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CN110746635A - A kind of composite starch foaming microbeads and preparation method thereof - Google Patents

A kind of composite starch foaming microbeads and preparation method thereof Download PDF

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CN110746635A
CN110746635A CN201911139433.4A CN201911139433A CN110746635A CN 110746635 A CN110746635 A CN 110746635A CN 201911139433 A CN201911139433 A CN 201911139433A CN 110746635 A CN110746635 A CN 110746635A
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starch
foaming
foamed
composite
matrix
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曾广胜
江太君
孟聪
胡灿
陈一
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Hunan University of Technology
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/22After-treatment of expandable particles; Forming foamed products
    • C08J9/228Forming foamed products
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C08J9/10Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen, the blowing agent being a compound containing a nitrogen-to-nitrogen bond
    • C08J9/102Azo-compounds
    • C08J9/103Azodicarbonamide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C08J9/10Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen, the blowing agent being a compound containing a nitrogen-to-nitrogen bond
    • C08J9/104Hydrazines; Hydrazides; Semicarbazides; Semicarbazones; Hydrazones; Derivatives thereof
    • C08J9/105Hydrazines; Hydrazides; Semicarbazides; Semicarbazones; Hydrazones; Derivatives thereof containing sulfur
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/04N2 releasing, ex azodicarbonamide or nitroso compound
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2303/00Characterised by the use of starch, amylose or amylopectin or of their derivatives or degradation products
    • C08J2303/02Starch; Degradation products thereof, e.g. dextrin
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2367/02Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2367/04Polyesters derived from hydroxy carboxylic acids, e.g. lactones
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2403/00Characterised by the use of starch, amylose or amylopectin or of their derivatives or degradation products
    • C08J2403/02Starch; Degradation products thereof, e.g. dextrin
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2467/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2467/02Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2467/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2467/04Polyesters derived from hydroxy carboxylic acids, e.g. lactones

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  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Biological Depolymerization Polymers (AREA)

Abstract

The invention discloses a composite starch foaming microbead and a preparation method thereof. According to the invention, the chemical foaming agent is added into the thermoplastic starch material and prepared into micro-particles, and then a layer of fully-degradable plastic film is coated outside the thermoplastic starch material to form the controllable foaming micro-beads, so that the preparation method can be widely applied to preparation of the full-starch or starch-based foaming composite material, and the production process is stable and controllable.

Description

一种复合淀粉发泡微珠及其制备方法A kind of composite starch foaming microbeads and preparation method thereof

技术领域technical field

本发明涉及发泡材料技术领域,更具体地,涉及一种复合淀粉发泡微珠及其制作方法。The invention relates to the technical field of foaming materials, and more particularly, to a composite starch foaming microbead and a preparation method thereof.

背景技术Background technique

淀粉是一种来自于自然植物的可再生可循环的绿色材料,其不仅可以作为粮食供人类食用,也被广泛应用于化工与新材料领域用于制备各类复合材料。因其优异的可生物降解性能,淀粉通常作为填充来制备热塑性高生物碳含量生物基复合材料,广泛应用于一次性用品,在当前石化资源日益短缺,白色污染日益严重的大环境下越来越受到人们的重视。采用淀粉为原材料制备热塑性的复合材料,因为淀粉的密度较大,经塑化压实的复合材料综合密度可以达到1.4g/cm3左右,相对于塑胶材料在运输与材料成本核算方面都没有优势。很有必要对淀粉基复合材料进行发泡处理,制备出密度与传统塑料相近或低于传统塑料的复合发泡材料,则可以大大拓展淀粉基复合材料的应用,并在更多的领域取代传统的塑料,对缓解塑料污染具有非常重要的意义。Starch is a renewable and recyclable green material from natural plants. It can not only be used as food for human consumption, but also widely used in the fields of chemical industry and new materials to prepare various composite materials. Because of its excellent biodegradability, starch is usually used as filler to prepare thermoplastic high biocarbon content bio-based composites, which are widely used in disposable products. people's attention. Using starch as raw material to prepare thermoplastic composite materials, because of the high density of starch, the comprehensive density of plasticized and compacted composite materials can reach about 1.4g/cm3, which has no advantages in transportation and material cost accounting compared with plastic materials. It is necessary to foam the starch-based composite materials to prepare composite foamed materials with a density similar to or lower than that of traditional plastics, which can greatly expand the application of starch-based composite materials and replace traditional plastics in more fields. It is of great significance to alleviate plastic pollution.

