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CN1939878B - Method for coating fertilizer by emulsified and/or soluble adhesive - Google Patents

Method for coating fertilizer by emulsified and/or soluble adhesive Download PDF

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CN1939878B
CN1939878B CN200510094536A CN200510094536A CN1939878B CN 1939878 B CN1939878 B CN 1939878B CN 200510094536 A CN200510094536 A CN 200510094536A CN 200510094536 A CN200510094536 A CN 200510094536A CN 1939878 B CN1939878 B CN 1939878B
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emulsion
hydrophobic
fertilizer
adhesive
aqueous solution
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CN1939878A (en
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应宗荣
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Nanjing University of Science and Technology
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Nanjing University of Science and Technology
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Abstract

Production of coated slow-released fertilizer by emulsion and solution adhesion agent is carried out by coating fertilizer by melt and/or organic solvent coating liquid, forming hydrophobic organic coating layer on fertilizer surface, coating pre-coated fertilizer with hydrophobic organic membrane-layer on surface by emulsion and/or solution adhesion and obtaining the final product. The hydrophobic organic membrane-layer can be low-molecular hydrophobic organic membrane layer and/or hydrophobic polymer membrane layer with melt point or softening point >=76 degree; emulsion and solution adhesion agent can be polymer emulsion adhesion agent, solution polymer adhesion agent and/or solution inorganic adhesion agent. It's cheap and effective.

Description

采用水乳液型和/或水溶液型胶粘剂包膜肥料的方法 Method for coating fertilizer with water emulsion type and/or aqueous solution type adhesive

一、技术领域1. Technical field

本发明涉及一种包膜方法,特别涉及一种采用水乳液型和水溶液型胶粘剂包膜肥料的方法,属于缓释肥料制备技术领域。The invention relates to a coating method, in particular to a method for coating fertilizer with water emulsion type and aqueous solution type adhesive, and belongs to the technical field of slow-release fertilizer preparation.

二、背景技术2. Background technology

缓释肥料是农业肥料的发展方向。其中,包膜型缓释肥料是缓释肥料中最重要的一类,它是在肥料颗粒表面涂覆有机聚合物或无机物的包膜,使肥料溶入田土中的速度减缓,达到缓释的目的。包膜型缓释肥料可以具有优异的可控缓释性能,是今后缓释肥料的主要方向。Slow-release fertilizers are the development direction of agricultural fertilizers. Among them, coated slow-release fertilizer is the most important type of slow-release fertilizer. It is coated with organic polymer or inorganic coating on the surface of fertilizer particles to slow down the rate of fertilizer dissolution into the field and achieve slow-release fertilizers. the goal of. Coated slow-release fertilizers can have excellent controllable slow-release performance, which is the main direction of slow-release fertilizers in the future.

对肥料进行包膜时,包膜液的形式可以是熔体(比如热固性聚合物的预聚体熔体),也可以是有机溶液(比如热塑性聚合物的有机溶液),还可以是水溶液或水乳液。对肥料进行包膜以制备包膜型缓释肥料时,能采用熔体形式的包膜液进行包膜是最理想的,因为不使用溶剂,经济环保。但是,有的只能采用溶液形式或水乳液形式的包膜液,而采用有机溶液形式的包膜液进行包膜由于要采用有机溶剂,既不经济也会存在环境污染问题,因此采用其水乳液形式的包膜液进行包膜是相对经济和环保的。当然,能采用水溶液形式进行包膜也是相对经济和环保的,有的只能采用水溶液,如氨基树脂预聚物溶液和聚乙烯醇及其共聚物的缩醛树脂溶液等。When coating fertilizers, the coating solution can be in the form of a melt (such as a prepolymer melt of a thermosetting polymer), an organic solution (such as an organic solution of a thermoplastic polymer), or an aqueous solution or water lotion. When coating fertilizers to prepare coated slow-release fertilizers, it is ideal to use the coating liquid in the form of melt for coating, because no solvent is used, which is economical and environmentally friendly. However, some can only use the coating liquid in the form of a solution or an aqueous emulsion, and the coating liquid in the form of an organic solution is used for coating because an organic solvent is used, which is neither economical nor environmentally polluting. Therefore, the use of other water The coating liquid in the form of emulsion is relatively economical and environmentally friendly. Of course, it is relatively economical and environmentally friendly to use aqueous solution for coating, and some can only use aqueous solution, such as amino resin prepolymer solution and acetal resin solution of polyvinyl alcohol and its copolymer.

