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CN100532453C - A polylactic acid foam plastic sheet for plastic absorption and its preparation method - Google Patents

A polylactic acid foam plastic sheet for plastic absorption and its preparation method Download PDF

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CN100532453C
CN100532453C CNB2006101170698A CN200610117069A CN100532453C CN 100532453 C CN100532453 C CN 100532453C CN B2006101170698 A CNB2006101170698 A CN B2006101170698A CN 200610117069 A CN200610117069 A CN 200610117069A CN 100532453 C CN100532453 C CN 100532453C
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CN1958668A (en
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任杰
刘智勇
袁华
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Tongji University
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Abstract

This invention relates to a method for preparing polylactic acid foamed plastic, especially polylactic acid foamed plastic sheet material for sucking-plasticization. The raw materials for the sheet material are: polylactic acid resin 100 parts, chain extender 0.2-2 parts, nucleating agent 0.1-5 parts, foamer 0.3-2.5 parts, toughener 0.5-15 parts, reinforcer 0.5-5 parts, and antioxidant 0.1-1 part. The method comprises: extruding the raw materials without the foamer to obtain master batch, adding the foamer, extruding, stretching unidirectionally, and shaping, cutting, spreading, coiling and packaging. The foamed plastic sheet material has good mechanical properties and obstructive ability, and is biodegradable, thus the cost performance is high. The sucking-plasticized products can be used to manufacture bottles for cosmetics, pesticides and drinks, food packaging containers, dishwares, trays and vacuum-shaped products.

Description

一种吸塑用聚乳酸泡沫塑料片材及其制备方法 A polylactic acid foam plastic sheet for plastic absorption and its preparation method

技术领域 technical field

本发明属工程塑料技术领域,具体涉及一种聚乳酸泡沫塑料特别是吸塑用聚乳酸泡沫塑料片材及其制备方法。The invention belongs to the technical field of engineering plastics, and in particular relates to a polylactic acid foamed plastic, in particular to a polylactic acid foamed plastic sheet for plastic absorption and a preparation method thereof.

背景技术 Background technique

进入21世纪以来,保护地球环境,构筑资源循环型社会,走可持续发展道路,已成为世界关注热点和紧迫任务。生物降解塑料通过产品整个生命周期分析,已确认为环境低负荷材料。另外,相当一部份生物降解塑料的主要原料是来自可年年再生的农业资源,作为有限的、日渐减少、日趋枯竭的不可再生的石油资源的补充替代,也已成为全球瞩目的发展趋势。因此,生物降解塑料已成为全球研究开发热点。Since the beginning of the 21st century, protecting the earth's environment, building a resource-recycling society, and taking the road of sustainable development have become the focus and urgent task of the world. Biodegradable plastics have been confirmed as low-environmental load materials through product life cycle analysis. In addition, a considerable part of the main raw materials of biodegradable plastics come from renewable agricultural resources. As a supplementary replacement for limited, dwindling, and depleting non-renewable petroleum resources, it has also become a global development trend. Therefore, biodegradable plastics have become a global research and development hotspot.

聚乳酸(PLA)也称为聚丙交酯,属于聚酯家族。作为新型可完全降解塑料,它受到越来越多国家、企业的关注。聚乳酸是以乳酸为主要原料聚合得到的聚合物,原料来源充分而且可以再生。聚乳酸可经由水解反应以及微生物分解作用而完全分解成二氧化碳和水,其在大气环境下、在含微生物的土壤或水中、在垃圾掩埋场中以及在堆肥中所需的分解时间分别为3-5年、2—3年、2—4月以及1—4周。聚乳酸的生产过程无污染,而且产品可以生物降解,实现在自然界中的循环,因此是理想的绿色高分子材料。Polylactic acid (PLA), also known as polylactide, belongs to the family of polyesters. As a new type of fully degradable plastic, it has attracted the attention of more and more countries and enterprises. Polylactic acid is a polymer obtained by polymerizing lactic acid as the main raw material. The raw material source is sufficient and can be regenerated. Polylactic acid can be completely decomposed into carbon dioxide and water through hydrolysis reaction and microbial decomposition, and the decomposition time required in the atmosphere, in soil or water containing microorganisms, in landfills and in compost is 3- 5 years, 2-3 years, 2-4 months and 1-4 weeks. The production process of polylactic acid is non-polluting, and the product can be biodegraded to realize the cycle in nature, so it is an ideal green polymer material.

