤出的粒料通过模具部件的几何形状成型, 生产出最终产品。 5) The extruded pellets are shaped by the geometry of the mold part to produce the final product.
经检测, 本产品的抗压强度达 30MPa, 抗弯曲强度达 20MPa, 抗弯模量达 500MPa, 断裂伸长率为 150%, 氧指数 >25, 使用温度为 -10°C〜85°C, 力学性能和耐候性优良。 After testing, the product has a compressive strength of 30MPa, a bending strength of 20MPa, a flexural modulus of 500MPa, an elongation at break of 150%, an oxygen index of >25, and a use temperature of -10°C to 85°C. Excellent mechanical properties and weather resistance.
实施例 2 Example 2
热塑性木塑复合材料的组分及其重量百分含量如下: 稻壳 45%, PP 45%, 生物质电 厂灰渣 (KD-1)5%, 助剂 5%。 The composition of the thermoplastic wood-plastic composite and its weight percentage are as follows: rice husk 45%, PP 45%, biomass power plant ash (KD-1) 5%, auxiliaries 5%.
具体生产过程如下: The specific production process is as follows:
1 )将稻壳粉碎后筛分出粒度为 100目的粒料放入蒸汽室中干燥,在 105°C下干燥 4h; 1) crushing the rice husk, sieving the granules with a particle size of 100 mesh into a steam chamber, drying, and drying at 105 ° C for 4 h;
2) 将占稻壳重量 2%的氨丙基三乙氧基硅垸偶联剂 (KH550)与乙醇按 1:1的比例混 合均匀, 加入到稻壳中, 在高速混合机中混合 30min; 2) Mix the aminopropyltriethoxysilane coupling agent (KH550), which accounts for 2% of the rice hull weight, with ethanol in a ratio of 1:1, add to the rice husk, and mix in a high-speed mixer for 30 min ;
3 )将上述改性后的稻壳, 生物质电厂灰渣(KD-1 ), PP, 及引发剂和着色剂等助剂 按配比加入到高速混合机中混合 lOmin出料, 并在 105°C下干燥 4h; 3) The above modified rice husk, biomass power plant ash (KD-1), PP, and initiators and colorants are added to the high-speed mixer for mixing for 10 min, and at 105 °. Drying for 4 hours under C;
4)将混合料放入平行双螺杆挤出机内进行塑化造粒,然后将混合料在单螺杆挤出机 中进行挤出造粒,单螺杆挤出机模头温度为 16CTC,螺杆加热区温度依次为 170°C、175°C、 170°C , 螺杆转速为 40r/min, 并通冷却水进行冷却; 4) The mixture is placed in a parallel twin-screw extruder for plasticizing and granulating, and then the mixture is subjected to extrusion granulation in a single-screw extruder. The temperature of the single-screw extruder is 16 CTC, and the screw is heated. The temperature of the zone is 170 ° C, 175 ° C, 170 ° C, the screw speed is 40 r / min, and is cooled by cooling water;
5) 将挤出的粒料通过模具部件的几何形状成型, 生产出最终产品。 5) The extruded pellets are shaped by the geometry of the mold part to produce the final product.
在上述过程中, 由于稻壳和生物质电厂灰(KD-1 )的存在, 使得混合料的体积膨胀, 结构疏松, 为了保证下料的连续性, 可采用增大加料量的方式避免挤出过程中板材或者
异性材料内部疏松影响致密性; 在成型过程中, 要严格控制模具温度, 并通冷却水环绕 板材界面进行冷却, 从而使板材各个面温度一致, 避免出现收缩率不一样的情况, 使得 板材或者异性材翘曲等情况, 影响使用和美观。 In the above process, due to the presence of rice husk and biomass power plant ash (KD-1), the volume of the mixture is expanded and the structure is loose. In order to ensure the continuity of the material, the amount of feed can be increased to avoid extrusion. In process plate or The internal looseness of the heterogeneous material affects the compactness; during the molding process, the temperature of the mold is strictly controlled, and the cooling water is cooled around the interface of the sheet, so that the temperature of each surface of the sheet is uniform, and the shrinkage rate is not uniform, so that the sheet or the opposite sex is caused. Warpage and other conditions affect the use and aesthetics.
产品抗压强度达 25MPa, 抗弯曲强度达 20MPa, 抗弯模量达 500MPa, 断裂伸长率 为 150%, 氧指数 >25, 使用温度 -10°C〜85°C, 力学性能和耐候性优良。 The product has a compressive strength of 25MPa, a bending strength of 20MPa, a flexural modulus of 500MPa, an elongation at break of 150%, an oxygen index of >25, a use temperature of -10°C to 85°C, excellent mechanical properties and weather resistance. .