但是,采用水溶液形式或水乳液形式的包膜液对肥料直接进行包膜时,肥料常常会溶入水溶液形式或水乳液形式的包膜液中,因此使形成的包膜膜层中含有肥料,干燥成膜时其中的肥料会在包膜膜层中呈针状等形状析出,成为肥料通过膜层的快速溶出通道,降低膜层对肥料的阻透性,使制备的包膜型缓释肥料的释放期减短,同时膜层中的肥料还会降低膜层强度,需要较厚的包膜厚度。因此,采用水溶液形式或水乳液形式的包膜液对肥料进行包膜制备包膜型缓释肥料时,如何避免肥料进入包膜形成的膜层中是一个难题。有研究者在采用聚丙烯酸酯乳液对尿素进行包膜制备聚丙烯酸酯包膜型缓释尿素时,采用在尿素表面先喷涂一薄层石蜡膜层或硫磺膜层、然后再采用聚丙烯酸酯乳液对尿素进行包膜的方法。由于石蜡的熔点通常低于75℃,因此先喷涂一薄层石蜡膜层、然后再采用聚丙烯酸酯乳液对尿素进行包膜,则挥发除去聚丙烯酸酯乳液中的水以形成聚丙烯酸酯膜层时,常压干燥时的温度得低于75℃,因此膜层中水分除去的速度很低,干燥成膜速度很慢;如果要提高干燥除水速度,则需要采用真空干燥,而真空干燥工艺复杂。采用在尿素表面先喷涂一薄层硫磺膜层、然后再采用聚丙烯酸酯乳液对尿素进行包膜的方法,也存在一个问题,喷涂硫磺膜层的设备和工艺复杂,并且在制备得到的包膜型缓释肥料中含有硫磺,有的应用场合的土质不希望有硫磺进入土层中,因此这一方法也存在一定的问题。But, when adopting the coating liquid of aqueous solution form or water emulsion form to directly coat fertilizer, fertilizer often can be dissolved in the coating liquid of aqueous solution form or water emulsion form, therefore make containing fertilizer in the coating film layer of formation, When drying into a film, the fertilizer in it will be precipitated in the shape of needles in the coated film layer, which will become a fast dissolution channel for the fertilizer to pass through the film layer, reduce the barrier property of the film layer to the fertilizer, and make the prepared coated slow-release fertilizer The release period is shortened, and the fertilizer in the film layer will also reduce the film strength, requiring a thicker film thickness. Therefore, when the coating liquid in the form of aqueous solution or water emulsion is used to coat the fertilizer to prepare the coated slow-release fertilizer, how to prevent the fertilizer from entering the film layer formed by the coating is a difficult problem. When some researchers use polyacrylate emulsion to coat urea to prepare polyacrylate coated slow-release urea, they first spray a thin layer of paraffin film or sulfur film on the surface of urea, and then use polyacrylate emulsion. A method of coating urea. Since the melting point of paraffin is usually lower than 75°C, a thin layer of paraffin film is sprayed first, and then polyacrylate emulsion is used to coat urea, and then the water in the polyacrylate emulsion is volatilized to form a polyacrylate film layer. When drying under normal pressure, the temperature must be lower than 75°C, so the water removal speed in the film layer is very low, and the drying film formation speed is very slow; if you want to increase the drying and water removal speed, you need to use vacuum drying, and the vacuum drying process complex. There is also a problem in the method of spraying a thin layer of sulfur film on the surface of urea, and then using polyacrylate emulsion to coat the urea. The equipment and process for spraying the sulfur film are complicated, and the prepared coating Type slow-release fertilizers contain sulfur, and the soil quality of some application occasions does not want sulfur to enter the soil layer, so this method also has certain problems.

三、发明内容3. Contents of the invention

本发明的目的在于提供一种经济有效的水乳液型和水溶液型胶粘剂包膜肥料的方法。The object of the present invention is to provide an economical and effective water emulsion type and water solution type adhesive coating fertilizer method.

实现本发明目的的技术解决方案为:一种采用水乳液型和水溶液型胶粘剂包膜肥料的方法,依次包括以下步骤:第一步,采用熔体型和/或有机溶液型包膜液对肥料进行包膜,在肥料表面形成疏水性有机物膜层;第二步,采用水乳液型和/或水溶液型胶粘剂对表面有疏水性有机物膜层的预包膜肥料进行包膜,最终得到包膜型缓释肥料。其中,疏水性有机物膜层可以是疏水性低分子有机物膜层、疏水性聚合物膜层或者疏水性低分子有机物膜层与疏水性聚合物膜层的复合膜层,疏水性低分子有机物的熔点或软化点≥76℃。The technical solution that realizes the object of the present invention is: a kind of method that adopts water emulsion type and aqueous solution type adhesive coating fertilizer, comprises the following steps successively: the first step, adopts melt type and/or organic solution type coating liquid to fertilizer Coating is performed to form a hydrophobic organic film on the surface of the fertilizer; in the second step, the pre-coated fertilizer with a hydrophobic organic film on the surface is coated with an aqueous emulsion type and/or aqueous solution adhesive, and finally a coated fertilizer is obtained. slow release fertilizer. Wherein, the hydrophobic organic film layer can be a hydrophobic low molecular organic film layer, a hydrophobic polymer film layer or a composite film layer of a hydrophobic low molecular organic film layer and a hydrophobic polymer film layer, and the melting point of the hydrophobic low molecular organic film layer is Or softening point ≥ 76 ℃.

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,疏水性低分子有机物可以是软化点≥76℃的松香酯及其混合物和熔点或软化点≥76℃的氯化石蜡及其混合物等中的一种或多种。In the method of using water emulsion type and water solution type adhesive to coat fertilizer in the present invention, the hydrophobic low-molecular organic matter can be rosin esters with a softening point ≥ 76°C and mixtures thereof, and chlorinated paraffins with a melting point or softening point ≥ 76°C and mixtures thereof one or more of these.

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,疏水性聚合物可以是疏水性热塑性聚合物,也可以是疏水性热固性聚合物,还可以即有疏水性热塑性聚合物又有疏水性热固性聚合物。疏水性热固性聚合物可以是聚氨酯、环氧树脂、不饱和聚酯、酚醛树脂、呋喃树脂、不饱和油树脂、顺丁橡胶、天然橡胶、聚异戊二烯橡胶、丁苯橡胶、丁腈橡胶、丁基橡胶和乙丙橡胶及三元乙丙橡胶等中的一种或多种。疏水性热塑性聚合物可以是聚烯烃及其共聚物、聚苯乙烯及其共聚物、聚氯乙烯及其共聚物、热塑性聚酯、ABS树脂、石油树脂和古马隆-茚树脂等中的一种或多种。In the method of the present invention adopting water emulsion type and aqueous solution type adhesive coating fertilizer, the hydrophobic polymer can be a hydrophobic thermoplastic polymer, also can be a hydrophobic thermosetting polymer, can also have both a hydrophobic thermoplastic polymer and a hydrophobic permanent thermosetting polymers. The hydrophobic thermosetting polymer can be polyurethane, epoxy resin, unsaturated polyester, phenolic resin, furan resin, unsaturated oleoresin, butadiene rubber, natural rubber, polyisoprene rubber, styrene-butadiene rubber, nitrile rubber One or more of butyl rubber, ethylene propylene rubber and EPDM rubber, etc. The hydrophobic thermoplastic polymer can be one of polyolefin and its copolymer, polystyrene and its copolymer, polyvinyl chloride and its copolymer, thermoplastic polyester, ABS resin, petroleum resin and coumarone-indene resin, etc. one or more species.

