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CN101864184B - Thermoplastic vegetable fiber/starch blending material and preparation method thereof - Google Patents

Thermoplastic vegetable fiber/starch blending material and preparation method thereof Download PDF

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Publication number
CN101864184B
CN101864184B CN2009100589640A CN200910058964A CN101864184B CN 101864184 B CN101864184 B CN 101864184B CN 2009100589640 A CN2009100589640 A CN 2009100589640A CN 200910058964 A CN200910058964 A CN 200910058964A CN 101864184 B CN101864184 B CN 101864184B
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thermoplastic
parts
plant fiber
starch
vegetable
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CN101864184A (en
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罗学刚
徐东
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Southwest University of Science and Technology
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B29C48/40Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/04Particle-shaped
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92514Pressure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92561Time, e.g. start, termination, duration or interruption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/92895Barrel or housing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92923Calibration, after-treatment or cooling zone

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Artificial Filaments (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Biological Depolymerization Polymers (AREA)

Abstract

本发明公开了一种热塑性植物纤维/淀粉共混材料及其制备方法。它的各组分重量比为:热塑性植物纤维1~99,热塑性淀粉1~99,交联剂0~10,增塑剂0~10。它的制备是将原料在高速混合机中搅拌5~20分钟,在温度30~60℃干燥8~12小时,控温于100~140℃将共混料在双螺杆挤塑机中熔融共混5~10min,在110~150℃、0.1~1MPa下造粒而得产品。本发明产品加工性能良好,在挤塑、吹塑、注塑和发泡过程中具有优良的热塑加工特性和力学性能,其制品使用后完全降解且环境友好,可广泛地用于化工、农地膜、机电、建筑材料、包装和环保等生产加工领域。The invention discloses a thermoplastic plant fiber/starch blend material and a preparation method thereof. The weight ratio of each component is: thermoplastic plant fiber 1-99, thermoplastic starch 1-99, crosslinking agent 0-10, plasticizer 0-10. Its preparation is to stir the raw materials in a high-speed mixer for 5-20 minutes, dry at a temperature of 30-60°C for 8-12 hours, and control the temperature at 100-140°C to melt and blend the blended materials in a twin-screw extruder. 5 ~ 10 minutes, granulation at 110 ~ 150 ° C, 0.1 ~ 1MPa to obtain the product. The product of the invention has good processing performance, and has excellent thermoplastic processing characteristics and mechanical properties in the process of extrusion molding, blow molding, injection molding and foaming. , electromechanical, building materials, packaging and environmental protection and other production and processing fields.

Description

热塑性植物纤维/淀粉共混材料及其制备方法Thermoplastic plant fiber/starch blend material and preparation method thereof

(一)技术领域  本发明涉及本发明涉及热塑性植物纤维/淀粉共混材料及其制备方法。(1) Technical field The present invention relates to the present invention relates to thermoplastic plant fiber/starch blend material and preparation method thereof.

(二)背景技术  全世界每年有1.5亿吨石油、天然气等有限的石化资源用于化学合成“合成高分子”,为了减少废弃合成高分子材料产品对环境的影响和有限资源的利用,重新构筑可持续发展的人类社会已成为世界各国的共识。实现世界经济的可持续发展,国内外的相关研究前沿之一是利用清洁生产技术,将可再生的生物质资源,改性、合成满足使用要求的环境友好高分子新材料,降低对有限资源的消耗,减少材料使用后对环境的污染,为此国内外的相关研究更注重寻找新的天然高分子塑料材料。(2) Background technology Every year, 150 million tons of limited petrochemical resources such as oil and natural gas are used to chemically synthesize "synthetic polymers". The sustainable development of human society has become the consensus of all countries in the world. To achieve the sustainable development of the world economy, one of the frontiers of related research at home and abroad is to use clean production technology to modify and synthesize renewable biomass resources into environmentally friendly polymer materials that meet the requirements of use, reducing the impact on limited resources. Consumption, to reduce the pollution of the environment after the use of materials, for this reason, related research at home and abroad pays more attention to finding new natural polymer plastic materials.