目前对淀粉基复合材料进行发泡设计的方法一般有两种,一种是添加化学发泡剂,即在均质化淀粉基复合材料的配方中加入AC等化发发泡剂在成型过程中化学发泡剂受热分解释放出气体并均匀分散于复合材料中,气体在成核剂的作用下发展成为泡,并在复合材料内部形成气孔,从而形成具有泡孔结构的发泡材料,这种技术主要应用于注塑成型工艺。另一种工艺是物理发泡,即在熔融的淀粉基复合材料的成型过程中强制向熔体内部通往超临界二氧化碳或其它类型气体,在外力的剪切或搅拌作用下使气体均匀分而于复合材料熔体内部,并迅速发展成为气泡,在复合材料内部形成泡孔。但这两种工艺对成型设备与材料配方的调配均有非常高的要求,生产过程不易控制,对于基体熔体强度低的材料无法实现。很有必须设计一种更加简单易控的发泡工艺与方法来制备低密度淀粉基复合材料。At present, there are generally two methods for foaming design of starch-based composite materials. One is to add chemical foaming agents, that is, adding AC and other chemical foaming agents to the formula of homogenized starch-based composite materials. During the molding process The chemical foaming agent is heated to decompose to release gas and evenly disperse in the composite material. The gas develops into bubbles under the action of the nucleating agent, and forms pores inside the composite material, thereby forming a foamed material with a cell structure. The technology is mainly used in the injection molding process. Another process is physical foaming, that is, during the molding process of the molten starch-based composite material, supercritical carbon dioxide or other types of gas are forced into the melt, and the gas is uniformly distributed under the action of external force shearing or stirring. Inside the melt of the composite material, and rapidly develop into bubbles, forming cells inside the composite material. However, these two processes have very high requirements on the deployment of molding equipment and material formulations, the production process is not easy to control, and cannot be realized for materials with low matrix melt strength. It is very necessary to design a more simple and controllable foaming process and method to prepare low-density starch-based composites.

发明内容SUMMARY OF THE INVENTION

本发明的目的在于针对现有技术中的不足,提供一种复合淀粉发泡微珠,密度低,可取代传统的塑料。The purpose of the present invention is to aim at the deficiencies in the prior art, and to provide a composite starch foaming microbead with low density, which can replace traditional plastics.

本发明的另一目的在于提供上述复合淀粉发泡微珠的制备方法。Another object of the present invention is to provide a method for preparing the above-mentioned composite starch foamed microbeads.

本发明的目的通过以下技术方案实现:The object of the present invention is achieved through the following technical solutions:

一种复合淀粉发泡微珠,包括淀粉发泡基体和全降解塑料膜,所述淀粉发泡机体位于微珠中心,所述全降解塑料膜包覆在发泡基体外部。A composite starch foaming microbead comprises a starch foaming matrix and a fully degradable plastic film, the starch foaming body is located in the center of the microbead, and the fully degradable plastic film is wrapped on the outside of the foaming matrix.

进一步地,所述淀粉发泡基体包括热塑性淀粉和发泡剂。Further, the starch foaming matrix includes thermoplastic starch and foaming agent.

进一步地,所述发泡剂为甲苯磺酰肼、偶氮甲酰胺的至少一种。Further, the foaming agent is at least one of tosyl hydrazide and azocarboxamide.

