WO2021103081A1 - Environmentally friendly water purification functional masterbatch and preparation method therefor - Google Patents

Environmentally friendly water purification functional masterbatch and preparation method therefor Download PDF

Info

Publication number
WO2021103081A1
WO2021103081A1 PCT/CN2019/123152 CN2019123152W WO2021103081A1 WO 2021103081 A1 WO2021103081 A1 WO 2021103081A1 CN 2019123152 W CN2019123152 W CN 2019123152W WO 2021103081 A1 WO2021103081 A1 WO 2021103081A1
Authority
WO
WIPO (PCT)
Prior art keywords
parts
water purification
masterbatch
environmentally friendly
friendly water
Prior art date
Application number
PCT/CN2019/123152
Other languages
French (fr)
Chinese (zh)
Inventor
台启龙
赵进文
Original Assignee
苏州和塑美科技有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 苏州和塑美科技有限公司 filed Critical 苏州和塑美科技有限公司
Publication of WO2021103081A1 publication Critical patent/WO2021103081A1/en

Links

Images

Classifications

    • 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
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/22Compounding polymers with additives, e.g. colouring using masterbatch techniques
    • C08J3/226Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/02Making granules by dividing preformed material
    • B29B9/06Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
    • 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
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/64Screws with two or more threads
    • B29C48/655Screws with two or more threads having three or more threads
    • 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
    • B29C2948/92704Temperature
    • 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
    • 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
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/10Homopolymers or copolymers of propene
    • C08J2323/12Polypropene
    • 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
    • C08J2433/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
    • C08J2433/04Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters
    • C08J2433/06Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters of esters containing only carbon, hydrogen, and oxygen, the oxygen atom being present only as part of the carboxyl radical
    • C08J2433/10Homopolymers or copolymers of methacrylic acid esters
    • C08J2433/12Homopolymers or copolymers of methyl methacrylate
    • 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
    • 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
    • C08J2469/00Characterised by the use of polycarbonates; Derivatives of polycarbonates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • C08K2003/265Calcium, strontium or barium carbonate