但是,由于聚乳酸生产成本过高的限制,它作为降解塑料使用起步较晚。近年来,由于环保要求和石油资源的短缺,使得人们对聚乳酸倍加重视,开始了聚乳酸产品的探索开发。目前,在市场上存在许多以聚乙烯、聚苯乙烯,大都以聚氨酯为原料制得的泡沫塑料吸塑产品,它们具有质轻、省料、热导率低、隔热性能好、吸收冲击载荷等性能,在包装行业发挥着巨大作用。然而,这些泡沫塑料被使用以后,很难回收处理再次循环使用,丢弃到环境中,不能与环境同化,对环境造成巨大危害。聚乳酸泡沫塑料的开发,不仅可以有效解决上述问题,而且降低了聚乳酸制品的成本。However, due to the limitation of high production cost of polylactic acid, its use as a degradable plastic started late. In recent years, due to environmental protection requirements and the shortage of petroleum resources, people have paid more attention to polylactic acid, and began to explore and develop polylactic acid products. At present, there are many foamed plastic blister products made of polyethylene, polystyrene, and mostly polyurethane on the market. They have light weight, material saving, low thermal conductivity, good heat insulation performance, and shock load absorption. And other properties, play a huge role in the packaging industry. However, after these foamed plastics are used, it is difficult to recycle and recycle them, and they are discarded into the environment, which cannot be assimilated with the environment and cause great harm to the environment. The development of polylactic acid foam can not only effectively solve the above problems, but also reduce the cost of polylactic acid products.

由于PLA延伸性优,但脆性大,原有的一些聚乳酸发泡工艺存在一些不足。Sterzel等人采用在聚乳酸中混入物理发泡剂的方法制备聚乳酸结构泡沫塑料(美国专利5348983,1994),但是要把聚乳酸制成粒径较小的粒子后才能发泡。Kameoka等人采用混入化学发泡剂和物理发泡剂直接挤出的方法制备聚乳酸泡沫塑料(美国专利5763098,1998),但性脆,耐冲击性不好。Due to the excellent extensibility of PLA, but high brittleness, some original polylactic acid foaming processes have some shortcomings. People such as Sterzel adopt the method for mixing physical foaming agent in polylactic acid to prepare polylactic acid structural foam (US Patent No. 5,348,983,1994), but polylactic acid must be made into particles with a smaller particle size before foaming. People such as Kameoka adopt the method for directly extruding by mixing chemical blowing agent and physical blowing agent to prepare polylactic acid foam (US Patent 5763098,1998), but property is brittle, and impact resistance is not good.

发明内容 Contents of the invention

本发明的目的是提供一种工艺要求低、耐冲击性能好的可降解吸塑用聚乳酸泡沫塑料片材及其制备方法。The purpose of the present invention is to provide a degradable polylactic acid foam sheet for plastic absorption with low process requirements and good impact resistance and a preparation method thereof.

本发明提出的一种吸塑用聚乳酸泡沫塑料片材,由挤出机直接挤出,发泡定型而制备获得,其原料组分按重量配比如下:A polylactic acid foam sheet for plastic absorption proposed by the present invention is directly extruded by an extruder and prepared by foaming and shaping, and its raw material components are proportioned as follows by weight:

聚乳酸树脂        100,Polylactic acid resin 100,

扩链剂            0.2-2,Chain extender 0.2-2,

成核剂            0.1-5,Nucleating agent 0.1-5,

发泡剂            0.3-2.5,Foaming agent 0.3-2.5,

增韧剂            0.5-15,Toughener 0.5-15,

抗氧剂            0.1-1,Antioxidant 0.1-1,

增强剂            0.5-5。Enhancer 0.5-5.

本发明中,所述泡沫塑料片材的表观密度为0.40g/cm3-1.0g/cm3之间。In the present invention, the apparent density of the foam plastic sheet is between 0.40 g/cm 3 and 1.0 g/cm 3 .

本发明中,所述的树脂为左旋光或者消旋光性聚乳酸树脂,数均分子量在3—15万之间,分子量分布为1-2,结晶度在20-60%。In the present invention, the resin is levorotatory or de-optical polylactic acid resin, the number average molecular weight is between 30,000 and 150,000, the molecular weight distribution is 1-2, and the crystallinity is 20-60%.

本发明中,所述的扩链剂是丁二醇、甲苯二异氰酸酯(TDI)、苯二甲撑二异氰酸酯(XDI)、二苯基甲烷二异氰酸酯(MDI)中1种或几种的混合物。In the present invention, the chain extender is one or a mixture of butanediol, toluene diisocyanate (TDI), xylylene diisocyanate (XDI), and diphenylmethane diisocyanate (MDI).