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,采用的水乳液型胶粘剂为聚合物乳液胶粘剂,采用的水溶液型胶粘剂可以是水溶液型聚合物胶粘剂和水溶液型无机胶粘剂中的一种或多种。In the method of using water emulsion type and water solution type adhesive to coat fertilizer in the present invention, the water emulsion type adhesive used is a polymer emulsion adhesive, and the water solution type adhesive used can be a kind of water solution type polymer adhesive and water solution type inorganic adhesive or more.

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,包膜用的聚合物乳液胶粘剂可以是聚丙烯酸酯及其共聚物乳液、聚醋酸乙烯酯及其共聚物乳液、聚苯乙烯及其共聚物乳液、聚氯乙烯及其共聚物乳液、聚偏二氯乙烯及其共聚物乳液、聚烯烃及其共聚物乳液、环氧树脂乳液和聚氨酯乳液等中的一种或多种。包膜用的水溶液型聚合物胶粘剂可以是氨基树脂预聚物溶液和聚乙烯醇及其共聚物的缩醛树脂溶液等中的一种或多种。包膜用的水溶液型无机胶粘剂可以是磷酸盐胶粘剂和硅酸盐胶粘剂等中的一种或多种。In the method that the present invention adopts water emulsion type and aqueous solution type adhesive coating fertilizer, the polymer emulsion adhesive agent of coating can be polyacrylic acid ester and copolymer emulsion thereof, polyvinyl acetate and copolymer emulsion thereof, polystyrene and One or more of its copolymer emulsion, polyvinyl chloride and its copolymer emulsion, polyvinylidene chloride and its copolymer emulsion, polyolefin and its copolymer emulsion, epoxy resin emulsion and polyurethane emulsion, etc. The aqueous solution polymer adhesive used for coating may be one or more of amino resin prepolymer solution, polyvinyl alcohol and its copolymer acetal resin solution, and the like. The aqueous solution type inorganic adhesive used for coating may be one or more of phosphate adhesive, silicate adhesive and the like.

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,疏水性有机物膜层的厚度可以为2~25μm。In the method of the present invention adopting the water emulsion type and the water solution type adhesive to coat the fertilizer, the thickness of the hydrophobic organic film layer can be 2-25 μm.

与现有技术相比,本发明具有显著的优点。本发明水乳液型和水溶液型胶粘剂包膜肥料的方法可以避免采用水溶液形式或水乳液形式的包膜液进行包膜时肥料进入形成的包膜膜层中,特别是包膜工艺简单,并且水乳液型和水溶液型胶粘剂进行包膜时的常压干燥脱水温度可以较高,膜层的干燥成膜速度快,因此工艺成本低。Compared with the prior art, the present invention has significant advantages. The method of water emulsion type and aqueous solution type adhesive coating fertilizer of the present invention can avoid that fertilizer enters in the coating film layer that forms when adopting the coating liquid of aqueous solution form or water emulsion form to carry out coating, and particularly coating process is simple, and water The normal pressure drying and dehydration temperature can be higher when the emulsion type and the aqueous solution type adhesive are coated, and the drying and film forming speed of the film layer is fast, so the process cost is low.

四、具体实施方式4. Specific implementation

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法,依次包括以下步骤:第一步,采用熔体型和/或有机溶液型包膜液对肥料进行包膜,在肥料表面形成疏水性有机物膜层;第二步,采用水乳液型和/或水溶液型胶粘剂对表面有疏水性有机物膜层的预包膜肥料进行包膜,最终得到包膜型缓释肥料。其中,疏水性有机物膜层可以是疏水性低分子有机物膜层、疏水性聚合物膜层或者疏水性低分子有机物膜层与疏水性聚合物膜层的复合膜层,疏水性低分子有机物的熔点或软化点≥76℃。The present invention adopts the method for coating fertilizer of water emulsion type and aqueous solution type adhesive, comprises the following steps successively: the first step, adopts melt type and/or organic solution type coating liquid to coat fertilizer, forms hydrophobicity on the surface of fertilizer Organic film layer; in the second step, the pre-coated fertilizer with a hydrophobic organic film layer on the surface is coated with a water emulsion type and/or aqueous solution type adhesive, and finally a coated slow-release fertilizer is obtained. Wherein, the hydrophobic organic film layer can be a hydrophobic low molecular organic film layer, a hydrophobic polymer film layer or a composite film layer of a hydrophobic low molecular organic film layer and a hydrophobic polymer film layer, and the melting point of the hydrophobic low molecular organic film layer is Or softening point ≥ 76 ℃.

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,采用有机溶液型包膜液对肥料进行包膜以在肥料表面形成疏水性有机物膜层时,有机溶液型包膜液中的有机溶剂要选用对肥料溶解性低的有机溶剂种类。比如,采用有机溶液型包膜液对尿素预包膜时,不要选用乙醇等对尿素溶解性强的有机溶剂。In the method that the present invention adopts water emulsion type and aqueous solution type adhesive coating fertilizer, adopts organic solution type coating liquid to coat fertilizer to form hydrophobic organic matter film layer on the fertilizer surface, the organic in the organic solution type coating liquid The solvent should be selected from organic solvents with low solubility to fertilizers. For example, when using an organic solution-type coating solution to pre-coat urea, do not use organic solvents such as ethanol that are highly soluble to urea.