实施例 3 Example 3
热塑性木塑复合材料的组分及其重量百分含量如下: 秸秆粉 20%, PVC 70% , 生物 质油厂灰渣 (KD-2)8%, 助剂 2%。 The composition of the thermoplastic wood-plastic composite and its weight percentage are as follows: straw powder 20%, PVC 70%, biomass oil plant ash (KD-2) 8%, and auxiliary 2%.
具体生产过程如下: The specific production process is as follows:
1 )将秸秆粉碎筛分出出粒度为 80目的粉料,然后将秸秆粉放入干燥箱中,在 105°C 下干燥 2h; 1) crushing the straw and sifting out the powder with a particle size of 80 mesh, and then putting the straw powder into a dry box and drying at 105 ° C for 2 hours;
2) 将占秸秆粉重量 3%的马来酸酐接枝聚丙烯和钛酸酯偶联剂加入到秸秆粉中, 在 高速混合机中以 80°C搅拌 15min, 进行改性处理; 2) adding maleic anhydride grafted polypropylene and titanate coupling agent, which accounts for 3% by weight of straw powder, to the straw powder, and stirring at 80 ° C for 15 min in a high speed mixer for modification;
3 ) 将改性后的秸秆粉, 生物油厂灰渣 (KD-2), PVC 及白炭黑等助剂, 按配比加入 到高速混合机中混合, 在 60°C下搅拌 30min; 3) Adding modified straw powder, bio-oil ash (KD-2), PVC and white carbon black into the high-speed mixer according to the ratio, and stirring at 60 ° C for 30 min;
4) 用双螺杆挤出机在 17CTC制得粒料; 4) pellets were produced at 17 CTC using a twin-screw extruder;
5 ) 用注塑机制备出复合材料的力学样条产品。 5) The mechanical spline product of the composite material is prepared by an injection molding machine.
产品抗压强度达 25MPa, 抗弯曲强度达 18MPa, 抗弯模量达 600MPa, 断裂伸长率 为 150%, 氧指数 >25, 使用温度 -10°C~85°C, 力学性能和耐候性能优良。 The product has a compressive strength of 25MPa, a bending strength of 18MPa, a flexural modulus of 600MPa, an elongation at break of 150%, an oxygen index of >25, a use temperature of -10°C to 85°C, excellent mechanical properties and weather resistance. .
实施例 4 Example 4
热塑性木塑复合材料的组分及其重量百分含量如下: 60%的秸秆粉和林业三剩物粉, 30%的 PVC禾口 PP, 5%的生物质油厂灰渣 (KD-2), 助剂 5%。 The components of the thermoplastic wood-plastic composite and its weight percentage are as follows: 60% straw powder and forestry three residual powder, 30% PVC and PP, 5% biomass oil plant ash (KD-2) , 5% additives.
具体生产过程如下: The specific production process is as follows:
1 ) 将秸秆和林业三剩物研磨制成粒度为 120 目的粉末后进行干燥, 使其含水率 < 1) Grinding the straw and forestry three residues into a powder with a particle size of 120 mesh, and drying it to make the water content <
5%; 5%;
2)将烘干后的秸秆粉和林业三剩物粉放入高混机中高速搅拌, 当温度达到 90°C时, 称取占粉料重量 1.5%的异氰酸酯,用 95%的乙醇稀释后用喷壶均匀喷到粉料中, 当温度 升高到 10CTC时放出, 烘干备用;
3 ) 将改性后的料粉, 生物油厂灰渣 (KD-2), PVC和 PP, 及润滑剂等助剂, 按配比 加入到高速混合机中混合, 在 60°C下搅拌 30min; 2) The dried straw powder and the forestry three residue powder are placed in a high-mixer for high-speed stirring. When the temperature reaches 90 °C, the isocyanate is 1.5% by weight of the powder, and diluted with 95% ethanol. Spray evenly into the powder with a watering can, release it when the temperature rises to 10CTC, and dry for use; 3) The modified powder, bio-oil ash (KD-2), PVC and PP, and lubricants are added to the high-speed mixer according to the ratio, and stirred at 60 ° C for 30 min;
4)将混合料放入双螺杆挤出机内进行塑化造粒,然后将混合料在单螺杆挤出机内以 17CTC进行混炼挤出, 挤出压力控制在 7~12MPa, 挤出料降温后磨面切粒; 4) The mixture is placed in a twin-screw extruder for plasticizing and granulation, and then the mixture is kneaded and extruded at 17 CTC in a single-screw extruder, and the extrusion pressure is controlled at 7 to 12 MPa. Grinding surface granulation after cooling;
5) 将挤出的粒料通过热压成型的方式生产出最终产品。 5) The extruded pellets are produced by hot press forming to produce the final product.
产品的抗压强度达 40MPa, 抗弯曲强度达 18MPa, 抗弯模量达 400MPa, 断裂伸长 率 150%, 氧指数 >25, 使用温度 -10°C〜85°C, 力学性能和耐候性能优良。 The product has a compressive strength of 40MPa, a bending strength of 18MPa, a flexural modulus of 400MPa, an elongation at break of 150%, an oxygen index of >25, a use temperature of -10°C to 85°C, excellent mechanical properties and weather resistance. .