植物纤维是地球上巨大的再生性生物高分子资源。从资源的可持续利用、保护环境和生物体亲和性与生物分解性特点出发,人们对于能再生的植物纤维的利用寄托了很大的期望。从而植物纤维资源化利用,开发环境友好的绿色产品,已形成环境绿色高技术研究与开发中的热点领域。植物纤维作为可再生资源,它的改性和利用一方面可节省大量石油资源,另一方面可以缓解大量非降解合成高分子材料废弃物造成的环境污染,植物纤维及其改性材料废弃后可以在自然环境中实现生物量的循环。Plant fiber is a huge regenerative biopolymer resource on the earth. Starting from the sustainable utilization of resources, protection of the environment, and the characteristics of biocompatibility and biodegradability, people place great expectations on the utilization of renewable plant fibers. Thus, the resource utilization of plant fibers and the development of environmentally friendly green products have formed a hot field in the research and development of environmentally green high-tech. As a renewable resource, the modification and utilization of plant fiber can save a lot of petroleum resources on the one hand, and alleviate the environmental pollution caused by a large amount of non-degradable synthetic polymer waste. Realize the cycle of biomass in the natural environment.

淀粉是来源丰富、价格便宜的天然高分子物质,是一种取之不竭的可再生资源。淀粉有着能再生、廉价、易保存和便于运输的特点,在一定条件下可进行各种反应,派生出众多衍生物。淀粉良好的可利用性和生物降解性使其成为生物降解材料的良好原料,淀粉基衍生物材料能在多种环境下被生物降解,最终降解产物CO2和H2O可通过光合作用进行再循环,不会对环境产生任何污染。多年来世界各国对淀粉基热塑材料的研究开发十分重视,但热塑性淀粉熔体性能差,加工应用过程中存在着困难,其材料的粘度和强度均较低,导致成型加工过程中定型速度很慢,实施吹塑、压延、注塑纺丝等加工方式难度很大,很难通过常规的加工方法在常规聚合物加工设备上加工出符合使用要求的产品。Starch is a natural polymer material with abundant sources and low price, and it is an inexhaustible renewable resource. Starch has the characteristics of being renewable, cheap, easy to store and easy to transport. Under certain conditions, it can undergo various reactions and derive many derivatives. The good availability and biodegradability of starch make it a good raw material for biodegradable materials. Starch-based derivative materials can be biodegraded in a variety of environments, and the final degradation products CO2 and H2O can be recycled through photosynthesis. will cause any pollution to the environment. Over the years, countries all over the world have attached great importance to the research and development of starch-based thermoplastic materials, but thermoplastic starch melt has poor performance, and there are difficulties in processing and application. It is very difficult to implement processing methods such as blow molding, calendering, injection molding and spinning, and it is difficult to process products that meet the requirements of use on conventional polymer processing equipment through conventional processing methods.

热塑性植物纤维与淀粉熔融共混改性后得到的新型热塑共混材料加工性能良好,在挤塑、吹塑、注塑和发泡过程中具有优良的热塑加工特性和力学性能,其制品使用后完全降解且环境友好,可广泛地用于化工、农地膜、机电、建筑材料、包装和环保等生产加工领域。The new thermoplastic blend material obtained after thermoplastic plant fiber and starch melt blending modification has good processing performance, and has excellent thermoplastic processing characteristics and mechanical properties in the process of extrusion, blow molding, injection molding and foaming. Its products are used After being completely degraded and environmentally friendly, it can be widely used in the production and processing fields of chemical industry, agricultural mulch film, electromechanical, building materials, packaging and environmental protection.