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,第一步中采用的疏水性低分子有机物可以是软化点≥76℃的松香酯及其混合物和熔点或软化点≥76℃的氯化石蜡及其混合物中的一种或多种,当然也可以是熔点或软化点≥76℃的其它疏水性低分子有机物。In the method of the present invention adopting water emulsion type and aqueous solution type adhesive coating fertilizer, the hydrophobic low-molecular organic matter adopted in the first step can be rosin esters with a softening point ≥ 76°C and mixtures thereof, and rosin esters with a melting point or softening point ≥ 76°C One or more of chlorinated paraffins and their mixtures, of course, can also be other hydrophobic low-molecular organic substances with melting point or softening point ≥ 76°C.

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,疏水性聚合物可以是疏水性热塑性聚合物,也可以是疏水性热固性聚合物,还可以即有疏水性热塑性聚合物又有疏水性热固性聚合物。疏水性热固性聚合物可以是聚氨酯、环氧树脂、不饱和聚酯、酚醛树脂、呋喃树脂、不饱和油树脂、顺丁橡胶、天然橡胶、聚异戊二烯橡胶、丁苯橡胶、丁腈橡胶、丁基橡胶和乙丙橡胶及三元乙丙橡胶中的一种或多种。疏水性热塑性聚合物可以是聚烯烃及其共聚物、聚苯乙烯及其共聚物、聚氯乙烯及其共聚物、热塑性聚酯、ABS树脂、石油树脂和古马隆-茚树脂中的一种或多种。当然,也可以是或可以含有可以采用熔体形式或有机溶液形式进行包膜的其它疏水性热塑性聚合物和疏水性热固性聚合物。其中,低分子量的聚合物是优选,比如聚乙烯蜡、聚异丁烯等低分子量聚烯烃以及石油树脂、古马隆-茚树脂、苯乙烯-茚树脂、芳香烃树脂等低分子量树脂,它们的分子量低,它们包膜时包膜液可以是熔体形式或有机溶剂用量低的有机溶液,同时它们为非极性或极性很低,形成的膜层的阻透性很高,可以为整个包膜提供高的阻透性,当然它们的流动温度应≥76℃。对于非极性或低极性聚合物乳液(如聚烯烃及其共聚物乳液、聚苯乙烯及其共聚物乳液)包膜肥料,聚氨酯、环氧树脂、不饱和聚酯、酚醛树脂、呋喃树脂和不饱和油树脂等可以是优选,尽管它们形成的膜层的阻透性不高,不能为整个包膜的阻透性提供贡献,但是它们包膜时采用的包膜液通常使用预聚物,通常可以是熔体形式,不使用有机溶剂。对于高极性聚合物乳液(如聚丙烯酸酯及其共聚物乳液、聚醋酸乙烯酯及其共聚物乳液、聚氯乙烯及其共聚物乳液和聚偏二氯乙烯及其共聚物乳液等)包膜肥料,也可优先考虑采用聚烯烃及其非极性共聚物、聚苯乙烯及其非极性共聚物、顺丁橡胶、天然橡胶、聚异戊二烯橡胶、丁苯橡胶、丁基橡胶和乙丙橡胶及三元乙丙橡胶等非极性聚合物去形成疏水性膜层,尽管他们需采用有机溶液进行包膜,但它们形成的疏水性非极性聚合物膜层的阻透性很高,可以为整个包膜提供高的阻透性。采用橡胶类聚合物(如顺丁橡胶、天然橡胶、聚异戊二烯橡胶、丁苯橡胶、丁腈橡胶、丁基橡胶和乙丙橡胶及三元乙丙橡胶等)有机溶液进行包膜而形成的疏水性膜层,可以硫化(或交联)也可以不硫化(或交联)。In the method of the present invention adopting water emulsion type and aqueous solution type adhesive coating fertilizer, the hydrophobic polymer can be a hydrophobic thermoplastic polymer, also can be a hydrophobic thermosetting polymer, can also have both a hydrophobic thermoplastic polymer and a hydrophobic permanent thermosetting polymers. The hydrophobic thermosetting polymer can be polyurethane, epoxy resin, unsaturated polyester, phenolic resin, furan resin, unsaturated oleoresin, butadiene rubber, natural rubber, polyisoprene rubber, styrene-butadiene rubber, nitrile rubber One or more of butyl rubber, ethylene propylene rubber and EPDM rubber. The hydrophobic thermoplastic polymer can be one of polyolefin and its copolymer, polystyrene and its copolymer, polyvinyl chloride and its copolymer, thermoplastic polyester, ABS resin, petroleum resin and coumarone-indene resin or more. Of course, other hydrophobic thermoplastic polymers and hydrophobic thermoset polymers that can be coated from the melt or from an organic solution can also be or be included. Among them, low-molecular-weight polymers are preferred, such as low-molecular-weight polyolefins such as polyethylene wax and polyisobutylene, and low-molecular-weight resins such as petroleum resins, coumarone-indene resins, styrene-indene resins, and aromatic hydrocarbon resins. Their molecular weight Low, when they are coated, the coating solution can be in the form of a melt or an organic solution with a low amount of organic solvent. At the same time, they are non-polar or very low in polarity. Membranes provide high barrier properties, of course their flow temperature should be ≥ 76°C. For non-polar or low-polar polymer emulsion (such as polyolefin and its copolymer emulsion, polystyrene and its copolymer emulsion) coated fertilizer, polyurethane, epoxy resin, unsaturated polyester, phenolic resin, furan resin And unsaturated oleoresin, etc. can be preferred, although the barrier properties of the film layer formed by them are not high, and cannot contribute to the barrier property of the entire coating, but the coating liquid used in their coating usually uses prepolymer , usually in the form of a melt, without the use of organic solvents. For highly polar polymer emulsions (such as polyacrylate and its copolymer emulsion, polyvinyl acetate and its copolymer emulsion, polyvinyl chloride and its copolymer emulsion, polyvinylidene chloride and its copolymer emulsion, etc.) Membrane fertilizer, polyolefin and its non-polar copolymers, polystyrene and its non-polar copolymers, butadiene rubber, natural rubber, polyisoprene rubber, styrene-butadiene rubber, butyl rubber can also be given priority And non-polar polymers such as ethylene-propylene rubber and EPDM rubber to form a hydrophobic film layer, although they need to use an organic solution for coating, but the barrier properties of the hydrophobic non-polar polymer film layer formed by them Very high, providing high barrier properties to the entire envelope. The organic solution of rubber polymers (such as butadiene rubber, natural rubber, polyisoprene rubber, styrene-butadiene rubber, nitrile rubber, butyl rubber, ethylene-propylene rubber and EPDM rubber, etc.) is used for coating. The formed hydrophobic film layer can be vulcanized (or cross-linked) or not vulcanized (or cross-linked).