Definitions

  • the invention relates to the manufacturing field of the resin mineral field, in particular to an environment-friendly water purification functional masterbatch and a preparation method.
  • the environmentally friendly water purification functional masterbatch can not only reduce the impact of sewage on the environment, but also improve the utilization rate of water resources. Moreover, the water purification functional masterbatch is made of environmentally friendly materials to meet environmentally friendly requirements.
  • the first object of the present invention is to provide an environmentally friendly water purification functional masterbatch;
  • the second object of the present invention is a method for preparing the environmentally friendly water purification functional masterbatch.
  • the present invention adopts the following first technical solution: an environmentally friendly water purification functional masterbatch, the masterbatch contains the following components by weight: 5-15 parts of polyester resin, poly 35-45 parts of olefin resin, 40-50 parts of mineral powder, and 5-10 parts of degradable resin polymer, and the particle surface of the masterbatch has a concave-convex thread-like structure.
  • the masterbatch is composed of the following components by weight: 5-10 parts by weight of the polyester resin, 40-45 parts by the polyolefin resin, 40-45 parts by the mineral powder, and degradable 8 parts of resin polymer.
  • the masterbatch is composed of the following components by weight: 6 parts by weight of polyester resin, 45 parts by polyolefin resin, 41 parts by mineral powder, and 8 parts by degradable resin polymer.
  • the degradable resin polymer is selected from at least one of polylactic acid PLA, polybutylene adipate terephthalate PBAT and starch.
  • the mineral powder is selected from at least one of talc powder, calcium carbonate, quartz powder, wollastonite and kaolin. Further preferably, the mineral powder mesh number is 500-5000 mesh.
  • the polyester resin is selected from polycarbonate PC, polymethyl methacrylate PMMA, polyethylene terephthalate-1 and 4-cyclohexanedimethanol At least one of ester PETG.
  • the polyolefin resin is selected from at least one of polypropylene PP, high-density polyethylene HDPE, low-density polyethylene LDPE and linear low-density polyethylene LLDPE.
  • the present invention adopts the following second technical solution: a method for preparing the above-mentioned environmentally friendly water purification functional masterbatch, the method including the method comprising:
  • Step 1 Stir the polyester resin, polyolefin resin, and degradable resin polymer uniformly, and then feed the mineral powder together with the mineral powder into the extruder through a weight loss scale to form a uniform mixture;
  • Step 2 Set the temperature of the extruder to 170-220°C so that the mixture is converted into a semi-molten state, and the mixture is extruded and pelletized through the extruder to obtain an environmentally friendly functional water purification functional mother grain.
  • the extrusion process of the extruder is controlled so that the mixture in a semi-molten state will undergo melt fracture when it enters the die of the extruder, In order to achieve the formation of concave and convex thread-like structure on the surface of the extrudate.
  • the water purification function masterbatch of the present invention not only has excellent water purification function, but also because the water purification function masterbatch is made of environmentally friendly materials, it meets the needs of environmental friendliness; in addition, the present invention has lower production costs, among which The prices of polyolefin materials and mineral powder are very low, and the production equipment is relatively simple, which greatly reduces the production cost.
  • the extrusion process and the material formula are set simultaneously, so that the material melts at the die of the extruder, and the concave-convex thread shape is formed on the surface of the masterbatch.
  • the structure makes it possible to form a microporous structure on the surface and inside of the masterbatch during use.
  • the degradable polymer in the formulation of the masterbatch with this structure accelerates decomposition under the influence of the external environment during use, and forms micropores on the surface and inside of the resin of the water purification function masterbatch, which greatly increases the specific surface area and surface roughness of the masterbatch It is more conducive to filtering and adsorbing impurities in the water.
  • the extruder in the following embodiments adopts a twin-screw extruder.
  • the extruder includes a feeding zone, a first heating zone, a second heating zone, a third heating zone, a fourth heating zone, and a second heating zone along the material movement direction. Five heating zones, sixth heating zone, seventh heating zone, eighth heating zone, ninth heating zone and machine head.
  • the extruder selects and installs the internal thread block, the internal thread block is divided into conveying section, melting section, homogenizing section and compression section according to the function; in the specific setting, the conveying section group is composed of thread blocks with long pitch , There is a compression section composed of appropriate short pitch thread blocks between entering the melting section.
  • the melting section is composed of a few thick shear slices and an appropriate amount of thin shear slice thread blocks.
  • the homogenization section is composed of scattered thin shear piece thread blocks.
  • the compression section is composed of a proper amount of short-pitch thread blocks. Reverse thread speed is not used in the arrangement.
  • the overall arrangement is weakly sheared and weakly dispersed.
  • the control temperature of each part of the extruder is: the first heating zone 140 ⁇ 10°C, the second heating zone 170 ⁇ 10°C, the third heating zone 190 ⁇ 10°C, and the first heating zone is 170 ⁇ 10°C.
  • the above-mentioned parts by weight of the raw materials are first transformed into a semi-molten state in the extruder, and the semi-molten mixture will undergo melt fracture when entering the die of the extruder head.
  • the surface of the product is formed with a concave-convex thread-like structure similar to a thread.
  • the above-mentioned parts by weight of the raw materials are first transformed into a semi-molten state in the extruder, and the semi-molten mixture will undergo melt fracture when entering the die of the extruder head. Concave and convex thread-like structures are formed on the surface of the product.
  • test results of the prepared environmentally friendly water purification function masterbatch the bulk density is 700g/L, and the depth of the raised threads on the particle surface is 1.8-2.3mm.
  • the environment-friendly water purification function masterbatch resin provided by the present invention can adjust the size, bulk density, and sedimentation rate of the water purification function masterbatch resin according to the water flow speed and impurity types, and filter most of the impurity particles in the sewage.
  • the purification mechanism is that the surface of the resin particles of the water purification function masterbatch prepared by a special process has raised threads and a large number of micropores, and some acidic or alkaline substances in the sewage can accelerate the decomposition of degradable polymers, and further improve the water purification function. Holes are formed on the masterbatch, which greatly increases the specific surface area and surface roughness of the water purification masterbatch, which effectively plays a role of filtration and adsorption.

Abstract

An environmentally friendly water purification functional masterbatch. The masterbatch comprises the following components: 5-15 parts polyester resin, 35-45 parts polyolefin resin, 40-50 parts mineral powder, and 5-10 parts of a degradable resin polymer. Further comprised is a preparation method for the masterbatch: the polyester resin, polyolefin resin, and degradable resin polymer are added into a mixing drum for uniform mixing, the mixed material and the mineral powder are added into an extruder, the temperature of the extruder is adjusted to be 170-220°C, the mixture is extruded and granulated, and the surfaces of extruded particles have concave and convex thread shapes.