本发明中,所述的成核剂是蒙脱土、滑石粉、碳酸钙、碳酸镁、二氧化钛、陶土、云母中1种或几种混合物构成。所述蒙脱土为蒙皂石粘土(包括钙基、钠基、钠-钙基、镁基蒙粘土)经剥片分散、提纯改型、超细分级、有机复合而成,平均晶片厚度小于25nm,蒙脱石含量大于95%。In the present invention, the nucleating agent is composed of one or more mixtures of montmorillonite, talc, calcium carbonate, magnesium carbonate, titanium dioxide, pottery clay and mica. The montmorillonite is made of smectite clay (including calcium-based, sodium-based, sodium-calcium-based, magnesium-based montmorillonite clay) after peeling and dispersing, purification and modification, ultra-fine classification, and organic compounding, with an average wafer thickness of less than 25nm , The montmorillonite content is greater than 95%.

本发明中,所述发泡剂为AC发泡剂,分解温度在140℃—190℃之间。In the present invention, the foaming agent is an AC foaming agent, and its decomposition temperature is between 140°C and 190°C.

本发明中,所述增韧剂为聚乙二醇(PEG),数均分子量为1000~20000之间,可选用PEG4000,PEG6000中1种或2种混合物。In the present invention, the toughening agent is polyethylene glycol (PEG) with a number average molecular weight of 1000-20000, and one or two mixtures of PEG4000 and PEG6000 can be selected.

本发明中,所述抗氧剂为邻苯二酚和对苯二酚中1种或2种混合物。In the present invention, the antioxidant is one or a mixture of catechol and hydroquinone.

本发明中,所述增强剂为甲基纤维素或乙基纤维素中1种或2种混合物成。In the present invention, the reinforcing agent is one or a mixture of methyl cellulose or ethyl cellulose.

本发明提出的吸塑用聚乳酸泡沫塑料片材的制备方法,具体步骤如下:The preparation method of the plastic-absorbing polylactic acid foam sheet that the present invention proposes, concrete steps are as follows:

(1)按计量将聚乳酸、成核剂、扩链剂、抗氧剂混合均匀,用挤出机挤出制成母料,冷却切粒;(1) Mix polylactic acid, nucleating agent, chain extender and antioxidant uniformly by metering, extrude with an extruder to make a masterbatch, cool and cut into pellets;

(2)按计量将母料、发泡剂均匀混合,用挤出机挤出发泡,挤出过程中向挤出机中注入增韧剂和增强剂,挤出机的温度控制在160—220℃之间,挤出得泡沫,冷却;(2) Evenly mix the masterbatch and foaming agent according to the measurement, extrude foaming with an extruder, inject toughening agent and reinforcing agent into the extruder during extrusion, and control the temperature of the extruder at 160- Between 220°C, extrude foam and cool;

(3)单向拉伸,定型,切割,展平,卷取,包装。(3) Unidirectional stretching, shaping, cutting, flattening, coiling and packaging.

本发明制备的吸塑用聚乳酸泡沫塑料片材,它是闭孔式泡沫结构,是利用直接挤出过程后单向拉伸定型后得到的。利用此种片材吸塑制备的产品,使用废弃后可自动降解,降解产物对环境友好。本发明生产工艺先进,产品性能良好,原料来源广泛,性价比高。吸塑后产品可用于制作化妆品瓶、农药瓶、饮料瓶、食品包装容器、餐饮具、托盘、真空成型品等,应用十分广泛。原料来源广泛,性价比高,吸塑后产品可用于制作化妆品瓶、农药瓶、饮料瓶、食品包装容器、餐饮具、托盘、真空成型品等,应用十分广泛。The polylactic acid foamed plastic sheet for plastic absorption prepared by the invention has a closed-cell foam structure, and is obtained after unidirectional stretching and setting after a direct extrusion process. Products prepared by blistering of such sheets can be automatically degraded after use and discarded, and the degradation products are environmentally friendly. The invention has advanced production technology, good product performance, wide source of raw materials and high cost performance. Blistered products can be used to make cosmetic bottles, pesticide bottles, beverage bottles, food packaging containers, tableware, trays, vacuum formed products, etc., and are widely used. Wide range of sources of raw materials, high cost performance, the products after blister can be used to make cosmetic bottles, pesticide bottles, beverage bottles, food packaging containers, tableware, trays, vacuum forming products, etc., which are widely used.