预包膜肥料时在肥料表面形成的疏水性有机物膜层中可以含有填料等添加物。本发明中疏水性聚合物与疏水性低分子有机物的混合物膜层也看作疏水性聚合物膜层,此时混合物中的疏水性低分子有机物的熔点或软化点可以低于76℃,但疏水性聚合物与疏水性低分子有机物的混合物的流动温度应≥76℃,这里的流动温度是指靠自重就可明显流动的温度。Additives such as fillers may be contained in the hydrophobic organic film layer formed on the surface of the fertilizer when pre-coating the fertilizer. In the present invention, the mixture film layer of hydrophobic polymer and hydrophobic low-molecular organic matter is also regarded as hydrophobic polymer film layer. At this time, the melting point or softening point of the hydrophobic low-molecular organic matter in the mixture can be lower than 76 ° C, but the hydrophobic The flow temperature of the mixture of non-toxic polymer and hydrophobic low-molecular organic matter should be ≥ 76 ° C, where the flow temperature refers to the temperature that can flow obviously by its own weight.

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,既可以采用水乳液型胶粘剂,也可以采用水溶液型胶粘剂,还可以同时采用水乳液型胶粘剂和水溶液型胶粘剂,可以是水乳液型胶粘剂和水溶液型胶粘剂的混合型胶粘剂.采用的水乳液型胶粘剂为聚合物乳液胶粘剂.采用的水溶液型胶粘剂可以是水溶液型聚合物胶粘剂,也可以是水溶液型无机胶粘剂,还可以同时采用水溶液型聚合物胶粘剂和水溶液型无机胶粘剂.In the method of using water emulsion type and water solution type adhesive to coat fertilizer in the present invention, both water emulsion type adhesive and water solution type adhesive can be used, water emulsion type adhesive and water solution type adhesive can also be used at the same time, it can be water emulsion type Mixed adhesive of adhesive and aqueous solution adhesive. The water emulsion adhesive used is a polymer emulsion adhesive. The aqueous solution adhesive used can be an aqueous solution polymer adhesive or an aqueous solution inorganic adhesive. Adhesives and water-based inorganic adhesives.

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,包膜采用的聚合物乳液型胶粘剂可以是聚丙烯酸酯及其共聚物乳液、聚醋酸乙烯酯及其共聚物乳液、聚苯乙烯及其共聚物乳液、聚氯乙烯及其共聚物乳液、聚偏二氯乙烯及其共聚物乳液、聚烯烃及其共聚物乳液、环氧树脂乳液和聚氨酯乳液等中的一种或多种。包膜用的水溶液型聚合物胶粘剂可以是氨基树脂预聚物溶液和聚乙烯醇及其共聚物的缩醛树脂溶液等中的一种或多种。包膜用的水溶液型无机胶粘剂可以是磷酸盐胶粘剂和硅酸盐胶粘剂等中的一种或多种。比如,水溶液型无机胶粘剂可以是下列之一种或多种硅酸盐胶粘剂:①模数为1~3的硅酸钠与磷酸的混合水溶液;②模数为1~3的硅酸钾与磷酸的混合水溶液;③SiO2溶胶。采用的水溶液型胶粘剂可以是水溶液型聚合物胶粘剂和水溶液型无机胶粘剂的混合型胶粘剂,比如,聚乙烯醇(缩醛)树脂与硅酸钾组成的混合水溶液、脲醛树脂预聚物与硅酸钠组成的混合水溶液等混合型胶粘剂。In the method that the present invention adopts water emulsion type and aqueous solution type adhesive to coat fertilizer, the polymer emulsion type adhesive that coating adopts can be polyacrylate and its copolymer emulsion, polyvinyl acetate and its copolymer emulsion, polystyrene One or more of polyvinyl chloride and its copolymer emulsion, polyvinyl chloride and its copolymer emulsion, polyvinylidene chloride and its copolymer emulsion, polyolefin and its copolymer emulsion, epoxy resin emulsion and polyurethane emulsion, etc. The aqueous solution polymer adhesive used for coating may be one or more of amino resin prepolymer solution, polyvinyl alcohol and its copolymer acetal resin solution, and the like. The aqueous solution type inorganic adhesive used for coating may be one or more of phosphate adhesive, silicate adhesive and the like. For example, the aqueous solution-type inorganic adhesive can be one or more of the following silicate adhesives: ① a mixed aqueous solution of sodium silicate and phosphoric acid with a modulus of 1 to 3; ② potassium silicate and phosphoric acid with a modulus of 1 to 3 Mixed aqueous solution; ③ SiO 2 sol. The aqueous solution adhesive used can be a mixed adhesive of aqueous solution polymer adhesive and aqueous solution inorganic adhesive, for example, a mixed aqueous solution composed of polyvinyl alcohol (acetal) resin and potassium silicate, urea formaldehyde resin prepolymer and sodium silicate Mixed adhesives such as mixed aqueous solutions.