Description

一种环境友好型水净化功能母粒及其制备方法Environment-friendly water purification functional masterbatch and preparation method thereof 技术领域Technical field
本发明涉及树脂矿物领域制造领域,特别涉及一种环境友好型水净化功能母粒以及制备方法。The invention relates to the manufacturing field of the resin mineral field, in particular to an environment-friendly water purification functional masterbatch and a preparation method.
背景技术Background technique
水对人们的生命起着重要的作用,它是生命的源泉,是人类赖以生存和发展的不可缺少的最重要的物质资源之一。在现代工业中,没有一个工业部门是不用水的,也没有一项工业不和水直接或间接发生关系。每个工厂都需要利用水的各个作用来维护正常生产,几乎每个生产环节都需要水的参与。联合国已经将我国列为世界上最缺水的13个国家之一,目前我国人均用水量是世界人均用水量的30%。不幸的是随着用水量的日益增长,水污染问题日趋严重,所以针对工业污水的净化处理变得极为重要。环境友好型水净化功能母粒不仅可以减少污水对环境的影响,而且提高了水资源利用率,并且该水净化功能母粒都是由环保材料制作而成,满足环境友好的需求。Water plays an important role in people's lives. It is the source of life and one of the most important material resources indispensable for human survival and development. In modern industry, no industrial sector does not use water, and no industry is not directly or indirectly related to water. Every factory needs to use the various functions of water to maintain normal production, and almost every production link needs the participation of water. The United Nations has listed my country as one of the 13 most water-scarce countries in the world. At present, my country's per capita water consumption is 30% of the world's per capita water consumption. Unfortunately, with the ever-increasing water consumption, the problem of water pollution has become more and more serious, so the purification treatment of industrial wastewater has become extremely important. The environmentally friendly water purification functional masterbatch can not only reduce the impact of sewage on the environment, but also improve the utilization rate of water resources. Moreover, the water purification functional masterbatch is made of environmentally friendly materials to meet environmentally friendly requirements.
发明内容Summary of the invention
为了解决上述技术问题,本发明的第一个目的是提供一种环境友好型水净化功能母粒;本发明的第二个目的是制备该环境友好型水净化功能母粒的方法。In order to solve the above technical problems, the first object of the present invention is to provide an environmentally friendly water purification functional masterbatch; the second object of the present invention is a method for preparing the environmentally friendly water purification functional masterbatch.
为了实现上述发明的第一个目的,本发明采用如下第一技术方案:一种环境友好型水净化功能母粒,该母粒含有如下重量份的组分:聚酯树脂5-15份,聚烯烃树脂35-45份、矿物粉40-50份以及可降解树脂聚合物5-10份,并且所述母粒的粒子表面为凹凸螺纹状结构。In order to achieve the first objective of the above-mentioned invention, the present invention adopts the following first technical solution: an environmentally friendly water purification functional masterbatch, the masterbatch contains the following components by weight: 5-15 parts of polyester resin, poly 35-45 parts of olefin resin, 40-50 parts of mineral powder, and 5-10 parts of degradable resin polymer, and the particle surface of the masterbatch has a concave-convex thread-like structure.
上述第一技术方案中,优选的,该母粒由如下重量份的组分构成:所述的聚酯树脂5-10份、聚烯烃树脂40-45份、矿物粉40-45份以及可降解树脂聚合物8份。进一步优选方案中,该母粒由如下重量份的组分构成:聚酯树脂6份、聚烯烃树脂45份、矿物粉41份以及可降解树脂聚合物8份。In the above-mentioned first technical solution, preferably, the masterbatch is composed of the following components by weight: 5-10 parts by weight of the polyester resin, 40-45 parts by the polyolefin resin, 40-45 parts by the mineral powder, and degradable 8 parts of resin polymer. In a further preferred embodiment, the masterbatch is composed of the following components by weight: 6 parts by weight of polyester resin, 45 parts by polyolefin resin, 41 parts by mineral powder, and 8 parts by degradable resin polymer.
上述第一技术方案中,优选的,所述的可降解树脂聚合物选自聚乳酸PLA、聚 己二酸对苯二甲酸丁二酯PBAT和淀粉中的至少一种。In the above first technical solution, preferably, the degradable resin polymer is selected from at least one of polylactic acid PLA, polybutylene adipate terephthalate PBAT and starch.