实施例 5 Example 5
热塑性木塑复合材料的组分及其重量百分含量如下: 秸秆粉 20%, PVC 50%, 生物 质电厂灰渣 (KD- 1)25%, 助剂 5%。 The composition of the thermoplastic wood-plastic composite and its weight percentage are as follows: straw powder 20%, PVC 50%, biomass power plant ash (KD-1) 25%, auxiliaries 5%.
具体生产过程如下: The specific production process is as follows:
1 )将秸秆粉碎筛分出粒度为 300目的粉料, 然后将秸秆粉放入干燥箱中, 在 105°C 下干燥 2h; 1) crushing the straw into a powder having a particle size of 300 mesh, and then placing the straw powder in a dry box and drying at 105 ° C for 2 hours;
2)用质量浓度为 5%的生物质油厂灰溶液作为浸泡液,用量以刚好浸没秸秆粉为宜, 浸泡时间为 48小时, 然后用水将秸秆粉洗呈中性后抽滤并烘干; 2) Using a biomass oil plant ash solution with a mass concentration of 5% as the soaking solution, the amount is just to soak the straw powder, the soaking time is 48 hours, then the straw powder is washed with water to be neutral, then filtered and dried;
并用钛酸酯、 硬脂酸、 石蜡共同处理秸秆粉: 把秸秆粉放在高混机中高温搅拌, 当 温度达到 90°C时加入占秸秆粉重量 0.8%的钛酸酯, 硬脂酸和石蜡, 混合 10分钟左右放 出, 冷却备用。 The straw powder is treated together with titanate, stearic acid and paraffin: the straw powder is placed in a high-mixing machine and stirred at a high temperature. When the temperature reaches 90 ° C, the titanate, stearic acid and 0.8% of the weight of the straw powder are added. Paraffin, mix and release for about 10 minutes, cool and set aside.
3 ) 将改性后的秸秆粉, 生物质电厂灰渣 (KD-1), PVC, 及防霉剂和阻燃剂等助剂, 按配比加入到高速混合机中混合, 在 60°C下搅拌 30min; 3) Adding modified straw powder, biomass power plant ash (KD-1), PVC, and anti-mold agent and flame retardant to the high-speed mixer according to the ratio, at 60 ° C Stir for 30min;
4) 用双螺杆挤出机和单螺杆挤出机制得粒料; 4) obtaining pellets by a twin-screw extruder and a single-screw extrusion mechanism;
5) 用注塑机生产出成型的复合材料。 5) The molded composite material is produced by an injection molding machine.
产品抗压强度达 40MPa,抗弯曲强度达 19MPa,抗弯模量达 450MPa,断裂伸长率为 150%, 氧指数 >25, 使用温度 -10°C~85°C, 力学性能和耐候性能优良。 The product has a compressive strength of 40MPa, a bending strength of 19MPa, a flexural modulus of 450MPa, an elongation at break of 150%, an oxygen index of >25, a use temperature of -10°C to 85°C, excellent mechanical properties and weather resistance. .
实施例 6 Example 6
热塑性木塑复合材料的组分及其重量百分含量如下: 木粉 50%, PP 30%, 生物质电 厂灰渣 (KD-1)10%, 助剂 10%。 The composition of the thermoplastic wood-plastic composite and its weight percentage are as follows: wood powder 50%, PP 30%, biomass power plant ash (KD-1) 10%, additive 10%.
具体生产过程如下:
1)对木粉进行预处理 The specific production process is as follows: 1) Pretreatment of wood flour
2)对木粉进行改性处理 2) Modification of wood flour
碱溶液处理木粉: 用质量浓度为 7%的生物质电厂灰溶液作为浸泡液, 用量以刚好浸 没木粉为宜, 浸泡时间为 48小时, 然后用水将木粉洗呈中性后抽滤并烘干; Alkali solution treatment of wood powder: Use 7% of biomass ash solution as the soaking solution, the amount should be just immersed in wood powder, soaking time is 48 hours, then wash the wood powder with neutrality with water and then filter Drying
3 ) 将干燥后的生物质电厂灰渣 (KD-1 ) 与改性后的木粉, PP粒子, 及着色剂和稳 定剂等助剂按配比一起放入混合机中混合均匀。 3) Put the dried biomass power plant ash (KD-1) with the modified wood powder, PP particles, and the additives such as coloring agents and stabilizers into the mixer and mix them evenly.
4)将混合料放入平行双螺杆挤出机内进行塑化造粒,然后再进入单螺杆挤出机挤出, 粒料在挤出机内被混合均化。 4) The mixture is placed in a parallel twin-screw extruder for plasticizing and granulation, and then extruded into a single-screw extruder, and the pellets are mixed and homogenized in the extruder.