进一步地,所述全降解塑料膜为PLA、PBAT或PBS的至少一种。Further, the fully degradable plastic film is at least one of PLA, PBAT or PBS.

一种上述复合淀粉发泡微珠的制备方法,包括以下步骤:A preparation method of the above-mentioned composite starch foaming microbeads, comprising the following steps:

S1.将热塑性淀粉和发泡剂高速混合后混炼均匀,得淀粉发泡基体;S1. The thermoplastic starch and the foaming agent are mixed at a high speed and then kneaded evenly to obtain a starch foaming matrix;

S2.将混炼好的淀粉发泡基体在抽粒机中经揉搓、制粒成球形颗粒,得发泡基体颗粒;S2. The kneaded starch foamed matrix is kneaded and granulated into spherical particles in a granulator to obtain foamed matrix particles;

S3.向发泡基体喷射熔融的可降解塑料膜熔体,并高速搅拌至发泡基体表面均匀包覆一层全降解塑料膜,得复合淀粉发泡微珠。S3. Spray the melted degradable plastic film melt to the foamed substrate, and stir at a high speed until the surface of the foamed substrate is evenly coated with a layer of fully degradable plastic film to obtain composite starch foamed microbeads.

进一步地,步骤S1中所述混炼温度为100~140℃。Further, the kneading temperature in step S1 is 100-140°C.

进一步地,步骤S2中所述发泡基体颗粒的粒径为0.2~0.3mm。Further, the particle size of the foamed matrix particles in step S2 is 0.2-0.3 mm.

与现有技术相比,本发明的有益效果如下:Compared with the prior art, the beneficial effects of the present invention are as follows:

本发明通过在热塑性淀粉材料内加入化学发泡剂并制备成微颗粒,然后在在其外部包覆一层全降解塑料膜形成可控发泡微珠,可广泛应用于全淀粉或淀粉基发泡复合材料制备的制备,微珠颗粒直径0.3-0.8mm,制备的发泡复合材料密度可达0.8-1.1g/cm3In the present invention, chemical foaming agent is added into thermoplastic starch material and prepared into micro-particles, and then a layer of fully degradable plastic film is coated on the outside to form controllable foaming micro-beads, which can be widely used in whole starch or starch-based hair In the preparation of the foamed composite material, the diameter of the microbead particles is 0.3-0.8 mm, and the density of the prepared foamed composite material can reach 0.8-1.1 g/cm 3 .

具体实施方式Detailed ways

为了便于理解本发明,下文将结合实施例对本发明作更全面、细致地描述,但本发明的保护范围并不限于以下具体的实施例。In order to facilitate the understanding of the present invention, the present invention will be described more comprehensively and in detail below with reference to the embodiments, but the protection scope of the present invention is not limited to the following specific embodiments.

除非另有定义,下文中所使用的所有专业术语与本领域技术人员通常理解的含义相同。本文中所使用的专业术语只是为了描述具体实施例的目的,并不旨在限制本发明的保护范围。Unless otherwise defined, all technical terms used hereinafter have the same meaning as commonly understood by those skilled in the art. The technical terms used herein are only for the purpose of describing specific embodiments, and are not intended to limit the protection scope of the present invention.

除非另有特别说明,本发明中用到的各种原材料、试剂、仪器和设备等均可通过市场购买得到或者可通过现有方法制备得到。Unless otherwise specified, various raw materials, reagents, instruments and equipment used in the present invention can be purchased from the market or can be prepared by existing methods.