(三)发明内容(3) Contents of the invention

1、发明目的  本发明的目的是提供一种环境友好的热塑性植物纤维/淀粉共混材料及其制备方法。热塑性植物纤维/淀粉共混可以改善热塑性植物纤维的加工性能,同时可以对淀粉起到较好的增塑作用,解决淀粉加工性能、韧性和抗撕裂性能不足、断裂伸长率低、薄膜较脆等不足等问题,提供一种以天然植物纤维为原料,生产环境友好的植物纤维/淀粉热塑材料的新方法,为可再生资源植物纤维的大规模开发利用服务。1. Purpose of the invention The purpose of the present invention is to provide an environmentally friendly thermoplastic plant fiber/starch blend material and its preparation method. The blending of thermoplastic plant fiber/starch can improve the processing performance of thermoplastic plant fiber, and at the same time, it can have a good plasticizing effect on starch, and solve the problems of insufficient starch processing performance, toughness and tear resistance, low elongation at break, and thin films. Brittleness and other problems, provide a new method of producing environmentally friendly plant fiber/starch thermoplastic materials using natural plant fibers as raw materials, and serve for the large-scale development and utilization of renewable resource plant fibers.

2、技术方案  本发明的技术方案是:2. Technical solution The technical solution of the present invention is:

一种热塑性植物纤维/淀粉共混材料,它的各组分的重量份配比为:热塑性植物纤维1~99,热塑性淀粉1~99,交联剂0~10,增塑剂0~10。所述的热塑性植物纤维是将去杂后的植物纤维原料粉碎,膨化,加入植物纤维重量2倍的1%H2S04溶液,在120℃下处理1h,过滤、清洗、干燥、粉碎过40目筛,得到去除木素和多缩戊糖的纯净植物纤维粉;在纯净植物纤维粉中加入3倍的18%NaOH溶液,在30℃下浸渍2h,压榨挤去多余的碱液,使植物纤维中含碱液控制在50%,即获得碱化植物纤维;按重量比取碱化植物纤维100份、过硫酸钾2份、丙烯酸甲酯200份于反应釜中,同时通入N2,30℃下搅拌反应10h,至物料呈浆状后加入10%的醋酸溶液中和至pH7.0;反应液通过离心分离去除溶液,所得固体经水洗至中性后真空干燥即得到热塑性植物纤维;所述的热塑性淀粉是按重量份数取淀粉100份、甘油15份、马来酸酐20份、过氧化叔丁基0.035份、马来酸二辛酯3份和水16份,在高速混炼机进行混合搅拌后,在140℃~160℃通过挤出机进行熔融共混接枝反应,反应结束后的挤出造粒得到热塑性淀粉;所述的交联剂选用顺丁烯二酸酐,柠檬酸三丁酯、乙撑双硬脂酸酰胺、六方氮化硼中的一种或两种以上的任意组合;所述的增塑剂选用丙三醇,聚乙二醇,邻苯二甲酸二丁酯,己二酸二丁酯中的一种或两种以上的任意组合。The invention relates to a thermoplastic plant fiber/starch blended material, the weight ratio of each component of which is: thermoplastic plant fiber 1-99, thermoplastic starch 1-99, crosslinking agent 0-10, plasticizer 0-10. The thermoplastic plant fiber is prepared by crushing and expanding the plant fiber raw material after removal of impurities, adding 1% H2SO4 solution twice the weight of the plant fiber, treating at 120° C. for 1 hour, filtering, cleaning, drying, and pulverizing through a 40-mesh sieve. Obtain the pure plant fiber powder that removes lignin and pentosan; Add 3 times of 18% NaOH solution to the pure plant fiber powder, dip for 2h at 30°C, press to squeeze out excess lye, so that the plant fiber contains The lye is controlled at 50% to obtain alkalized plant fibers; take 100 parts of alkalized plant fibers, 2 parts of potassium persulfate, and 200 parts of methyl acrylate in the reaction kettle by weight, and feed N2 at the same time, stirring at 30 ° C React for 10 hours, add 10% acetic acid solution to neutralize to pH 7.0 after the material is in a slurry form; the reaction solution is removed by centrifugation, and the obtained solid is washed to neutral and then vacuum-dried to obtain a thermoplastic plant fiber; the thermoplastic The starch is 100 parts by weight of starch, 15 parts of glycerin, 20 parts of maleic anhydride, 0.035 parts of tert-butyl peroxide, 3 parts of dioctyl maleate and 16 parts of water, and mix and stir in a high-speed mixer Finally, melt blending and grafting reaction is carried out through an extruder at 140°C to 160°C, and extrusion granulation after the reaction is completed to obtain thermoplastic starch; the crosslinking agent is selected from maleic anhydride, tributyl citrate , ethylene bis stearic acid amide, hexagonal boron nitride, or any combination of two or more; the plasticizer is selected from glycerol, polyethylene glycol, dibutyl phthalate, hexagonal One or any combination of two or more dibutyl diacids.