当然,本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,采用的水乳液型胶粘剂和水溶液型胶粘剂中可以有填料等添加物。Of course, in the method of the present invention using water-emulsion-type and aqueous-solution-type adhesives to coat fertilizers, the water-emulsion-type adhesives and aqueous-solution-type adhesives used may contain additives such as fillers.

本发明采用水乳液型和水溶液型胶粘剂包膜肥料的方法中,在肥料表面预包覆的疏水性有机物膜层只要是完整或基本完整的即可,因此其厚度不要求太高,通常2~25μm即可。当然,厚度更大也可以。In the method of using water emulsion type and aqueous solution type adhesive to coat fertilizer in the present invention, the hydrophobic organic matter film layer pre-coated on the surface of the fertilizer only needs to be complete or basically complete, so its thickness does not require too high, usually 2~ 25 μm is enough. Of course, a larger thickness is also possible.

下面以采用水乳液型和水溶液型胶粘剂包膜工业粒状尿素制备包膜型缓释尿素的个别实例来说明采用水乳液型和水溶液型胶粘剂包膜肥料方法的部分具体实施方式。Some specific implementations of the method for coating fertilizers with water emulsion and water solution adhesives will be described below with individual examples of preparing coated slow-release urea by using water emulsion and water solution adhesives to coat industrial granular urea.

实施例1Example 1

将粒状工业尿素加入流化床包膜设备中,并使粒状尿素处于沸腾状态,流化床中粒状尿素温度保持在90℃。将4、4-二苯基甲烷二异氰酸酯MDI、三乙醇胺和二乙二醇的混合物(混合物中三乙醇胺∶二乙二醇的摩尔比为0.2∶1,-NCO∶-OH的摩尔比为1.1∶1,含少量催化剂)喷涂于粒状尿素表面,喷涂直到形成的聚氨酯膜层厚度达到15μm。然后,喷涂聚苯乙烯乳液于聚氨酯膜层表面,喷涂直到形成的聚苯乙烯膜层厚度达到90μm。逐渐升温至100℃,充分干燥除去膜层中含水,即制备得到采用聚苯乙烯乳液进行包膜的缓释尿素。Add granular industrial urea into the fluidized bed coating equipment, and keep the granular urea in a boiling state, and keep the temperature of the granular urea in the fluidized bed at 90°C. The mixture of 4,4-diphenylmethane diisocyanate MDI, triethanolamine and diethylene glycol (the molar ratio of triethanolamine in the mixture: diethylene glycol is 0.2: 1, and the molar ratio of -NCO: -OH is 1.1 : 1, containing a small amount of catalyst) sprayed on the surface of granular urea, and sprayed until the thickness of the polyurethane film layer formed reaches 15 μm. Then, spray the polystyrene emulsion on the surface of the polyurethane film until the thickness of the formed polystyrene film reaches 90 μm. Gradually raise the temperature to 100° C., fully dry to remove water in the film layer, and then prepare the slow-release urea coated with polystyrene emulsion.

实施例2Example 2

将粒状工业尿素加入控温80℃的转鼓包膜设备中,转动转鼓(转速40r/min)使粒状尿素在转鼓内流动。将松香酯(软化点为100℃)熔体喷涂于粒状尿素表面,喷涂直到形成的松香酯膜层厚度达到20μm。然后将转鼓内的粒状尿素温度升至95℃,再喷涂丁苯乳液于松香酯膜层表面,喷涂直到丁苯乳液形成的丁苯共聚物膜层厚度达到90μm。充分干燥除去膜层中含水,即制备得到采用丁苯乳液进行包膜的缓释尿素。Add granular industrial urea to the drum coating equipment with a temperature control of 80°C, and rotate the drum (rotating speed 40r/min) to make the granular urea flow in the drum. Spray the melt of rosin ester (softening point: 100° C.) on the surface of granular urea until the thickness of the formed rosin ester film reaches 20 μm. Then raise the temperature of the granular urea in the drum to 95°C, and then spray the styrene-butadiene emulsion on the surface of the rosin ester film until the thickness of the styrene-butadiene copolymer film formed by the styrene-butadiene emulsion reaches 90 μm. The water in the film layer is fully dried to remove the slow-release urea coated with the styrene-butadiene emulsion.

实施例3Example 3

将粒状工业尿素加入控温80℃的转鼓包膜设备中,转动转鼓(转速40r/min)使粒状尿素在转鼓内流动.将聚乙烯的松节油溶液喷涂于粒状尿素表面,喷涂直到形成的聚乙烯膜层厚度达到10μm.然后将转鼓内的粒状尿素温度升至95℃,再喷涂由聚乙烯醇缩甲醛树脂水溶液和模数为1~3的硅酸钾与磷酸的水溶液组成的混合水溶液于聚乙烯膜层表面,喷涂直到形成的聚乙烯醇缩甲醛树脂与硅酸盐复合物膜层厚度达到130μm.逐渐升温至100℃,充分干燥除去膜层中含水,并使聚乙烯醇缩甲醛树脂充分固化和硅酸盐充分胶凝,即制备得到采用由聚乙烯醇缩甲醛树脂水溶液和模数为1~3的硅酸钾与磷酸的水溶液组成的混合水溶液进行包膜的缓释尿素.Add granular industrial urea to the drum coating equipment with a temperature control of 80°C, and rotate the drum (rotating speed 40r/min) to make the granular urea flow in the drum. Spray the polyethylene turpentine solution on the surface of the granular urea until it forms The thickness of the polyethylene film layer reaches 10μm. Then the temperature of the granular urea in the drum is raised to 95°C, and then sprayed with a polyvinyl formal resin aqueous solution and an aqueous solution of potassium silicate and phosphoric acid with a modulus of 1 to 3. Mix the aqueous solution on the surface of the polyethylene film layer, spray until the thickness of the polyvinyl formal resin and silicate composite film layer reaches 130 μm. Gradually raise the temperature to 100 ° C, fully dry to remove the water in the film layer, and make the polyvinyl alcohol The formal resin is fully cured and the silicate is fully gelled, that is, the slow-release film is prepared by using a mixed aqueous solution composed of a polyvinyl formal resin aqueous solution and an aqueous solution of potassium silicate and phosphoric acid with a modulus of 1-3. urea.