上述第一技术方案中,优选的,所述的矿物粉选自滑石粉、碳酸钙、石英粉、硅灰石以及高岭土中的至少一种。进一步优选,所述的矿物粉目数在500-5000目。In the above first technical solution, preferably, the mineral powder is selected from at least one of talc powder, calcium carbonate, quartz powder, wollastonite and kaolin. Further preferably, the mineral powder mesh number is 500-5000 mesh.
上述第一技术方案中,优选的,所述的聚酯树脂选自聚碳酸酯PC、聚甲基丙烯酸甲酯PMMA、聚对苯二甲酸乙二醇酯-1以及4-环己烷二甲醇酯PETG中的至少一种。In the above first technical solution, preferably, the polyester resin is selected from polycarbonate PC, polymethyl methacrylate PMMA, polyethylene terephthalate-1 and 4-cyclohexanedimethanol At least one of ester PETG.
上述第一技术方案中,优选的,所述的聚烯烃树脂选自聚丙烯PP、高密度聚乙烯HDPE、低密度聚乙烯LDPE和线性低密度聚乙烯LLDPE中的至少一种。In the above first technical solution, preferably, the polyolefin resin is selected from at least one of polypropylene PP, high-density polyethylene HDPE, low-density polyethylene LDPE and linear low-density polyethylene LLDPE.
为了实现上述发明的第二个目的,本发明采用如下第二技术方案:一种制备上述环境友好型水净化功能母粒的方法,该方法包括该方法包括:In order to achieve the second object of the above-mentioned invention, the present invention adopts the following second technical solution: a method for preparing the above-mentioned environmentally friendly water purification functional masterbatch, the method including the method comprising:
步骤一:使所述聚酯树脂、聚烯烃树脂以及可降解树脂聚合物搅拌均匀后与所述矿物粉一起通过失重称送入挤出机中形成均匀混合物;Step 1: Stir the polyester resin, polyolefin resin, and degradable resin polymer uniformly, and then feed the mineral powder together with the mineral powder into the extruder through a weight loss scale to form a uniform mixture;
步骤二:设定所述挤出机温度为170-220℃,使得所的混合物转化为半熔融状态,将所述混合物通过挤出机挤出造粒,即得到环境友好型功能水净化功能母粒。Step 2: Set the temperature of the extruder to 170-220°C so that the mixture is converted into a semi-molten state, and the mixture is extruded and pelletized through the extruder to obtain an environmentally friendly functional water purification functional mother grain.
上述第二优选方案中,在上述步骤二中,控制所述挤出机的挤出工艺,使得处于半熔融状态的混合物在进入到所述挤出机的口模处时发生熔体破裂现象,以实现在挤出物的表面形成凹凸螺纹状结构。In the above second preferred solution, in the above step 2, the extrusion process of the extruder is controlled so that the mixture in a semi-molten state will undergo melt fracture when it enters the die of the extruder, In order to achieve the formation of concave and convex thread-like structure on the surface of the extrudate.
本发明的水净化功能母粒不仅具有优良的水净化功能,而且由于该水净化功能母粒都是由环保材料制成,满足环境友好的需求;另外,本发明具有较低的生产成本,其中聚烯烃材料和矿物粉的价格都很低廉,生产设备也相对简单,大大降低了生产成本。在本发明的水净化功能母粒制备方法中,通过挤出工艺与材料配方的同步设定,使材料在挤出机口模处发生熔体破裂现象,在母粒的粒子表面形成凹凸螺纹状结构,使得该母粒在使用过程中,粒子表面和内部可以形成微孔结构。具有该结构的母粒在使用过程中配方里的可降解聚合物在外界环境影响下加速分解,在水净化功能母粒树脂表面和内部形成微孔,大大增加了母粒的比表面积和表面粗糙度,更有利于过滤和吸附水中的杂质。The water purification function masterbatch of the present invention not only has excellent water purification function, but also because the water purification function masterbatch is made of environmentally friendly materials, it meets the needs of environmental friendliness; in addition, the present invention has lower production costs, among which The prices of polyolefin materials and mineral powder are very low, and the production equipment is relatively simple, which greatly reduces the production cost. In the preparation method of the water purification function masterbatch of the present invention, the extrusion process and the material formula are set simultaneously, so that the material melts at the die of the extruder, and the concave-convex thread shape is formed on the surface of the masterbatch. The structure makes it possible to form a microporous structure on the surface and inside of the masterbatch during use. The degradable polymer in the formulation of the masterbatch with this structure accelerates decomposition under the influence of the external environment during use, and forms micropores on the surface and inside of the resin of the water purification function masterbatch, which greatly increases the specific surface area and surface roughness of the masterbatch It is more conducive to filtering and adsorbing impurities in the water.