一种制备热塑性植物纤维/淀粉共混材料的方法,其具体步骤是:A kind of method for preparing thermoplastic plant fiber/starch blended material, its concrete steps are:

第一步,配料:按重量比配比取热塑性植物纤维1~99,热塑性淀粉1~99,交联剂0~10,增塑剂0~10,在高速混合机中搅拌混匀5~20min。The first step, ingredients: take thermoplastic plant fiber 1~99, thermoplastic starch 1~99, crosslinking agent 0~10, plasticizer 0~10 according to weight ratio, stir and mix in a high-speed mixer for 5~20min .

第二步,干燥:将混合均匀的共混物在温度30~60℃干燥8~12小时。The second step, drying: the homogeneously mixed blend is dried at a temperature of 30-60°C for 8-12 hours.

第三步,共混造粒:将干燥好的共混料在双螺杆挤出机中于100~140℃熔融共混5~10min,在110~150℃、0.1~1MPa下挤出造粒,制备成热塑性植物纤维/淀粉共混材料。The third step, blending and granulation: Melt and blend the dried blended material in a twin-screw extruder at 100-140°C for 5-10 minutes, extrude and granulate at 110-150°C and 0.1-1MPa, Prepare thermoplastic plant fiber/starch blend material.

3、有益效果  植物纤维作为一种可再生天然资源,来源充足以及可生物降解。对其进行共混改性,可得到以植物纤维为骨架的热塑性植物纤维/淀粉共混新材料。作为可再生资源,它的共混改性和利用一方面可节省大量石油资源,另一方面可以缓解大量非降解合成高分子材料废弃物造成的环境污染,热塑性植物纤维/淀粉共混材料废弃后可以在自然环境中实现生物量的循环。热塑性植物纤维与热塑性淀粉共混改性,两者相容性很好,能够达到热力学相容状态,避免产品的相分离现象,提高了改性产品性能的稳定性。热塑性植物纤维与热塑性淀粉共混改性,使其加工流变特性与聚乙烯相似,便于使用常规设备进行工业化生产。热塑性植物纤维与热塑性淀粉共混改性产品,综合力学性能优良,其制品使用后完全降解且环境友好,可广泛地用于化工、农地膜、机电、建筑材料、包装和环保等生产加工领域。3. Beneficial effects As a renewable natural resource, plant fiber has sufficient sources and is biodegradable. By blending and modifying it, a new thermoplastic plant fiber/starch blend material with plant fiber as the skeleton can be obtained. As a renewable resource, its blending modification and utilization can save a lot of petroleum resources on the one hand, and on the other hand can alleviate the environmental pollution caused by a large amount of non-degradable synthetic polymer waste. Biomass recycling can be achieved in the natural environment. The blending modification of thermoplastic plant fiber and thermoplastic starch has good compatibility and can reach a state of thermodynamic compatibility, avoiding the phase separation of the product, and improving the stability of the performance of the modified product. The blending modification of thermoplastic plant fiber and thermoplastic starch makes its processing rheological properties similar to that of polyethylene, which is convenient for industrial production with conventional equipment. The blended modified product of thermoplastic plant fiber and thermoplastic starch has excellent comprehensive mechanical properties, and its products are completely degradable and environmentally friendly after use. They can be widely used in the production and processing fields of chemical industry, agricultural mulch film, electromechanical, building materials, packaging and environmental protection.

(四)具体实施方式(4) Specific implementation methods

下面结合实施例对本发明做进一步详细说明,其中所述原料份数除特殊说明外,均为重量份数。The present invention will be further described in detail below in conjunction with the examples, wherein the parts of raw materials are all parts by weight unless otherwise specified.