以下将通过本发明的实例来进一步详细的说明本发明。在实例中,除非另外指明分数和百分比均以重量计。但是不发明并不局限于这些实例。The following will illustrate the present invention in further detail through the examples of the present invention. In the examples, parts and percentages are by weight unless otherwise indicated. But the invention is not limited to these examples.

具体实施方式 Detailed ways

有必要指出下列实施例只用于对本发明进行进一步说明,不能理解为对本发明保护范围的限制,本领域的技术熟练人员可根据上述内容对本发明做一些非实质性改进和调整。It is necessary to point out that the following examples are only used to further illustrate the present invention, and should not be interpreted as limiting the protection scope of the present invention. Those skilled in the art can make some non-essential improvements and adjustments to the present invention according to the foregoing.

实施例1Example 1

将有聚乳酸树脂(上海同杰良生物材料有限公司,数均分子量3—15万)100重量份和扩链剂甲苯二异氰酸酯0.5重量份、成核剂蒙脱土(钠基)2重量份、抗氧剂对苯二酚0.5重量份组成的原料混合均匀,加入到挤出机中进行挤出,挤出机温度为160—200℃,主机转速为850rpm,螺杆的转速为30rpm,制得母料冷却切粒。将母料、发泡剂0.3重量份均匀混合加入到挤出机中进行挤出发泡,挤出温度以及主机转速、螺杆转速同上,挤出过程中通过计量泵加入增韧剂聚乙二醇(PEG4000)2重量份,甲基纤维素0.5重量份。挤出得泡沫,冷却,单向拉伸、定型、切割、展平、牵引后卷取。拉伸比率为5%,牵引速度为28rpm,所得产品规格为:厚度3mm,宽度800mm。将片材制成标准样条(140mm×10mm×4mm),于恒温、恒湿的条件下,拉伸速度为5.0/(mm/min),测得的拉伸强度为30Mpa,断裂伸长率为5%。片材表观密度为0.75g/cm3。生物降解试验证实,可以完全降解。There will be 100 parts by weight of polylactic acid resin (Shanghai Tongjieliang Biomaterials Co., Ltd., number average molecular weight 3-150,000), 0.5 parts by weight of chain extender toluene diisocyanate, and 2 parts by weight of nucleating agent montmorillonite (sodium base) , Antioxidant hydroquinone 0.5 parts by weight of raw materials are mixed evenly, added to the extruder and extruded, the temperature of the extruder is 160-200 ℃, the speed of the host is 850rpm, and the speed of the screw is 30rpm. The masterbatch is cooled and diced. Evenly mix the masterbatch and 0.3 parts by weight of the foaming agent and add them to the extruder for extrusion and foaming. The extrusion temperature, the speed of the main engine, and the speed of the screw are the same as above, and the toughening agent polyethylene glycol is added through a metering pump during the extrusion process. (PEG4000) 2 parts by weight, 0.5 parts by weight of methylcellulose. Extruded foam, cooling, unidirectional stretching, shaping, cutting, flattening, traction and coiling. The stretch ratio is 5%, the pulling speed is 28rpm, and the specifications of the obtained product are: thickness 3mm, width 800mm. The sheet is made into a standard sample (140mm×10mm×4mm), under constant temperature and humidity conditions, the tensile speed is 5.0/(mm/min), the measured tensile strength is 30Mpa, and the elongation at break 5%. The apparent density of the sheet was 0.75 g/cm 3 . Biodegradation test confirmed that it can be completely degraded.