实施例1Example 1

本实施例提供一种复合淀粉发泡微珠的制备方法,包括以下步骤:The present embodiment provides a preparation method of composite starch foaming microbeads, comprising the following steps:

S1.将热塑性淀粉和甲苯磺酰肼高速混合,甲苯磺酰肼的用量为热塑性淀粉用量的2%,在120℃下混炼均匀,得淀粉发泡基体;S1. Mix thermoplastic starch and tosyl hydrazide at a high speed, the amount of tosyl hydrazide is 2% of the amount of thermoplastic starch, and the mixture is uniformly mixed at 120 ° C to obtain a starch foaming matrix;

S2.将混炼好的淀粉发泡基体在抽粒机中经揉搓、制粒成0.3mm的球形颗粒,得发泡基体颗粒;S2. The kneaded starch foamed matrix is kneaded and granulated into spherical particles of 0.3 mm in a granulator to obtain foamed matrix particles;

S3.向发泡基体喷射熔融的PLA熔体,并高速搅拌至发泡基体表面均匀包覆一层全降解塑料膜,得复合淀粉发泡微珠。S3. Spray the molten PLA melt to the foamed substrate, and stir at a high speed until the surface of the foamed substrate is evenly coated with a layer of fully degradable plastic film to obtain composite starch foamed microbeads.

本实施例制备的微珠粒径为0.6mm,密度为1.0g/cm3The microbeads prepared in this example have a particle size of 0.6 mm and a density of 1.0 g/cm 3 .

实施例2Example 2

本实施例提供一种复合淀粉发泡微珠的制备方法,包括以下步骤:The present embodiment provides a preparation method of composite starch foaming microbeads, comprising the following steps:

S1.将热塑性淀粉和甲苯磺酰肼高速混合,甲苯磺酰肼的用量为热塑性淀粉用量的4%,在140℃下混炼均匀,得淀粉发泡基体;S1. Mix thermoplastic starch and tosyl hydrazide at a high speed, and the amount of tosyl hydrazide is 4% of the amount of thermoplastic starch, and knead uniformly at 140 ° C to obtain a starch foaming matrix;

S2.将混炼好的淀粉发泡基体在抽粒机中经揉搓、制粒成0.2mm的球形颗粒,得发泡基体颗粒;S2. The kneaded starch foamed matrix is kneaded and granulated into spherical particles of 0.2 mm in a granulator to obtain foamed matrix particles;

S3.向发泡基体喷射熔融的PBS熔体,并高速搅拌至发泡基体表面均匀包覆一层全降解塑料膜,得复合淀粉发泡微珠。S3. Spray the molten PBS melt to the foamed substrate, and stir at a high speed until the surface of the foamed substrate is evenly coated with a layer of fully degradable plastic film to obtain composite starch foamed microbeads.

本实施例制备的微珠粒径为0.8mm,密度为1.0g/cm3The microbeads prepared in this example have a particle size of 0.8 mm and a density of 1.0 g/cm 3 .

实施例3Example 3

本实施例提供一种复合淀粉发泡微珠的制备方法,包括以下步骤:The present embodiment provides a preparation method of composite starch foaming microbeads, comprising the following steps:

S1.将热塑性淀粉、偶氮甲酰胺和甲苯磺酰肼高速混合,其中偶氮甲酰胺的用量为热塑性淀粉用量的2%,甲苯磺酰肼的用量为热塑性淀粉用量的1%,在100℃下混炼均匀,得淀粉发泡基体;S1. Mix thermoplastic starch, azoformamide and tosylhydrazide at high speed, wherein the amount of azoformamide is 2% of the amount of thermoplastic starch, and the amount of tosylhydrazide is 1% of the amount of thermoplastic starch, at 100°C The lower mixing is uniform to obtain a starch foaming matrix;

S2.将混炼好的淀粉发泡基体在抽粒机中经揉搓、制粒成0.2mm的球形颗粒,得发泡基体颗粒;S2. The kneaded starch foamed matrix is kneaded and granulated into spherical particles of 0.2 mm in a granulator to obtain foamed matrix particles;

S3.向发泡基体喷射熔融的PBAT熔体,并高速搅拌至发泡基体表面均匀包覆一层全降解塑料膜,得复合淀粉发泡微珠。S3. The molten PBAT melt is sprayed onto the foamed substrate, and stirred at a high speed until the surface of the foamed substrate is evenly coated with a layer of fully degradable plastic film to obtain composite starch foamed microbeads.