具体实施方式Detailed ways
为详细说明发明的技术内容、构造特征、所达成目的及功效,下面将结合实施例予以详细说明。In order to describe in detail the technical content, structural features, objectives and effects of the invention, a detailed description will be given below in conjunction with the embodiments.
下述实施例中的挤出机采用双螺杆挤出机,该挤出机沿物料移动方向包括下料区、第一加热区、第二加热区、第三加热区、第四加热区、第五加热区、第六加热区、第七加热区、第八加热区、第九加热区以及机头。其中挤出机在选配和设置内部螺纹块时,将内部螺纹块按照功能分成输送段、熔融段、均化段以及压缩段;在具体设置时,输送段组采用由长螺距的螺纹块组成,进入熔融段之间有适当短螺距螺纹块组成的压缩段。熔融段由较少的厚剪切片和适量的薄剪切片螺纹块组成。均化段由分散的薄剪切片螺纹块组成。压缩段有适量的短螺距螺纹块组成。排列方式中不使用反向螺纹快。整体呈弱剪切,弱分散的排列方式。The extruder in the following embodiments adopts a twin-screw extruder. The extruder includes a feeding zone, a first heating zone, a second heating zone, a third heating zone, a fourth heating zone, and a second heating zone along the material movement direction. Five heating zones, sixth heating zone, seventh heating zone, eighth heating zone, ninth heating zone and machine head. When the extruder selects and installs the internal thread block, the internal thread block is divided into conveying section, melting section, homogenizing section and compression section according to the function; in the specific setting, the conveying section group is composed of thread blocks with long pitch , There is a compression section composed of appropriate short pitch thread blocks between entering the melting section. The melting section is composed of a few thick shear slices and an appropriate amount of thin shear slice thread blocks. The homogenization section is composed of scattered thin shear piece thread blocks. The compression section is composed of a proper amount of short-pitch thread blocks. Reverse thread speed is not used in the arrangement. The overall arrangement is weakly sheared and weakly dispersed.
在制作下述实施例的母粒时,挤出机各部件的控制温度分别为:第一加热区140±10℃、第二加热区170±10℃、第三加热区190±10℃、第四加热区190±10℃、第五加热区175±10℃、第六加热区区175±10℃、第七加热区200±10℃、第八加热区190±10℃、第九加热区210±10℃以及机头210±10℃。When making the masterbatch of the following embodiment, the control temperature of each part of the extruder is: the first heating zone 140±10°C, the second heating zone 170±10°C, the third heating zone 190±10°C, and the first heating zone is 170±10°C. Four heating zones 190±10℃, fifth heating zone 175±10℃, sixth heating zone 175±10℃, seventh heating zone 200±10℃, eighth heating zone 190±10℃, ninth heating zone 210± 10℃ and the head 210±10℃.
各段螺纹块排列以及参数配置如下表:The arrangement and parameter configuration of each thread block are as follows:
[Table 1][Table 1]
Figure PCTCN2019123152-appb-000001
Figure PCTCN2019123152-appb-000001
测试仪器和标准:Test equipment and standards:
1.堆积密度:粉体堆积密度测试仪GB/T1479.1-2011。1. Bulk density: powder bulk density tester GB/T1479.1-2011.
2.母粒颗粒表面螺纹深浅:游标卡尺测量。2. The depth of thread on the surface of masterbatch particles: measured by vernier calipers.
实施例1:Example 1:
按重量份数计,将PMMA(CM-205)6份,PP(T30S)45份,PLA(4032D)8份,混合均匀后与碳酸钙(500目)41份通过失重称加入双螺杆挤出机中,挤出机的温度以及螺纹块配置按照上述内容设定。挤出机的真空度控制在-0.8MPa,螺杆转速为350RPM,产量40kg/h。In parts by weight, 6 parts of PMMA (CM-205), 45 parts of PP (T30S), 8 parts of PLA (4032D), mixed uniformly, and 41 parts of calcium carbonate (500 mesh) are added to the twin-screw extrusion by weight loss In the machine, the temperature of the extruder and the configuration of the screw block are set as described above. The vacuum degree of the extruder is controlled at -0.8MPa, the screw speed is 350RPM, and the output is 40kg/h.