5) 将挤出的粒料通过模具部件的几何形状成型, 生产出最终产品。 5) The extruded pellets are shaped by the geometry of the mold part to produce the final product.
经检测, 本产品的抗压强度达 35MPa, 抗弯曲强度达 20MPa, 抗弯模量达 500MPa, 断裂伸长率为 150%, 氧指数 >25, 使用温度为 -10°C〜85°C, 力学性能和耐候性优良。 After testing, the product has a compressive strength of 35MPa, a bending strength of 20MPa, a flexural modulus of 500MPa, an elongation at break of 150%, an oxygen index of >25, and a use temperature of -10°C to 85°C. Excellent mechanical properties and weather resistance.
实施例 7 Example 7
热塑性木塑复合材料的组分及其重量百分含量如下: 木粉 65%, PE25%, 生物质电 厂灰渣 (KD-1)5%, 助剂 5%。 The composition of the thermoplastic wood-plastic composite and its weight percentage are as follows: wood powder 65%, PE 25%, biomass power plant ash (KD-1) 5%, auxiliary 5%.
具体生产过程如下: The specific production process is as follows:
1)对木粉进行预处理 1) Pretreatment of wood flour
2)对木粉进行改性处理 2) Modification of wood flour
a、 碱溶液处理木粉: 用质量浓度为 3%的生物质电厂灰溶液作为浸泡液, 用量以刚 好浸没木粉为宜, 浸泡时间为 48小时, 然后用水将木粉洗呈中性后抽滤并烘干; a. Alkali solution treatment of wood powder: Use 3% of biomass ash solution as the soaking solution, the amount should be just immersed in wood powder, soaking time is 48 hours, then wash the wood powder with neutral water and then pump Filter and dry;
b、 再用马来酸酐接枝聚乙烯处理木粉: 将占木粉重量 1.2%的马来酸酐接枝聚乙烯 直接加入到木粉和 PE粒子的混合料中, 在混合机中搅拌均匀备用。 b. Treat the wood powder with maleic anhydride grafted polyethylene: Add maleic anhydride grafted polyethylene, which accounts for 1.2% by weight of wood powder, directly to the mixture of wood powder and PE particles, and mix well in a mixer. .
3 ) 将干燥后的生物质电厂灰渣 (KD-1 ) 与改性后的木粉, PE粒子, 及防霉剂和润 滑剂等助剂按配比一起放入混合机中混合均匀。 3) Mix the dried biomass power plant ash (KD-1) with the modified wood powder, PE particles, and mildew inhibitors and lubricants into the mixer and mix them evenly.
4)将混合料放入平行双螺杆挤出机内进行塑化造粒,然后再进入单螺杆挤出机挤出, 粒料在挤出机内被混合均化。 4) The mixture is placed in a parallel twin-screw extruder for plasticizing and granulation, and then extruded into a single-screw extruder, and the pellets are mixed and homogenized in the extruder.
5) 将挤出的粒料通过模具部件的几何形状成型, 生产出最终产品。 5) The extruded pellets are shaped by the geometry of the mold part to produce the final product.
经检测, 本产品的抗压强度达 40MPa, 抗弯曲强度达 19MPa, 抗弯模量达 600MPa, 断裂伸长率为 150%, 氧指数 >25, 使用温度为 -10°C〜85°C, 力学性能和耐候性优良。
实施例 8 After testing, the product has a compressive strength of 40MPa, a bending strength of 19MPa, a flexural modulus of 600MPa, an elongation at break of 150%, an oxygen index of >25, and a use temperature of -10°C to 85°C. Excellent mechanical properties and weather resistance. Example 8
热塑性木塑复合材料的组分及其重量百分含量如下: 木粉和稻壳 36%, PE、 PP, 及 PVC40%, 生物质电厂灰渣 (KD- 1)20%, 助剂 4%。 The components of the thermoplastic wood-plastic composite and its weight percentage are as follows: wood powder and rice husk 36%, PE, PP, and PVC 40%, biomass power plant ash (KD-1) 20%, and additives 4%.
具体生产过程如下: The specific production process is as follows:
1)对木粉和稻壳进行预处理 1) Pretreatment of wood flour and rice husk
2)对木粉和稻壳粉进行改性处理 2) Modification of wood flour and rice husk powder
碱溶液处理木粉和稻壳粉: 用质量浓度为 5%的生物质油厂灰溶液作为浸泡液, 用 量以刚好浸没木粉和稻壳粉为宜,浸泡时间为 48小时,然后用水将木粉和稻壳粉洗呈中 性后抽滤并烘干; Alkali solution treatment of wood flour and rice husk powder: Use 5% of biomass oil plant ash solution as the soaking solution, the amount should be just immersed in wood powder and rice husk powder, soaking time is 48 hours, then use water to wood The powder and rice husk powder are washed neutrally, then filtered and dried;
3 ) 将干燥后的生物质电厂灰渣 (KD-1 ) 与改性后的木粉和稻壳, PE、 PP, 及 PVC 粒子, 及发泡剂, 引发剂和润滑剂等助剂按配比一起放入混合机中混合均匀。 3) Mixing the dried biomass power plant ash (KD-1) with modified wood flour and rice hulls, PE, PP, and PVC particles, and foaming agents, initiators and lubricants. Put them together in a mixer and mix well.