本实施例制备的微珠粒径为0.3mm,密度为0.8g/cm3The microbeads prepared in this example have a particle size of 0.3 mm and a density of 0.8 g/cm 3 .

实施例4Example 4

本实施例提供一种复合淀粉发泡微珠的制备方法,包括以下步骤:The present embodiment provides a preparation method of composite starch foaming microbeads, comprising the following steps:

S1.将热塑性淀粉和偶氮甲酰胺高速混合,偶氮甲酰胺的用量为热塑性淀粉用量的5%,在115℃下混炼均匀,得淀粉发泡基体;S1. Mix thermoplastic starch and azoformamide at a high speed, and the amount of azoformamide is 5% of the amount of thermoplastic starch, and knead uniformly at 115 ° C to obtain a starch foaming matrix;

S2.将混炼好的淀粉发泡基体在抽粒机中经揉搓、制粒成0.3mm的球形颗粒,得发泡基体颗粒;S2. The kneaded starch foamed matrix is kneaded and granulated into spherical particles of 0.3 mm in a granulator to obtain foamed matrix particles;

S3.向发泡基体喷射熔融的PLA和PBAT熔体,并高速搅拌至发泡基体表面均匀包覆一层全降解塑料膜,得复合淀粉发泡微珠。S3. The molten PLA and PBAT melts are sprayed onto the foamed substrate, and stirred at a high speed until the surface of the foamed substrate is evenly coated with a layer of fully degradable plastic film to obtain composite starch foamed microbeads.

本实施例制备的微珠粒径为0.5mm,密度为1.1g/cm3The microbeads prepared in this example have a particle size of 0.5 mm and a density of 1.1 g/cm 3 .

显然,上述实施例仅仅是为清楚地说明本发明的技术方案所作的举例,而并非是对本发明的实施方式的限定。对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其它不同形式的变化或变动。这里无需也无法对所有的实施方式予以穷举。凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明权利要求的保护范围之内。Obviously, the above-mentioned embodiments are only examples for clearly illustrating the technical solutions of the present invention, and are not intended to limit the embodiments of the present invention. For those of ordinary skill in the art, changes or modifications in other different forms can also be made on the basis of the above description. There is no need and cannot be exhaustive of all implementations here. Any modifications, equivalent replacements and improvements made within the spirit and principle of the present invention shall be included within the protection scope of the claims of the present invention.

Claims (7)