实施例1:按重量比取热塑性植物纤维1份、热塑性淀粉99份,顺丁烯二酸酐1份在高速混合机中搅拌5分钟,在温度30℃干燥12小时,控温于100℃将共混料在双螺杆挤塑机中熔融共混5min,在110℃、1MPa下造粒得到完全生物降解热塑性植物纤维/淀粉共混材料。Example 1: Take 1 part of thermoplastic plant fiber, 99 parts of thermoplastic starch, and 1 part of maleic anhydride in a high-speed mixer for 5 minutes, dry at a temperature of 30 ° C for 12 hours, and control the temperature at 100 ° C. The mixture was melt-blended in a twin-screw extruder for 5 minutes, and pelletized at 110° C. and 1 MPa to obtain a fully biodegradable thermoplastic plant fiber/starch blend material.

实施例2:按重量比取热塑性植物纤维99份、热塑性淀粉1份,邻苯二甲酸二丁酯10份在高速混合机中搅拌20分钟,在温度60℃干燥8小时,控温于140℃将共混料在双螺杆挤塑机中熔融共混10min,在150℃、0.1MPa下造粒得到完全生物降解热塑性植物纤维/淀粉共混材料。Example 2: Take 99 parts of thermoplastic plant fiber, 1 part of thermoplastic starch, and 10 parts of dibutyl phthalate according to the weight ratio, stir in a high-speed mixer for 20 minutes, dry at a temperature of 60°C for 8 hours, and control the temperature at 140°C The blended material was melt-blended in a twin-screw extruder for 10 minutes, and pelletized at 150° C. and 0.1 MPa to obtain a fully biodegradable thermoplastic plant fiber/starch blended material.

实施例3:按重量比取热塑性植物纤维10份、热塑性淀粉90份,柠檬酸三丁酯3份和丙三醇3份、聚乙二醇7份在高速混合机中搅拌8分钟,在温度40℃干燥10小时,控温于110℃将熔融共混料在双螺杆挤塑机中共混6min,在120℃、0.7MPa下造粒得到完全生物降解热塑性植物纤维/淀粉共混材料。Embodiment 3: get 10 parts of thermoplastic plant fibers, 90 parts of thermoplastic starches by weight, 3 parts of tributyl citrate and 3 parts of glycerol, 7 parts of Polyethylene Glycol are stirred in high-speed mixer 8 minutes, at temperature Dry at 40°C for 10 hours, blend the melt blended material in a twin-screw extruder at 110°C for 6 minutes, and granulate at 120°C and 0.7 MPa to obtain a fully biodegradable thermoplastic plant fiber/starch blend material.

实施例4:按重量比取热塑性植物纤维30份、热塑性淀粉70份,乙撑双硬脂酸酰胺5份和己二酸二丁酯3份在高速混合机中搅拌10分钟,在温度45℃干燥12小时,控温于120℃将共混料在双螺杆挤塑机中熔融共混7min,在130℃、0.5MPa下造粒得到完全生物降解热塑性植物纤维/淀粉共混材料。Example 4: Take 30 parts of thermoplastic plant fiber, 70 parts of thermoplastic starch, 5 parts of ethylene bis stearic acid amide and 3 parts of dibutyl adipate by weight, stir in a high-speed mixer for 10 minutes, and dry at a temperature of 45 ° C For 12 hours, the blend was melt-blended in a twin-screw extruder at 120°C for 7 minutes, and granulated at 130°C and 0.5 MPa to obtain a fully biodegradable thermoplastic plant fiber/starch blend material.

实施例5:按重量比取热塑性植物纤维50份、热塑性淀粉50份,六方氮化硼7份和聚乙二醇5份在高速混合机中搅拌15分钟,在温度35℃干燥12小时,控温于130℃将共混料在双螺杆挤塑机中熔融共混8min,在140℃、0.3MPa下造粒得到完全生物降解热塑性植物纤维/淀粉共混材料。Embodiment 5: Take 50 parts of thermoplastic plant fiber, 50 parts of thermoplastic starch, 7 parts of hexagonal boron nitride and 5 parts of polyethylene glycol by weight, stir in a high-speed mixer for 15 minutes, and dry at a temperature of 35 ° C for 12 hours. The blended material was melt-blended in a twin-screw extruder at 130° C. for 8 minutes, and pelletized at 140° C. and 0.3 MPa to obtain a fully biodegradable thermoplastic plant fiber/starch blended material.