4)将混合料放入平行双螺杆挤出机内进行塑化造粒,然后再进入单螺杆挤出机挤出, 粒料在挤出机内被混合均化。 4) The mixture is placed in a parallel twin-screw extruder for plasticizing and granulation, and then extruded into a single-screw extruder, and the pellets are mixed and homogenized in the extruder.
5) 将挤出的粒料通过模具部件的几何形状成型, 生产出最终产品。 5) The extruded pellets are shaped by the geometry of the mold part to produce the final product.
经检测, 本产品的抗压强度达 35MPa, 抗弯曲强度达 20MPa, 抗弯模量达 600MPa, 断裂伸长率为 150%, 氧指数 >25, 使用温度为 -10°C〜85°C, 力学性能和耐候性优良。 After testing, the product has a compressive strength of 35MPa, a bending strength of 20MPa, a flexural modulus of 600MPa, an elongation at break of 150%, an oxygen index of >25, and a use temperature of -10°C to 85°C. Excellent mechanical properties and weather resistance.
本发明生产出的热塑性木塑复合材料力学性能良好, 不易变形开裂, 机械性能高, 吸水率低, 可在很多领域替代原木, 塑料和铝合金等使用; 从生产原料来看, 热塑性木 塑复合材料的原料采用各种废旧塑料、 废木料及农作物的剩余物, 降低了塑料废弃物和 农业废弃物焚烧带来的环境污染; 热塑性木塑复合材料的生产和使用, 不会向周围环境 散发危害人类健康的挥发物,材料本身还可回收利用,是一种生态洁净的木塑复合材料。
The thermoplastic wood-plastic composite material produced by the invention has good mechanical properties, is not easy to be deformed and cracked, has high mechanical properties and low water absorption rate, and can be used for replacing logs, plastics and aluminum alloys in many fields; from the perspective of producing raw materials, thermoplastic wood-plastic composite The raw materials of the materials use various waste plastics, waste wood and crop residues, which reduce the environmental pollution caused by plastic waste and agricultural waste incineration; the production and use of thermoplastic wood-plastic composite materials will not cause harm to the surrounding environment. The volatiles of human health, the material itself can be recycled, is an ecologically clean wood-plastic composite material.
Claims
权利要求书 Claim
1、 一种热塑性木塑复合材料, 其特征在于: 该材料的组分及其重量百分比如下: 植物纤维 20〜70%; 1. A thermoplastic wood-plastic composite material, characterized in that: the composition of the material and its weight percentage are as follows: plant fiber 20 to 70%;
塑料 20〜70%; Plastic 20~70%;
生物质电厂灰渣或生物质油厂灰渣 5〜25%; Biomass power plant ash or biomass oil plant ash 5~25%;
助剂 1〜10%。 Additives 1~10%.
2、 根据权利要求 1所述的热塑性木塑复合材料, 其特征在于: 2. The thermoplastic wood-plastic composite according to claim 1, wherein:
所述各组分的重量百分比如下: The weight percentages of the components are as follows:
植物纤维 50〜65%; Plant fiber 50~65%;
塑料 20〜40%; Plastic 20~40%;
生物质电厂灰渣或生物质油厂灰渣 5〜10%; Biomass power plant ash or biomass oil plant ash 5~10%;
助剂 1〜10%。 Additives 1~10%.
3、 根据权利要求 1所述的热塑性木塑复合材料, 其特征在于: 3. The thermoplastic wood-plastic composite according to claim 1, wherein:
所述各组分的重量百分比如下: The weight percentages of the components are as follows:
植物纤维 35〜53%; Plant fiber 35~53%;
塑料 40〜45%; Plastic 40~45%;
生物质电厂灰渣或生物质油厂灰渣 5〜15%; Biomass power plant ash or biomass oil plant ash 5~15%;
助剂 1〜5%。 Additives 1 to 5%.
4、根据权利要求 1所述的热塑性木塑复合材料, 其特征在于: 所述植物纤维与所述 塑料的重量比为 9:10。 The thermoplastic wood-plastic composite according to claim 1, wherein the weight ratio of the plant fiber to the plastic is 9:10.