实施例2Example 2

将有聚乳酸树脂(上海同杰良生物材料有限公司,数均分子量3—15万)100重量份,扩链剂甲苯二异氰酸酯0.5重量份、成核剂蒙脱土(钠基)4重量份,抗氧剂邻苯二酚0.5重量份组成的原料混合均匀,加入到挤出机中进行挤出,挤出机温度为180—220℃,主机转速为850rpm,螺杆的转速为30rpm,制得母料,冷却切粒。将母料、发泡剂0.5重量份均匀混合加入到挤出机中进行挤出发泡,挤出温度以及主机转速、螺杆转速同上,挤出过程中通过计量泵加入聚乙二醇(PEG4000)2.5重量份,聚乙二醇(PEG6000)2.5重量份,甲基纤维素1重量份。挤出得泡沫经冷却、单向拉伸、定型、切割、展平、牵引后卷取。拉伸比率为5%,牵引速度为30rpm,所得产品规格为:厚度2.8mm,宽度800mm。将片材制成标准样条(140mm×10mm×4mm),于恒温、恒湿的条件下,拉伸速度为5.0/(mm/min),测得的拉伸强度为28Mpa,断裂伸长率为5.6%。片材表观密度为0.71g/cm3。生物降解试验证实,可以完全降解。There will be 100 parts by weight of polylactic acid resin (Shanghai Tongjieliang Biomaterials Co., Ltd., number average molecular weight 3-150,000), 0.5 parts by weight of chain extender toluene diisocyanate, 4 parts by weight of nucleating agent montmorillonite (sodium base) , the raw materials composed of 0.5 parts by weight of antioxidant catechol are mixed evenly, and then added to the extruder for extrusion. Masterbatch, cooled and diced. Mix the masterbatch and 0.5 parts by weight of foaming agent evenly and add them to the extruder for extrusion and foaming. The extrusion temperature, the speed of the host machine and the speed of the screw are the same as above, and polyethylene glycol (PEG4000) is added through a metering pump during the extrusion process. 2.5 parts by weight, 2.5 parts by weight of polyethylene glycol (PEG6000), and 1 part by weight of methylcellulose. The extruded foam is coiled after cooling, unidirectional stretching, shaping, cutting, flattening and traction. The stretch ratio is 5%, the pulling speed is 30rpm, and the specifications of the obtained product are: thickness 2.8mm, width 800mm. The sheet is made into a standard sample (140mm×10mm×4mm), under constant temperature and humidity conditions, the tensile speed is 5.0/(mm/min), the measured tensile strength is 28Mpa, and the elongation at break was 5.6%. The apparent density of the sheet was 0.71 g/cm 3 . Biodegradation test confirmed that it can be completely degraded.

实施例3Example 3

将有聚乳酸树脂(上海同杰良生物材料有限公司,数均分子量3—15万)100重量份,扩链剂甲苯二异氰酸酯0.5重量份、苯二甲撑二异氰酸酯0.5重量份,成核剂蒙脱土(钠基)5重量份,抗氧剂邻苯二酚0.5重量份和对苯二酚0.5重量份组成的原料混合均匀,加入到挤出机中进行挤出,挤出机温度为170—210℃,主机转速为850rpm,螺杆的转速为30rpm,制得母料,冷却切粒。将母料、发泡剂0.7重量份均匀混合加入到挤出机中进行挤出发泡,挤出温度以及主机转速、螺杆转速同上,挤出过程中通过计量泵加入增韧剂聚乙二醇(PEG4000)5重量份、聚乙二醇(PEG6000)5重量份,增强剂甲基纤维素1.5重量份。挤出得泡沫,冷却,单向拉伸、定型、切割、展平、牵引后卷取。拉伸比率为5%,牵引速度为35rpm,所得产品规格为:厚度2.5mm,宽度800mm。将片材制成标准样条(140mm×10mm×4mm),于恒温、恒湿的条件下,拉伸速度为5.0/(mm/min),测得的拉伸强度为25Mpa,断裂伸长率为6.2%。片材表观密度为0.67g/cm3。生物降解试验证实,可以完全降解。There will be 100 parts by weight of polylactic acid resin (Shanghai Tongjieliang Biomaterials Co., Ltd., number average molecular weight 3-150,000), 0.5 parts by weight of chain extender toluene diisocyanate, 0.5 parts by weight of xylylene diisocyanate, nucleating agent 5 parts by weight of montmorillonite (sodium base), 0.5 parts by weight of antioxidant catechol and 0.5 parts by weight of hydroquinone are mixed evenly, and are added into an extruder to extrude, and the extruder temperature is 170—210°C, the speed of the main machine is 850rpm, the speed of the screw is 30rpm, the masterbatch is prepared, cooled and diced. Evenly mix the masterbatch and 0.7 parts by weight of the foaming agent and add them to the extruder for extrusion foaming. The extrusion temperature, the speed of the main engine, and the speed of the screw are the same as above. During the extrusion process, the toughening agent polyethylene glycol is added through a metering pump. (PEG4000) 5 parts by weight, polyethylene glycol (PEG6000) 5 parts by weight, reinforcing agent methylcellulose 1.5 parts by weight. Extruded foam, cooling, unidirectional stretching, shaping, cutting, flattening, traction and coiling. The stretching ratio is 5%, the pulling speed is 35 rpm, and the specifications of the obtained product are: thickness 2.5 mm, width 800 mm. The sheet is made into a standard sample (140mm×10mm×4mm), under constant temperature and humidity conditions, the tensile speed is 5.0/(mm/min), the measured tensile strength is 25Mpa, and the elongation at break was 6.2%. The apparent density of the sheet was 0.67 g/cm 3 . Biodegradation test confirmed that it can be completely degraded.

