Abstract:
PURPOSE: A method for preparing an acryl-based polymer nano water dispersion is provided, to improve the environmental-friendliness of the acryl-based polymer nano water dispersion used in polymer cement and the tensile strength of the polymer cement. CONSTITUTION: The method comprises the steps of stirring the mixture comprising 45-55 parts by weight of an acryl-based monomer, 0.8-1.2 parts by weight of polyoxyethylene lauryl ether represented by C12H25O(C2H4O)nH (wherein n is 21-50) as a nonionic surfactant and 25-35 parts by weight distilled water at a temperature of 40-70 deg.C to prepare a stable monomer emulsion; stirring the mixture comprising 35-45 parts by weight of distilled water and 0.04-0.06 parts by weight of an anionic surfactant at a temperature of 60-80 deg.C and adding 0.2-1.5 parts by weight of an initiator to prepare an aqueous solution mixture; and continuously dropping the monomer emulsion to the aqueous solution mixture to perform the emulsion polymerization. The obtained acryl-based polymer nano water dispersion has a particle size of 315-350 nm and a polymer solid content of 37-41 wt%.
Abstract translation:目的:提供一种制备基于丙烯酰基的聚合物纳米水分散体的方法,以改善聚合物水泥中使用的基于丙烯酰基的聚合物纳米水分散体的环境友好性和聚合物水泥的拉伸强度。 构成:该方法包括如下步骤:搅拌包含45-55重量份丙烯酸类单体,0.8-1.2重量份由C 12 H 25 O(C 2 H 4 O)n H表示的聚氧乙烯月桂醚(其中n为21-50) 作为非离子表面活性剂和25-35重量份的蒸馏水,在40-70℃的温度下制备稳定的单体乳液; 在60〜80℃的温度下搅拌包含35〜45重量份蒸馏水和0.04〜0.06重量份阴离子表面活性剂的混合物,并加入0.2〜1.5重量份引发剂以制备水溶液 混合物; 并将单体乳液连续滴加到水溶液混合物中进行乳液聚合。 所得到的丙烯酸类聚合物纳米水分散体的粒径为315〜350nm,聚合物固体成分为37〜41重量%。
Abstract:
PURPOSE: A method for preparing the graft polymer of a polyvinylidene fluoride resin and an acryl derivative and its polymerization apparatus are provided to use little solvent, to reduce the reaction time, to improve the graft rate and to modify the surface of the polymer. CONSTITUTION: The method comprises the steps of putting a solid polyvinylidene fluoride resin supplying the main chain of a linear polymer into a solid state polymerization reactor; purging nitrogen gas to remove the oxygen present in the reactor; heating the temperature to 90-120 deg.C; injecting a solid state initiator to generate radicals at the polymerization reaction temperature; spraying a liquid acryl derivative in the state of aerosol; and reacting it at the polymerization reaction temperature for 10-50 min after the injection of an initiator. Preferably the initiator is benzoyl peroxide, and the acryl derivative is selected from the group consisting of acrylic acid, methacrylic acid and glycidyl methacrylate.
Abstract:
PURPOSE: A method for preparing an acryl-based polymer nano water dispersion is provided, to improve the environmental-friendliness of the acryl-based polymer nano water dispersion used in polymer cement and the tensile strength of the polymer cement. CONSTITUTION: The method comprises the steps of stirring the mixture comprising 45-55 parts by weight of an acryl-based monomer, 0.8-1.2 parts by weight of polyoxyethylene lauryl ether represented by C12H25O(C2H4O)nH (wherein n is 21-50) as a nonionic surfactant and 25-35 parts by weight distilled water at a temperature of 40-70 deg.C to prepare a stable monomer emulsion; stirring the mixture comprising 35-45 parts by weight of distilled water and 0.04-0.06 parts by weight of an anionic surfactant at a temperature of 60-80 deg.C and adding 0.2-1.5 parts by weight of an initiator to prepare an aqueous solution mixture; and continuously dropping the monomer emulsion to the aqueous solution mixture to perform the emulsion polymerization. The obtained acryl-based polymer nano water dispersion has a particle size of 315-350 nm and a polymer solid content of 37-41 wt%.
Abstract:
PURPOSE: A method for preparing the graft polymer of a polyvinylidene fluoride resin and an acryl derivative and its polymerization apparatus are provided to use little solvent, to reduce the reaction time, to improve the graft rate and to modify the surface of the polymer. CONSTITUTION: The method comprises the steps of putting a solid polyvinylidene fluoride resin supplying the main chain of a linear polymer into a solid state polymerization reactor; purging nitrogen gas to remove the oxygen present in the reactor; heating the temperature to 90-120 deg.C; injecting a solid state initiator to generate radicals at the polymerization reaction temperature; spraying a liquid acryl derivative in the state of aerosol; and reacting it at the polymerization reaction temperature for 10-50 min after the injection of an initiator. Preferably the initiator is benzoyl peroxide, and the acryl derivative is selected from the group consisting of acrylic acid, methacrylic acid and glycidyl methacrylate.