实施例6:按重量比取热塑性植物纤维70份、热塑性淀粉30份,柠檬酸三丁酯5份、乙撑双硬脂酸酰胺5份和丙三醇7份在高速混合机中搅拌12分钟,在温度50℃干燥8小时,控温于140℃将共混料在双螺杆挤塑机中熔融共混9min,在150℃、0.2MPa下造粒得到完全生物降解热塑性植物纤维/淀粉共混材料。Embodiment 6: Get 70 parts of thermoplastic plant fibers, 30 parts of thermoplastic starch, 5 parts of tributyl citrate, 5 parts of ethylene bis stearic acid amide and 7 parts of glycerol by weight and stir in a high-speed mixer for 12 minutes , dried at 50°C for 8 hours, controlled temperature at 140°C, melt blended the blended material in a twin-screw extruder for 9 minutes, and granulated at 150°C and 0.2MPa to obtain a fully biodegradable thermoplastic plant fiber/starch blend Material.

Claims (4)

1. a thermoplastic vegetable fiber is characterized in that, the weight part proportioning of its each component is: thermoplastic plant fiber 1~99, thermoplastic starch 1~99, linking agent 0~10, softening agent 0~10; Described thermoplastic plant fiber is that the plant fiber material after the impurity elimination is pulverized, and is expanded; The 1%H that adds 2 times of vegetable fibre weight 2SO 4Solution is handled 1h down at 120 ℃; Filter, clean, dry, pulverized 40 mesh sieves, obtain removing the pure plant fiber powder of lignin and pentosan; The 18%NaOH solution that in pure plant fiber powder, adds 3 times, at 30 ℃ of dipping 2h down, squeezing is squeezed and is removed unnecessary alkali lye, makes to contain alkali lye in the vegetable fibre and be controlled at 50%, promptly obtains the alkalization vegetable fibre; Get 200 parts of alkalization 100 parts on vegetable fibre, 2 parts of Potassium Persulphates, methyl acrylates by weight in reactor, feed N simultaneously 2, 30 ℃ of following stirring reaction 10h are to material and add 10% acetum behind the pulpous state and be neutralized to pH7.0; Reaction solution is removed solution by centrifugation, and the gained solid is drying to obtain thermoplastic plant fiber through being washed to neutral final vacuum; Described thermoplastic starch is to get 16 parts in 100 parts of starch, 15 parts of glycerine, 20 parts of maleic anhydrides, 0.035 part of tert-butyl peroxide, 3 parts of dioctyl maleates and water by weight, after high speed mixing roll mixing stirring, carry out the melt blending graft reaction at 140 ℃~160 ℃ by forcing machine, the extruding pelletization after reaction finishes obtains thermoplastic starch.
2. thermoplastic vegetable fiber according to claim 1 is characterized in that, described linking agent is a MALEIC ANHYDRIDE, the arbitrary combination of one or more in tributyl citrate, ethylene bis stearic acid amide, the hexagonal boron nitride.
3. thermoplastic vegetable fiber according to claim 1 is characterized in that, described softening agent is a glycerol, polyoxyethylene glycol, dibutyl phthalate, the arbitrary combination of one or more in the Polycizer W 260.
4. prepare the method for the described thermoplastic vegetable fiber of claim 1, the steps include:
The first step, batching: by weight proportioning heat-obtaining plasticity vegetable fibre 1~99, thermoplastic starch 1~99, linking agent 0~10, softening agent 0~10, stirring and evenly mixing 5~20min in high-speed mixer;
Second step, drying: with the blend that mixes 30~60 ℃ of dryings of temperature 8~12 hours;
In the 3rd step, the blend granulation: in 100~140 ℃ of melt blending 5~10min, extruding pelletization under 110~150 ℃, 0.1~1MPa is prepared into thermoplastic vegetable fiber to the blend composition that drying is good in twin screw extruder.
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