依照上述控制参数,上述重量份的原料首先在挤出机中转变成半熔融状态,半熔融状态的混合物在进入到挤出机机头的口模处时将发生熔体破裂现象,从而在挤出物的表面形成类似螺纹的凹凸螺纹状结构。According to the above-mentioned control parameters, the above-mentioned parts by weight of the raw materials are first transformed into a semi-molten state in the extruder, and the semi-molten mixture will undergo melt fracture when entering the die of the extruder head. The surface of the product is formed with a concave-convex thread-like structure similar to a thread.
制得的环境友好型水净化功能母粒测试结果:堆积密度600g/L,颗粒表面凸起螺纹深度1.5-2mm。Test results of the prepared environmentally friendly water purification functional masterbatch: the bulk density is 600g/L, and the depth of the raised threads on the particle surface is 1.5-2mm.
实施例2:Example 2:
按重量份数计,将PC(ET-3113)6份,PP(K8003)40份,PLA(4032D)8份,混合均匀后与碳酸钙(500目)46份通过失重称加入双螺杆挤出机中,挤出机的温度以及螺纹块配置按照上述内容设定。真空度控制在-0.5MPa,螺杆转速为400RPM,产量40kg/h。In parts by weight, 6 parts of PC (ET-3113), 40 parts of PP (K8003), 8 parts of PLA (4032D), mixed uniformly, and 46 parts of calcium carbonate (500 mesh) are added to the twin-screw extrusion by weight loss In the machine, the temperature of the extruder and the configuration of the screw block are set as described above. The vacuum degree is controlled at -0.5MPa, the screw speed is 400RPM, and the output is 40kg/h.
依照上述控制参数,上述重量份的原料首先在挤出机中转变成半熔融状态,半熔融状态的混合物在进入到挤出机机头的口模处时将发生熔体破裂现象,从而在挤出物的表面形成凹凸螺纹状结构。According to the above-mentioned control parameters, the above-mentioned parts by weight of the raw materials are first transformed into a semi-molten state in the extruder, and the semi-molten mixture will undergo melt fracture when entering the die of the extruder head. Concave and convex thread-like structures are formed on the surface of the product.
制得的环境友好型水净化功能母粒测试结果:堆积密度700g/L,颗粒表面凸起螺纹深度1.8-2.3mm。Test results of the prepared environmentally friendly water purification function masterbatch: the bulk density is 700g/L, and the depth of the raised threads on the particle surface is 1.8-2.3mm.
本发明所提供的环境友好型水净化功能母粒树脂可以根据水流速度和杂质种类对水净化功能母粒树脂颗粒尺寸,堆积密度,沉降率进行调整,将污水中的绝大部分杂质颗粒过滤干净,净化机理是经过特殊工艺制备的水净化功能母粒树脂颗粒表面有凸起螺纹和大量微孔,并且污水中的一些酸性或碱性物质可以加速可降解聚合物的分解,进一步在水净化功能母粒上形成孔洞,很大程度的加大了水净化功能母粒的比表面积和表面粗糙度,有效的起到了过滤和吸附作用。The environment-friendly water purification function masterbatch resin provided by the present invention can adjust the size, bulk density, and sedimentation rate of the water purification function masterbatch resin according to the water flow speed and impurity types, and filter most of the impurity particles in the sewage. The purification mechanism is that the surface of the resin particles of the water purification function masterbatch prepared by a special process has raised threads and a large number of micropores, and some acidic or alkaline substances in the sewage can accelerate the decomposition of degradable polymers, and further improve the water purification function. Holes are formed on the masterbatch, which greatly increases the specific surface area and surface roughness of the water purification masterbatch, which effectively plays a role of filtration and adsorption.
上述实施例只为说明本发明的技术构思及特点,其目的在于让熟悉此项技术人士能够了解本发明的内容并据以实施,并不能以此限制本发明保护范围。凡根据本发明精神所作的等效变化或修饰,都应涵盖在本发明的保护范围之内。The above-mentioned embodiments are only to illustrate the technical concept and features of the present invention, and their purpose is to enable those skilled in the art to understand the content of the present invention and implement them accordingly, and should not limit the protection scope of the present invention. All equivalent changes or modifications made according to the spirit of the present invention should be covered within the protection scope of the present invention.
发明概述Summary of the invention
技术问题technical problem
问题的解决方案The solution to the problem
发明的有益效果The beneficial effects of the invention