实施例4Example 4

将有聚乳酸树脂(上海同杰良生物材料有限公司,数均分子量3—15万)100重量份和扩链剂苯二甲撑二异氰酸酯0.5重量份、二苯基甲烷二异氰酸酯0.5重量份,成核剂滑石粉5重量份,抗氧剂对苯二酚1重量份组成的原料混合均匀,加入到挤出机中进行挤出,挤出机温度为160—210℃,主机转速为1000rpm,螺杆的转速为40rpm,制得母料,冷却切粒。将母料、发泡剂1.0重量份均匀混合加入到挤出机中进行挤出发泡,挤出温度以及主机转速、螺杆转速同上,挤出过程中通过计量泵加入增韧剂聚乙二醇(PEG4000)7.5重量份、聚乙二醇(PEG6000)2.5重量份,增强剂甲基纤维素1.5重量份。挤出得泡沫,冷却,单向拉伸、定型、切割、展平、牵引后卷取。拉伸比率为5%,牵引速度为35rpm,所得产品规格为:厚度2.7mm,宽度800mm。将片材制成标准样条(140mm×10mm×4mm),于恒温、恒湿的条件下,拉伸速度为5.0/(mm/min),测得的拉伸强度为22Mpa,断裂伸长率为6.7%。片材表观密度为0.61g/cm3。生物降解试验证实,可以完全降解。There will be 100 parts by weight of polylactic acid resin (Shanghai Tongjieliang Biomaterials Co., Ltd., number average molecular weight 3-150,000) and 0.5 parts by weight of chain extender xylylene diisocyanate and 0.5 parts by weight of diphenylmethane diisocyanate, The raw materials consisting of 5 parts by weight of nucleating agent talcum powder and 1 part by weight of antioxidant hydroquinone are mixed evenly, and then added to the extruder for extrusion. The rotation speed of the screw is 40rpm, and the masterbatch is prepared, cooled and diced. Evenly mix the masterbatch and 1.0 parts by weight of the foaming agent and add them to the extruder for extrusion and foaming. The extrusion temperature, the speed of the main engine, and the speed of the screw are the same as above. During the extrusion process, the toughening agent polyethylene glycol is added through a metering pump. (PEG4000) 7.5 parts by weight, polyethylene glycol (PEG6000) 2.5 parts by weight, reinforcing agent methylcellulose 1.5 parts by weight. Extruded foam, cooling, unidirectional stretching, shaping, cutting, flattening, traction and coiling. The stretching ratio is 5%, the pulling speed is 35 rpm, and the specifications of the obtained product are: thickness 2.7 mm, width 800 mm. The sheet is made into a standard sample (140mm×10mm×4mm), under constant temperature and humidity conditions, the tensile speed is 5.0/(mm/min), the measured tensile strength is 22Mpa, and the elongation at break was 6.7%. The apparent density of the sheet was 0.61 g/cm 3 . Biodegradation test confirmed that it can be completely degraded.