实施例4Example 4

将粒状工业尿素加入控温65℃的转鼓包膜设备中,转动转鼓(转速40r/min)使粒状尿素在转鼓内流动。将苯乙烯-丁二烯-苯乙烯嵌段共聚物环己烷溶液喷涂于粒状尿素表面,喷涂直到形成的苯乙烯-丁二烯-苯乙烯嵌段共聚物膜层厚度达到6μm,充分干燥除去膜层中的环己烷。然后将转鼓内的粒状尿素温度升至95℃,再喷涂聚丙烯酸酯乳液(丙烯酸甲酯与丙烯酸丁酯的共聚物乳液,丙烯酸甲酯与丙烯酸丁酯的摩尔比为1∶0.2)于苯乙烯-丁二烯-苯乙烯嵌段共聚物膜层表面,喷涂直到形成的聚丙烯酸酯膜层厚度达到110μm。逐渐升温至100℃,充分干燥除去膜层中含水,即制备得到采用聚丙烯酸酯乳液进行包膜的缓释尿素。Add granular industrial urea to the drum coating equipment with a temperature control of 65°C, and rotate the drum (rotating speed 40r/min) to make the granular urea flow in the drum. Spray the styrene-butadiene-styrene block copolymer cyclohexane solution on the surface of granular urea, spray until the thickness of the formed styrene-butadiene-styrene block copolymer film reaches 6 μm, fully dry and remove Cyclohexane in the film layer. Then the temperature of granular urea in the drum was raised to 95°C, and then sprayed with polyacrylate emulsion (copolymer emulsion of methyl acrylate and butyl acrylate, the molar ratio of methyl acrylate and butyl acrylate was 1:0.2) on benzene The surface of the ethylene-butadiene-styrene block copolymer film layer is sprayed until the thickness of the formed polyacrylate film layer reaches 110 μm. Gradually raise the temperature to 100°C, fully dry to remove the water in the film layer, and then prepare the slow-release urea coated with polyacrylate emulsion.

实施例5Example 5

将粒状工业尿素加入控温70℃的转鼓包膜设备中,转动转鼓(转速40r/min)使粒状尿素在转鼓内流动。将石油树脂(软化点为100℃)熔体慢慢喷涂于粒状尿素表面,喷除直到形成的石油树脂膜层厚度达到20μm。然后将转鼓内的粒状尿素温度升至95℃,再喷涂聚醋酸乙烯酯乳液于石油树脂膜层表面,喷涂直到形成的聚醋酸乙烯酯膜层厚度达到85μm。逐渐升温至98℃,充分干燥除去膜层中含水,即制备得到采用聚醋酸乙烯酯乳液进行包膜的缓释尿素。Add granular industrial urea to the drum coating equipment with a temperature control of 70°C, and rotate the drum (rotating speed 40r/min) to make the granular urea flow in the drum. Slowly spray the melted petroleum resin (with a softening point of 100° C.) on the surface of the granular urea, and spray until the thickness of the formed petroleum resin film reaches 20 μm. Then raise the temperature of the granular urea in the drum to 95°C, and then spray polyvinyl acetate emulsion on the surface of the petroleum resin film until the thickness of the formed polyvinyl acetate film reaches 85 μm. Gradually raise the temperature to 98°C, fully dry to remove the water in the film layer, and then prepare the slow-release urea coated with polyvinyl acetate emulsion.

实施例6Example 6

将粒状工业尿素加入控温70℃的转鼓包膜设备中,转动转鼓(转速40r/min)使粒状尿素在转鼓内流动。将聚乙烯蜡(熔点为105℃)的松节油溶液慢慢喷涂于粒状尿素表面,喷涂直到形成的聚乙烯蜡膜层厚度达到25μm。然后将转鼓内的粒状尿素温度升至95℃,再喷涂模数为1~3的硅酸钠与磷酸的混合水溶液于聚乙烯蜡膜层表面,喷涂直到形成的硅酸盐膜层厚度达到130μm。逐渐升温至100℃,充分干燥除去膜层中含水,并使硅酸盐充分胶凝,即制备得到采用模数为1~3的硅酸钠与磷酸的混合水溶液进行包膜的缓释尿素。Add granular industrial urea to the drum coating equipment with a temperature control of 70°C, and rotate the drum (rotating speed 40r/min) to make the granular urea flow in the drum. Slowly spray the turpentine solution of polyethylene wax (melting point is 105° C.) on the surface of granular urea until the thickness of the formed polyethylene wax film reaches 25 μm. Then raise the temperature of the granular urea in the drum to 95°C, and then spray the mixed aqueous solution of sodium silicate and phosphoric acid with a modulus of 1 to 3 on the surface of the polyethylene wax film until the thickness of the formed silicate film reaches 130 μm. Gradually raise the temperature to 100°C, fully dry to remove the water in the film layer, and fully gel the silicate, that is, prepare the slow-release urea coated with the mixed aqueous solution of sodium silicate and phosphoric acid with a modulus of 1-3.