5、根据权利要求 1至 4中任一项所述的热塑性木塑复合材料, 其特征在于: 所述生 物质电厂灰渣或生物质油厂灰渣的主要成分为硅酸盐、 钙盐, 以及钾的化合物, 其粒度 为 1000〜5000目, 长径比为 3〜6。
6、根据权利要求 1至 4中任一项所述的热塑性木塑复合材料, 其特征在于: 所述植 物纤维为木粉、 稻壳、 秸秆粉, 及林业三剩物粉中一种或几种任意比例的组合。 The thermoplastic wood-plastic composite material according to any one of claims 1 to 4, wherein: the main component of the biomass power plant ash or biomass oil plant ash is silicate, calcium salt, And a potassium compound having a particle size of 1000 to 5000 mesh and an aspect ratio of 3 to 6. The thermoplastic wood-plastic composite material according to any one of claims 1 to 4, wherein: the plant fiber is one or more of wood flour, rice husk, straw powder, and forestry three remnant powder. Any combination of ratios.
7、根据权利要求 1至 4中任一项所述的热塑性木塑复合材料, 其特征在于: 所述塑 料为废旧的聚乙烯、 聚丙烯, 及聚氯乙烯中一种或几种任意比例的组合。 The thermoplastic wood-plastic composite material according to any one of claims 1 to 4, wherein: the plastic is one or more of any one of waste polyethylene, polypropylene, and polyvinyl chloride. combination.
8、根据权利要求 1至 4中任一项所述的热塑性木塑复合材料, 其特征在于: 所述助 剂为偶联剂、 发泡剂、 引发剂、 抗氧化剂、 着色剂、 阻燃剂、 稳定剂、 防霉剂, 及润滑 剂中的一种或几种。 The thermoplastic wood-plastic composite material according to any one of claims 1 to 4, wherein the auxiliary agent is a coupling agent, a foaming agent, an initiator, an antioxidant, a colorant, and a flame retardant. One or more of stabilizers, mold inhibitors, and lubricants.
9、一种权利要求 1所述的热塑性木塑复合材料的生产方法, 其特征在于: 包括以下 步骤: A method of producing a thermoplastic wood-plastic composite according to claim 1, comprising the steps of:
1 )植物纤维的预处理:将植物纤维粉碎并筛分出粒度为 80〜300目的颗粒后对其进 行干燥, 使植物纤维的含水率 < 5%; 1) pretreatment of plant fibers: the plant fibers are pulverized and sieved to a particle size of 80 to 300 mesh and then dried to make the plant fiber moisture content < 5%;
2) 植物纤维的改性处理: 用质量浓度为 3〜7%的生物质电厂灰渣溶液、 质量浓度 为 3〜7%的生物质油厂灰渣溶液,及占植物纤维重量 0.5%~3%的偶联剂中的一种或几种 对植物纤维表面进行改性处理; 2) Modification of plant fiber: Biomass power plant ash solution with mass concentration of 3~7%, biomass oil plant ash solution with mass concentration of 3~7%, and plant fiber weight 0.5%~3 One or more of the % coupling agents modify the surface of the plant fiber;
3 )混合: 将改性后的植物纤维, 塑料粒子, 生物质电厂灰渣或生物质油厂灰渣, 及 助剂按所述配比进行混合均匀, 备用; 3) mixing: mixing the modified plant fiber, plastic particles, biomass power plant ash or biomass oil plant ash, and auxiliaries according to the ratio, and reserve;
4) 造粒: 将混合物料在 110〜180°C下充分熔合塑化后挤出造粒; 4) granulation: the mixture is fully fused and plasticized at 110~180 ° C, and then extruded and granulated;
5) 热压成型: 将挤出造粒后的粒料用热压成型的方式制得热塑性木塑复合材料。 5) Hot press forming: A thermoplastic wood-plastic composite material is obtained by hot press forming the pellets after extrusion granulation.
10、 根据权利要求 9所述的热塑性木塑复合材料的生产方法, 其特征在于: 所述步 骤 2) 中, 所述偶联剂为钛酸酯、 硬脂酸、 石蜡、 异氰酸酯, 及马来酸配接枝聚乙烯中 的一种或几种任意比例的组合。 The method for producing a thermoplastic wood-plastic composite according to claim 9, wherein in the step 2), the coupling agent is titanate, stearic acid, paraffin, isocyanate, and Malay. One or a combination of several of the acid-grafted polyethylenes in any ratio.