实施例5Example 5

将有聚乳酸树脂(上海同杰良生物材料有限公司,数均分子量3—15万)100重量份和扩链剂甲苯二异氰酸酯1重量份、二苯基甲烷二异氰酸酯1重量份,成核剂蒙脱土7.5(钠基)重量份、抗氧剂对苯二酚1重量份组成的原料混合均匀,加入到挤出机中进行挤出,挤出机温度为160—200℃,主机转速为1000rpm,螺杆的转速为40rpm,制得母料,冷却切粒。将母料、发泡剂1.5重量份均匀混合加入到挤出机中进行挤出发泡,挤出温度以及主机转速、螺杆转速同上,挤出过程中通过计量泵加入增韧剂聚乙二醇(PEG4000)10重量份、聚乙二醇(PEG6000)5重量份,甲基纤维素3重量份。挤出得泡沫,冷却,单向拉伸、定型、切割、展平、牵引后卷取。拉伸比率为5%,牵引速度为40rpm,所得产品规格为:厚度2.3mm,宽度800mm。将片材制成标准样条(140mm×10mm×4mm),于恒温、恒湿的条件下,拉伸速度为5.0/(mm/min),测得的拉伸强度为23Mpa,断裂伸长率为5.9%。片材表观密度为0.55g/cm3。生物降解试验证实,可以完全降解。There will be 100 parts by weight of polylactic acid resin (Shanghai Tongjieliang Biomaterials Co., Ltd., number average molecular weight 3-150,000), 1 part by weight of chain extender toluene diisocyanate, 1 part by weight of diphenylmethane diisocyanate, nucleating agent The raw materials consisting of 7.5 parts by weight of montmorillonite (sodium base) and 1 part by weight of antioxidant hydroquinone are mixed evenly, and then added to the extruder for extrusion. 1000rpm, the rotation speed of the screw is 40rpm, the masterbatch is prepared, cooled and diced. Evenly mix the masterbatch and 1.5 parts by weight of the foaming agent and add them to the extruder for extrusion and foaming. The extrusion temperature, the speed of the main engine, and the speed of the screw are the same as above. During the extrusion process, the toughening agent polyethylene glycol is added through a metering pump. (PEG4000) 10 parts by weight, polyethylene glycol (PEG6000) 5 parts by weight, methylcellulose 3 parts by weight. Extruded foam, cooling, unidirectional stretching, shaping, cutting, flattening, traction and coiling. The stretch ratio is 5%, the pulling speed is 40rpm, and the specifications of the obtained product are: thickness 2.3mm, width 800mm. The sheet is made into a standard sample (140mm×10mm×4mm), under constant temperature and humidity conditions, the tensile speed is 5.0/(mm/min), the measured tensile strength is 23Mpa, and the elongation at break was 5.9%. The apparent density of the sheet was 0.55 g/cm 3 . Biodegradation test confirmed that it can be completely degraded.

实施例6Example 6

将有聚乳酸树脂(上海同杰良生物材料有限公司,数均分子量3-15万)100重量份和扩链剂二苯基甲烷二异氰酸酯1重量份,成核剂蒙脱土(钠基)5重量份、抗氧剂对苯二酚1重量份组成的原料混合均匀,加入到挤出机中进行挤出,挤出机温度为180—220℃,主机转速为850rpm,螺杆的转速为30rpm,制得母料,冷却切粒。将母料、发泡剂0.5重量份均匀混合加入到挤出机中进行挤出发泡,挤出温度以及主机转速、螺杆转速同上,挤出过程中通过计量泵加入增韧剂聚乙二醇(PEG4000)15重量份,增强剂乙基纤维素5重量份。挤出得泡沫,冷却,单向拉伸、定型、切割、展平、牵引后卷取。拉伸比率为5%,牵引速度为28rpm,所得产品规格为:厚度2.8mm,宽度800mm。将片材制成标准样条(140mm×10mm×4mm),于恒温、恒湿的条件下,拉伸速度为5.0/(mm/min),测得的拉伸强度为17Mpa,断裂伸长率为7.5%。片材表观密度为0.66g/cm3。生物降解试验证实,可以完全降解。There will be 100 parts by weight of polylactic acid resin (Shanghai Tongjieliang Biological Materials Co., Ltd., number average molecular weight 3-150,000) and 1 part by weight of chain extender diphenylmethane diisocyanate, nucleating agent montmorillonite (sodium base) The raw materials consisting of 5 parts by weight and 1 part by weight of antioxidant hydroquinone are mixed evenly, and then added to the extruder for extrusion. , to prepare the masterbatch, cooling and dicing. Evenly mix the masterbatch and 0.5 parts by weight of the foaming agent and add them to the extruder for extrusion and foaming. The extrusion temperature, the speed of the main engine, and the speed of the screw are the same as above. During the extrusion process, the toughening agent polyethylene glycol is added through a metering pump. (PEG4000) 15 parts by weight, reinforcing agent ethyl cellulose 5 parts by weight. Extruded foam, cooling, unidirectional stretching, shaping, cutting, flattening, traction and coiling. The stretch ratio is 5%, the pulling speed is 28rpm, and the specifications of the obtained product are: thickness 2.8mm, width 800mm. The sheet is made into a standard sample (140mm×10mm×4mm), under constant temperature and humidity conditions, the tensile speed is 5.0/(mm/min), the measured tensile strength is 17Mpa, and the elongation at break 7.5%. The apparent density of the sheet was 0.66 g/cm 3 . Biodegradation test confirmed that it can be completely degraded.