Claims (10)

  1. 一种环境友好型水净化功能母粒,其特征在于:该母粒含有如下重量份的组分:聚酯树脂5-15份,聚烯烃树脂35-45份、矿物粉40-50份以及可降解树脂聚合物5-10份,并且所述母粒的粒子表面为凹凸螺纹状结构。An environmentally friendly water purification functional masterbatch, which is characterized in that the masterbatch contains the following components by weight: 5-15 parts by weight of polyester resin, 35-45 parts by polyolefin resin, 40-50 parts by mineral powder, and The degradable resin polymer is 5-10 parts, and the particle surface of the masterbatch has a concave-convex thread-like structure.
  2. 根据权利要求1所述的环境友好型水净化功能母粒,其特征在于:该母粒由如下重量份的组分构成:所述的聚酯树脂5-10份、聚烯烃树脂40-45份、矿物粉40-45份以及可降解树脂聚合物8份。The environmentally friendly water purification functional masterbatch according to claim 1, wherein the masterbatch is composed of the following parts by weight: 5-10 parts of the polyester resin and 40-45 parts of the polyolefin resin , 40-45 parts of mineral powder and 8 parts of degradable resin polymer.
  3. 根据权利要求2所述的环境友好型水净化功能母粒,其特征在于:该母粒由如下重量份的组分构成:聚酯树脂6份、聚烯烃树脂45份、矿物粉41份以及可降解树脂聚合物8份。The environmentally-friendly water purification functional masterbatch according to claim 2, characterized in that: the masterbatch is composed of the following components by weight: 6 parts of polyester resin, 45 parts of polyolefin resin, 41 parts of mineral powder, and 8 parts of degradable resin polymer.
  4. 根据权利要求1所述的环境友好型水净化功能母粒,其特征在于:所述的可降解树脂聚合物选自聚乳酸PLA、聚己二酸对苯二甲酸丁二酯PBAT和淀粉中的至少一种。The environmentally friendly water purification functional masterbatch according to claim 1, wherein the degradable resin polymer is selected from the group consisting of polylactic acid PLA, polybutylene adipate terephthalate PBAT and starch At least one.
  5. 根据权利要求1所述的环境友好型水净化功能母粒,其特征在于:所述的矿物粉选自滑石粉、碳酸钙、石英粉、硅灰石以及高岭土中的至少一种。The environmentally friendly water purification functional masterbatch according to claim 1, wherein the mineral powder is selected from at least one of talc powder, calcium carbonate, quartz powder, wollastonite and kaolin.
  6. 根据权利要求5所述的环境友好型水净化功能母粒,其特征在于:所述的矿物粉目数在500-5000目。The environmentally friendly water purification functional masterbatch according to claim 5, wherein the mineral powder has a mesh number of 500-5000 mesh.
  7. 根据权利要求1所述的环境友好型水净化功能母粒,其特征在于:所述的聚酯树脂选自聚碳酸酯PC、聚甲基丙烯酸甲酯PMMA、聚对苯二甲酸乙二醇酯-1以及4-环己烷二甲醇酯PETG中的至少一种;The environmentally friendly water purification functional masterbatch according to claim 1, wherein the polyester resin is selected from polycarbonate PC, polymethyl methacrylate PMMA, polyethylene terephthalate -1 and at least one of 4-cyclohexanedimethanol ester PETG;
  8. 根据权利要求1所述的环境友好型水净化功能母粒,其特征在于:所述的聚烯烃树脂选自聚丙烯PP、高密度聚乙烯HDPE、低密度聚乙烯LDPE和线性低密度聚乙烯LLDPE中的至少一种。The environmentally friendly water purification functional masterbatch according to claim 1, wherein the polyolefin resin is selected from polypropylene PP, high-density polyethylene HDPE, low-density polyethylene LDPE and linear low-density polyethylene LLDPE At least one of them.
  9. 一种制备如权利要求1-8中任意一项所述的环境友好型水净化功能母粒的方法,其特征在于,该方法包括:A method for preparing the environmentally friendly water purification functional masterbatch according to any one of claims 1-8, characterized in that the method comprises:
    步骤一:使所述聚酯树脂、聚烯烃树脂以及可降解树脂聚合物搅拌均匀后与所述矿物粉一起通过失重称送入挤出机中形成均匀混合物;Step 1: Stir the polyester resin, polyolefin resin, and degradable resin polymer uniformly, and then feed the mineral powder together with the mineral powder into the extruder through a weight loss scale to form a uniform mixture;
    步骤二:设定所述挤出机的温度为170-220℃,使得所的混合物转化为半熔融状态,将所述混合物挤出造粒,即得到环境友好型功能水净化功能母粒。Step 2: Set the temperature of the extruder to 170-220°C, so that the mixture is converted into a semi-molten state, and the mixture is extruded and pelletized to obtain an environmentally friendly functional water purification masterbatch.
  10. 根据权利要求9所述的制备方法,其特征在于:在上述步骤二中,控制所述挤出机的挤出工艺使得处于半熔融状态的混合物在进入到所述挤出机的口模处时发生熔体破裂现象,以实现在挤出物的表面形成凹凸螺纹状结构。The preparation method according to claim 9, characterized in that: in the second step, the extrusion process of the extruder is controlled so that the mixture in a semi-molten state enters the die of the extruder Melt fracture occurs to achieve the formation of concave and convex thread-like structures on the surface of the extrudate.
PCT/CN2019/123152 2019-11-30 2019-12-05 Environmentally friendly water purification functional masterbatch and preparation method therefor WO2021103081A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201911207993.9A CN110776694A (en) 2019-11-30 2019-11-30 Environment-friendly water purification functional master batch and preparation method thereof
CN201911207993.9 2019-11-30