11、根据权利要求 9或 10所述的热塑性木塑复合材料的生产方法, 其特征在于: 所 述步骤 4) 中, 先采用双螺杆塑料挤出机进行熔合塑化, 温度设定为 110〜170°C, 然后
再采用单螺杆挤出机挤出造粒,单螺杆机头温度控制为 115〜180°C,控制挤出压力为 7〜 12MPa0 The method for producing a thermoplastic wood-plastic composite material according to claim 9 or 10, wherein in the step 4), the twin-screw plastic extruder is used for fusion plasticization, and the temperature is set to 110~ 170 ° C, then Single screw extruder and then extrusion granulation, single-screw head temperature is controlled to 115~180 ° C, the extrusion pressure is controlled 7~ 12MPa 0
12、根据权利要求 9或 10所述的热塑性木塑复合材料的生产方法, 其特征在于: 所 述步骤 1 ) 中, 粉碎筛分后的植物纤维粒度为 80〜120目。
The method for producing a thermoplastic wood-plastic composite according to claim 9 or 10, wherein in the step 1), the granulated plant fiber has a particle size of 80 to 120 mesh.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310279688.7A CN103435882B (en) | 2013-07-05 | 2013-07-05 | Thermoplastic wood-plastic composite and production method thereof |
CN201310279688.7 | 2013-07-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2015000363A1 true WO2015000363A1 (en) | 2015-01-08 |
Family
ID=49689609
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/CN2014/080202 WO2015000363A1 (en) | 2013-07-05 | 2014-06-18 | Thermoplastic wood-plastic composite material and method for manufacture thereof |
Country Status (2)
Country | Link |
---|---|
CN (1) | CN103435882B (en) |
WO (1) | WO2015000363A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2632225A1 (en) * | 2016-03-10 | 2017-09-11 | Universidad A Distancia De Madrid Udima, S.A. | Polymeric compound and procedure for obtaining it (Machine-translation by Google Translate, not legally binding) |
SE1751603A1 (en) * | 2017-12-21 | 2019-06-22 | Stora Enso Oyj | Improved process for manufacturing composite product |
CN111421852A (en) * | 2020-04-01 | 2020-07-17 | 国际竹藤中心 | Preparation method of multi-wall-layer weather-resistant plant fiber reinforced air pipe |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104387698B (en) * | 2014-11-06 | 2016-03-30 | 安徽省三乐门窗幕墙工程有限公司 | PVC wood plastic composite material that a kind of plant waste is produced and preparation method thereof |
CN105713407A (en) * | 2016-01-29 | 2016-06-29 | 安徽以诺木塑板材科技有限公司 | Insect prevention and mold prevention wood-plastic panel |
CN106738182A (en) * | 2016-12-09 | 2017-05-31 | 广西北海浩邦新能源科技有限公司 | A kind of processing method of environment-friendly sheet |
CN106827729A (en) * | 2017-01-10 | 2017-06-13 | 东北林业大学 | A kind of high temperature is coextruded Wood-plastic profiles |
CN110294821B (en) * | 2019-07-03 | 2022-03-18 | 广东工业大学 | Dispersing agent and preparation method and application thereof |
CN111019229A (en) * | 2019-12-06 | 2020-04-17 | 兴义市亿洪市场管理有限公司 | Stone wood plastic material prepared from regenerated raw materials and preparation method |
CN111168874A (en) * | 2019-12-31 | 2020-05-19 | 湖南格林美映鸿资源循环有限公司 | Method for efficiently recycling plastic-wood sawdust powder |
CN114605849B (en) * | 2022-03-24 | 2022-11-11 | 华南农业大学 | Manufacturing method of wood-plastic granules and composite material with ultrahigh wood fiber content |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101418086A (en) * | 2008-12-08 | 2009-04-29 | 中国热带农业科学院农产品加工研究所 | Method for preparing rice hull ash-natural rubber composite material |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100368167C (en) * | 2004-01-15 | 2008-02-13 | 中国科学院过程工程研究所 | Composite waterproof plate, ad its manufacturing method and use |
CN101224966B (en) * | 2007-12-27 | 2010-06-23 | 中国科学院长春应用化学研究所 | Wood-silicon-plastic net floor and preparation method thereof |
CN102321374B (en) * | 2011-07-29 | 2012-12-12 | 东北林业大学 | Fire-retardant polyolefin based wood plastic composite material and preparation method thereof |
-
2013
- 2013-07-05 CN CN201310279688.7A patent/CN103435882B/en active Active
-
2014
- 2014-06-18 WO PCT/CN2014/080202 patent/WO2015000363A1/en active Application Filing
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101418086A (en) * | 2008-12-08 | 2009-04-29 | 中国热带农业科学院农产品加工研究所 | Method for preparing rice hull ash-natural rubber composite material |
Non-Patent Citations (5)
Title |
---|
BU, FANHUA;: "Aging Resistance of Rice Hull Powder/Recycled HDPE Composites", SCIENCE -ENGINEERING (A), CHINA MASTER'S THESES FULL-TEXT DATABASE, no. 4, 15 April 2011 (2011-04-15), pages 8 - 9 * |
CHAUDHARY, D.S. ET AL.: "Recycling Rice Hull Ash: a Filler Material for Polymeric Composites?", ADVANCES IN POLYMER TECHNOLOGY, vol. 23, no. 2, 29 March 2004 (2004-03-29), pages 147 - 155, XP001233525, DOI: doi:10.1002/adv.20000 * |