1.一种复合淀粉发泡微珠,其特征在于,包括淀粉发泡基体和全降解塑料膜,所述淀粉发泡机体位于微珠中心,所述全降解塑料膜包覆在发泡基体外部。1. a composite starch foaming microbead, is characterized in that, comprises starch foaming matrix and fully degradable plastic film, described starch foaming body is positioned at the center of microbead, and described fully degradable plastic film is wrapped outside the foaming matrix . 2.根据权利要求1所述的复合淀粉发泡微珠,其特征在于,所述淀粉发泡基体包括热塑性淀粉和发泡剂。2 . The composite starch foaming microbeads according to claim 1 , wherein the starch foaming matrix comprises thermoplastic starch and a foaming agent. 3 . 3.根据权利要求2所述的复合淀粉发泡微珠,其特征在于,所述发泡剂为甲苯磺酰肼、偶氮甲酰胺的至少一种。3 . The composite starch foaming microbeads according to claim 2 , wherein the foaming agent is at least one of tosyl hydrazide and azocarboxamide. 4 . 4.根据权利要求1所述的复合淀粉发泡微珠,其特征在于,所述全降解塑料膜为PLA、PBAT或PBS的至少一种。4 . The composite starch foamed microbeads according to claim 1 , wherein the fully degradable plastic film is at least one of PLA, PBAT or PBS. 5 . 5.一种权利要求1~4任一项所述的复合淀粉发泡微珠的制备方法,其特征在于,包括以下步骤:5. the preparation method of the composite starch foaming microbeads described in any one of claim 1~4, is characterized in that, comprises the following steps: S1.将热塑性淀粉和发泡剂高速混合均匀后混炼均匀,得淀粉发泡基体;S1. Mix the thermoplastic starch and the foaming agent at a high speed and then mix them evenly to obtain a starch foaming matrix; S2.将混炼好的淀粉发泡基体在抽粒机中经揉搓、制粒成球形颗粒,得发泡基体颗粒;S2. The kneaded starch foamed matrix is kneaded and granulated into spherical particles in a granulator to obtain foamed matrix particles; S3.向发泡基体喷射熔融的可降解塑料膜熔体,并高速搅拌至发泡基体表面均匀包覆一层全降解塑料膜,得复合淀粉发泡微珠。S3. Spray the melted degradable plastic film melt to the foamed substrate, and stir at a high speed until the surface of the foamed substrate is evenly coated with a layer of fully degradable plastic film to obtain composite starch foamed microbeads. 6.根据权利要求5所述的制备方法,其特征在于,步骤S1中所述混炼温度为100~140℃。6 . The preparation method according to claim 5 , wherein the mixing temperature in step S1 is 100-140° C. 7 . 7.根据权利要求5所述的制备方法,其特征在于,步骤S2中所述发泡基体颗粒的粒径为0.2~0.3mm。7 . The preparation method according to claim 5 , wherein the particle size of the foamed matrix particles in step S2 is 0.2 to 0.3 mm. 8 .
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Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1112143A (en) * 1994-02-09 1995-11-22 诺瓦蒙特股份公司 Expanded articles of biodegradable plastic material and a process for the preparation thereof
CN1800249A (en) * 2005-01-05 2006-07-12 项爱民 Biodegradable starch-base foaming composition and foaming product containing same
CN101522768A (en) * 2006-10-11 2009-09-02 巴斯夫欧洲公司 Coated foam beads and process for producing halogen-free, fire-resistant bead foam moldings
CN101668798A (en) * 2007-04-19 2010-03-10 辛伯拉技术有限公司 The inflatable particulate poly(lactic acid) that applies
CN102206361A (en) * 2011-04-27 2011-10-05 广东益德环保科技有限公司 Fully-degradable foam material using starch as base material and preparation method for fully-degradable foam material
WO2012008784A2 (en) * 2010-07-15 2012-01-19 대상 주식회사 Expandable starch bead and method for preparing same
CN102702562A (en) * 2012-05-24 2012-10-03 中国科学院宁波材料技术与工程研究所 Preparation method for thermoplastic polyimide foaming particle and formed body thereof

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1112143A (en) * 1994-02-09 1995-11-22 诺瓦蒙特股份公司 Expanded articles of biodegradable plastic material and a process for the preparation thereof
CN1800249A (en) * 2005-01-05 2006-07-12 项爱民 Biodegradable starch-base foaming composition and foaming product containing same
CN101522768A (en) * 2006-10-11 2009-09-02 巴斯夫欧洲公司 Coated foam beads and process for producing halogen-free, fire-resistant bead foam moldings
CN101668798A (en) * 2007-04-19 2010-03-10 辛伯拉技术有限公司 The inflatable particulate poly(lactic acid) that applies
WO2012008784A2 (en) * 2010-07-15 2012-01-19 대상 주식회사 Expandable starch bead and method for preparing same
CN102206361A (en) * 2011-04-27 2011-10-05 广东益德环保科技有限公司 Fully-degradable foam material using starch as base material and preparation method for fully-degradable foam material
CN102702562A (en) * 2012-05-24 2012-10-03 中国科学院宁波材料技术与工程研究所 Preparation method for thermoplastic polyimide foaming particle and formed body thereof

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