Claims (3)

1.一种吸塑用聚乳酸泡沫塑料片材,其特征在于由挤出机直接挤出,发泡定型而制备获得,其原料组分按重量配比如下:1. A polylactic acid foamed plastic sheet for plastic absorption is characterized in that it is directly extruded by an extruder, and is prepared by foaming and shaping, and its raw material components are as follows by weight: 聚乳酸树脂        100,Polylactic acid resin 100, 扩链剂            0.2-2,Chain extender 0.2-2, 成核剂            0.1-5,Nucleating agent 0.1-5, 发泡剂            0.3-2.5,Foaming agent 0.3-2.5, 增韧剂            0.5-15,Toughener 0.5-15, 增强剂            0.5-5,Enhancer 0.5-5, 抗氧剂            0.1-1;Antioxidant 0.1-1; 该泡沫塑料片材的表观密度为0.40g/cm3-1.0g/cm3之间;The apparent density of the foam plastic sheet is between 0.40g/cm 3 and 1.0g/cm 3 ; 所述的树脂为左旋光或者消旋光性聚乳酸树脂,数均分子量3—15万之间,分子量分布为1-2,结晶度在20-60%;The resin is levorotatory or de-optical polylactic acid resin, with a number average molecular weight of 30,000-150,000, a molecular weight distribution of 1-2, and a crystallinity of 20-60%; 所述的扩链剂是丁二醇、甲苯二异氰酸酯、苯二甲撑二异氰酸酯、二苯基甲烷二异氰酸酯中1种或几种的混合物;The chain extender is a mixture of one or more of butylene glycol, toluene diisocyanate, xylylene diisocyanate, and diphenylmethane diisocyanate; 所述的成核剂是:蒙脱土、滑石粉、碳酸钙、碳酸镁、二氧化钛、陶土、云母中1种或几种的混合物;The nucleating agent is: montmorillonite, talcum powder, calcium carbonate, magnesium carbonate, titanium dioxide, pottery clay, mica one or more of the mixture; 所述发泡剂为AC发泡剂,分解温度在140℃—190℃之间;The foaming agent is an AC foaming agent, and its decomposition temperature is between 140°C and 190°C; 所述增韧剂为聚乙二醇,数均分子量为1000-20000之间;The toughening agent is polyethylene glycol, and the number average molecular weight is between 1000-20000; 所述抗氧剂为邻苯二酚和对苯二酚中1种或2种的混合物;The antioxidant is a mixture of one or two of catechol and hydroquinone; 所述增强剂为甲基纤维素或乙基纤维素中1种或2种的混合物。The reinforcing agent is a mixture of one or two of methylcellulose or ethylcellulose. 2.根据权利要求1所述的吸塑用聚乳酸泡沫塑料片材,其特征在于所述的蒙脱土为蒙皂石粘土经剥片分散、提纯改型、超细分级、有机复合而成,平均晶片厚度小于25nm,蒙脱石含量大于95%。2. the polylactic acid foam plastic sheet for plastic absorption according to claim 1, is characterized in that described montmorillonite is that montmorillonite clay forms through stripping and dispersing, purifying and remodeling, superfine classification, and organic compounding, The average wafer thickness is less than 25nm, and the montmorillonite content is greater than 95%. 3.一种如权利要求1所述的吸塑用聚乳酸泡沫塑料片材的制备方法,其特征在于具体步骤如下:3. a preparation method of plastic-absorbing polylactic acid foam sheet as claimed in claim 1, is characterized in that concrete steps are as follows: (1)按计量将聚乳酸、成核剂、扩链剂、抗氧剂混合均匀,用挤出机挤出制成母料,冷却切粒;(1) Mix polylactic acid, nucleating agent, chain extender and antioxidant uniformly by metering, extrude with an extruder to make a masterbatch, cool and cut into pellets; (2)按计量将母料、发泡剂均匀混合,用挤出机挤出发泡,挤出过程中向挤出机中注入增韧剂和增强剂,挤出机的温度控制在160—220℃之间,挤出得泡沫,冷却;(2) Evenly mix the masterbatch and foaming agent according to the measurement, extrude foaming with an extruder, inject toughening agent and reinforcing agent into the extruder during extrusion, and control the temperature of the extruder at 160- Between 220°C, extrude foam and cool; (3)单向拉伸,定型,切割,展平,卷取,包装。(3) Unidirectional stretching, shaping, cutting, flattening, coiling and packaging.
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