CHEN, HUATANG ET AL.: "Preparation and Mechanical Properties of PP/Biomass Ash Composites", ENGINEERING PLASTICS APPLICATION, vol. 38, no. 12, 10 December 2010 (2010-12-10), pages 32 - 33 * |
KHALIL, R. ET AL.: "Effect of Coupling Agents on the Crystallinity and Viscoe-lastic Properties of Composites of Rice Hull Ash-filled Polypropylene", JOURNAL OF MATERIALS SCIENCE, vol. 42, 22 September 2007 (2007-09-22), pages 10219 - 10227 * |
MI, TIE ET AL.: "Chemistry Characteristic Study on Biomass Ash", ACTA ENERGIAE SOLARIS SINICA, vol. 25, no. 2, 25 April 2004 (2004-04-25), pages 236 - 240 * |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2632225A1 (en) * | 2016-03-10 | 2017-09-11 | Universidad A Distancia De Madrid Udima, S.A. | Polymeric compound and procedure for obtaining it (Machine-translation by Google Translate, not legally binding) |
SE1751603A1 (en) * | 2017-12-21 | 2019-06-22 | Stora Enso Oyj | Improved process for manufacturing composite product |
WO2019123231A1 (en) * | 2017-12-21 | 2019-06-27 | Stora Enso Oyj | Improved process for manufacturing composite product |
SE541870C2 (en) * | 2017-12-21 | 2020-01-02 | Stora Enso Oyj | Improved process for manufacturing composite product |
CN111406089A (en) * | 2017-12-21 | 2020-07-10 | 斯道拉恩索公司 | Improved process for manufacturing composite products |
US11267206B2 (en) | 2017-12-21 | 2022-03-08 | Stora Enso Oyj | Process for manufacturing composite product |
CN111421852A (en) * | 2020-04-01 | 2020-07-17 | 国际竹藤中心 | Preparation method of multi-wall-layer weather-resistant plant fiber reinforced air pipe |
Also Published As
Publication number | Publication date |
---|---|
CN103435882B (en) | 2015-09-09 |
CN103435882A (en) | 2013-12-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2015000363A1 (en) | Thermoplastic wood-plastic composite material and method for manufacture thereof | |
CN107298868A (en) | A kind of enhanced Wood-plastic material of lignin and preparation method thereof | |
CN102352116B (en) | Wood-plastic composite material and preparation method thereof | |
CN101775167B (en) | Environment protective plastic-wood composite material and preparation method thereof | |
CN105585868B (en) | A kind of straw plastic composite materials and preparation method thereof | |
CN104130515A (en) | Hickory nut shell ecologic wood composite material and preparation method thereof | |
CN102140255A (en) | Hot-press type wood plastic composite for toy and preparation method thereof | |
CN102250476A (en) | Bamboo-fiber-based micro-foamed wood-plastic composite material and preparation method thereof | |
KR100991506B1 (en) | Composition of synthetic wood and method of manufacturing the same | |
KR101042694B1 (en) | Synthetic wood using natural fiber plastics | |
CN104231646A (en) | Preparation method of high-strength wood-plastic composite material and high-strength wood-plastic composite material | |
CN102304291A (en) | Bamboo and plastic composite material and preparation method thereof | |
CN103450530A (en) | Nanoparticle composite material | |
CN104761820A (en) | Method for preparing polypropylene-based wood-plastic composite material by using rice husk powder | |
KR102181876B1 (en) | Manufacturing method of composite resin composition using waste separator for secondary battery | |
CN104804452A (en) | Method of preparing polyvinyl wood-plastic composite with cotton stalks | |
CN108530854B (en) | Preparation method of straw powder-PLA wood-plastic composite material | |
CN108610651B (en) | Badam/polyolefin flame-retardant composite material and preparation method thereof | |
CN104403345A (en) | High-strength abrasion-proof high-molecular material and preparation method thereof | |
KR100681333B1 (en) | A wood plastic composites | |
CN104403342A (en) | High-strength wood-plastic composite with swelling resistance, moisture resistance and ageing resistance and preparation method of wood-plastic composite | |
CN101153119A (en) | Clubbed composite material of wood-wool and plastics, and method of producing the same | |
CN102532661A (en) | Natural fiber filled polyethylene composite material and preparation method thereof | |
CN104774408A (en) | Method for preparing PVC (polyvinyl chloride)-based wood-plastic composite material by using rice hull powder | |
CN104231512A (en) | Preparation method of degradable wood-plastic composite material and degradable wood-plastic composite material |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 14819911 Country of ref document: EP Kind code of ref document: A1 |
|
NENP | Non-entry into the national phase in: |
Ref country code: DE |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 14819911 Country of ref document: EP Kind code of ref document: A1 |