Publications (1)

Publication Number Publication Date
WO2021103081A1 true WO2021103081A1 (en) 2021-06-03

Family

ID=69393992

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2019/123152 WO2021103081A1 (en) 2019-11-30 2019-12-05 Environmentally friendly water purification functional masterbatch and preparation method therefor

Country Status (2)

Country Link
CN (1) CN110776694A (en)
WO (1) WO2021103081A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115926386A (en) * 2022-03-16 2023-04-07 苏州方位无菌包装有限公司 Medical plastic uptake tray for surgical operation instrument and preparation method thereof

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101143962A (en) * 2006-09-15 2008-03-19 奇钛科技股份有限公司 Biodegradable resin composition for modifying toughness and heat resistance and preparation method thereof
US20090124717A1 (en) * 2007-08-23 2009-05-14 Nisshinbo Industries, Inc. Carrier for fluid treatment and method of making the same
CN102227476A (en) * 2009-09-30 2011-10-26 索尼公司 Resin composition
CN103936147A (en) * 2010-11-24 2014-07-23 栗田工业株式会社 Anaerobic Treatment Method And Apparatus
CN105102378A (en) * 2013-03-27 2015-11-25 栗田工业株式会社 Anaerobic treatment method
CN105431479A (en) * 2013-08-09 2016-03-23 金伯利-克拉克环球有限公司 Technique for selectively controlling the porosity of a polymeric material
CN106414605A (en) * 2014-06-05 2017-02-15 欧米亚国际集团 Polymer composition filled with an inorganic filler material mixture

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100999361A (en) * 2007-01-05 2007-07-18 华南理工大学 Nutrition slow-release type biofiller for water treatment and its preparation method
CN101928069B (en) * 2009-06-19 2012-06-27 深圳市意可曼生物科技有限公司 Sewage purifier and sewage purification method
CN108726688B (en) * 2018-04-25 2021-05-04 上海祺宇生物科技有限公司 Porous carrier for water treatment and preparation method thereof
CN108912458A (en) * 2018-07-19 2018-11-30 朱玮 A kind of preparation method of environment-friendly type ultra-high molecular weight polyethylene filtering material

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101143962A (en) * 2006-09-15 2008-03-19 奇钛科技股份有限公司 Biodegradable resin composition for modifying toughness and heat resistance and preparation method thereof
US20090124717A1 (en) * 2007-08-23 2009-05-14 Nisshinbo Industries, Inc. Carrier for fluid treatment and method of making the same
CN102227476A (en) * 2009-09-30 2011-10-26 索尼公司 Resin composition
CN103936147A (en) * 2010-11-24 2014-07-23 栗田工业株式会社 Anaerobic Treatment Method And Apparatus
CN105102378A (en) * 2013-03-27 2015-11-25 栗田工业株式会社 Anaerobic treatment method
CN105431479A (en) * 2013-08-09 2016-03-23 金伯利-克拉克环球有限公司 Technique for selectively controlling the porosity of a polymeric material
CN106414605A (en) * 2014-06-05 2017-02-15 欧米亚国际集团 Polymer composition filled with an inorganic filler material mixture

Also Published As

Publication number Publication date
CN110776694A (en) 2020-02-11

Similar Documents

Publication Publication Date Title
CN106700134B (en) Degradable casting films of starch-based bio and preparation method thereof
CN109912878B (en) Raw material composition for preparing film-blowing breathable film, film-blowing breathable film and preparation of film-blowing breathable film
JPH01118425A (en) Method of manufacturing molded form from paper and synthetic resin
CN102060564A (en) Light-weight environmental-friendly stone paper and preparation method thereof
CN107216517B (en) Preparation method of ultrahigh molecular weight polyethylene 3D printing supplies
WO2021103081A1 (en) Environmentally friendly water purification functional masterbatch and preparation method therefor
CN112778600A (en) Special material for polyolefin breathable film and preparation method and application thereof
CN110684279A (en) Pearlescent master batch for biaxially oriented film and preparation method and application thereof
CN102304268B (en) Modified acrylonitrile-butadiene-styrene copolymer and preparation process thereof
CN113234304A (en) Biodegradable film material and preparation method of film
CN111349283A (en) Application of inorganic filled polyolefin material in preparation of all-plastic nose bridge strip of disposable mask
CN102241853A (en) Calcium-whisker-modified polyethylene composite material and preparation method thereof
CN104072843A (en) Multi-scale composite function masterbatch and preparation method thereof
CN103709479A (en) Aluminum-plastic composite panel with high rigidity and high bending strength and preparation method of aluminum-plastic composite panel
CN109575396A (en) A kind of waterproof ventilated membrane composite material and preparation method
CN107573660A (en) A kind of low temperature FDM types biological medical degradable 3D printing material, preparation and application
CN101591458A (en) A kind of composition and method of making the same of melt-processable
CN102311603B (en) Calcium sulfate whisker modified polymethylmethacrylate and preparation process thereof
WO2019047700A1 (en) Preparation methods for environment-friendly plastic masterbatch material, environment-friendly film and environment-friendly tape
JP2018079640A (en) Process for producing pellet, process for producing resin molding, and pellet
CN113881111A (en) Thermoplastic corn starch for plastic filling and preparation method thereof
CN103923389B (en) A kind of calcium sulfate crystal whiskers synthetic paper and preparation method thereof
CN114133705A (en) Preparation method of degradable plastic mixed particles
CN115044116A (en) Light-scattering agricultural film
JP3005044B2 (en) Porous sheet

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: 19954396

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 19954396

Country of ref document: EP

Kind code of ref document: A1

122 Ep: pct application non-entry in european phase

Ref document number: 19954396

Country of ref document: EP

Kind code of ref document: A1