实施例7Example 7

将粒状工业尿素加入控温80℃的转鼓包膜设备中,转动转鼓(转速40r/min)使粒状尿素在转鼓内流动。将桐油喷涂于粒状尿素表面,喷涂直到形成的桐油树脂膜层厚度达到15μm,使桐油树脂膜层适当固化。然后将转鼓内的粒状尿素温度升至95℃,再喷涂丁苯乳液于桐油树脂膜层表面,喷涂直到丁苯乳液形成的丁苯共聚物膜层厚度达到90μm。充分干燥除去膜层中含水,并使桐油树脂膜层充分固化,即制备得到采用丁苯乳液进行包膜的缓释尿素。Add granular industrial urea to the drum coating equipment with a temperature control of 80°C, and rotate the drum (rotating speed 40r/min) to make the granular urea flow in the drum. Tung oil is sprayed on the granular urea surface until the thickness of the formed tung oil resin film layer reaches 15 μm, so that the tung oil resin film layer is properly cured. Then, the temperature of granular urea in the drum was raised to 95° C., and then the styrene-butadiene emulsion was sprayed on the surface of the tung oil resin film until the thickness of the styrene-butadiene copolymer film formed by the styrene-butadiene emulsion reached 90 μm. Fully dry to remove water in the film layer, and fully solidify the tung oil resin film layer, that is, prepare the slow-release urea coated with the styrene-butadiene emulsion.

实施例8Example 8

将粒状工业尿素加入控温65℃的转鼓包膜设备中,转动转鼓(转速40r/min)使粒状尿素在转鼓内流动.将丁苯橡胶生胶的溶剂汽油溶液喷涂于粒状尿素表面,喷涂直到形成的丁苯橡胶生胶膜层厚度达到15μm.然后将转鼓内的粒状尿素温度升至95℃,再喷涂丁苯乳液于丁苯橡胶生胶膜层表面,喷涂直到丁苯乳液形成的丁苯共聚物膜层厚度达到90μm.充分干燥除去膜层中含水,即制备得到采用丁苯乳液进行包膜的缓释尿素.Add granular industrial urea to the drum coating equipment with a temperature control of 65°C, and rotate the drum (rotating speed 40r/min) to make the granular urea flow in the drum. Spray the solvent gasoline solution of styrene-butadiene rubber raw rubber on the surface of the granular urea , spray until the thickness of the formed styrene-butadiene rubber film layer reaches 15 μm. Then raise the temperature of the granular urea in the drum to 95°C, and then spray the styrene-butadiene emulsion on the surface of the styrene-butadiene rubber film layer until the styrene-butadiene emulsion The thickness of the formed styrene-butadiene copolymer film reached 90 μm. The water contained in the film was fully dried to prepare the slow-release urea coated with styrene-butadiene emulsion.

实施例9Example 9

将粒状工业尿素加入控温70℃的转鼓包膜设备中,转动转鼓(转速40r/min)使粒状尿素在转鼓内流动。将石油树脂(软化点为105℃)熔体慢慢喷涂于粒状尿素表面,喷涂直到形成的石油树脂膜层厚度达到20μm。然后将转鼓内的粒状尿素温度升至95℃,再喷涂脲醛树脂预聚物水溶液于石油树脂膜层表面,喷涂直到形成的脲醛树脂膜层厚度达到100μm。逐渐升温至100℃,充分干燥除去膜层中含水,即制备得到采用脲醛树脂预聚物水溶液进行包膜的缓释尿素。Add granular industrial urea to the drum coating equipment with a temperature control of 70°C, and rotate the drum (rotating speed 40r/min) to make the granular urea flow in the drum. Slowly spray the melt of petroleum resin (with a softening point of 105° C.) on the surface of granular urea until the thickness of the formed petroleum resin film reaches 20 μm. Then raise the temperature of the granular urea in the drum to 95°C, and then spray the aqueous solution of urea-formaldehyde resin prepolymer on the surface of the petroleum resin film until the thickness of the formed urea-formaldehyde resin film reaches 100 μm. Gradually raise the temperature to 100° C., fully dry to remove water in the film layer, and then prepare slow-release urea coated with an aqueous solution of urea-formaldehyde resin prepolymer.

实施例10Example 10

将粒状工业尿素加入流化床包膜设备中,并使粒状尿素处于沸腾状态,流化床中粒状尿素温度保持在70℃。将古马隆-茚树脂(软化点为80℃)熔体慢慢喷涂于粒状尿素表面,喷涂直到形成的古马隆-茚树脂膜层厚度达到20μm。然后将流化床中粒状尿素温度升至78℃,喷涂聚氯乙烯乳液于古马隆-茚树脂膜层表面,喷涂直到形成的聚氯乙烯膜层厚度达到80μm。鼓风干燥充分除去膜层中含水,即制备得到采用聚氯乙烯乳液进行包膜的缓释尿素。Add granular industrial urea to the fluidized bed coating equipment, and keep the granular urea in a boiling state, and keep the temperature of the granular urea in the fluidized bed at 70°C. Slowly spray the melt of coumarone-indene resin (with a softening point of 80° C.) on the surface of granular urea until the thickness of the formed coumarone-indene resin film reaches 20 μm. Then, the temperature of the granular urea in the fluidized bed was raised to 78° C., and the polyvinyl chloride emulsion was sprayed on the surface of the coumarone-indene resin film until the thickness of the formed polyvinyl chloride film reached 80 μm. Blast drying fully removes water in the film layer, and then the slow-release urea coated with polyvinyl chloride emulsion is prepared.

上述实施例制备得到的包膜型缓释尿素,在其由水乳液型和水溶液型胶粘剂进行包膜形成的膜层中基本没有尿素存在,其膜层阻水性比采用水乳液型和水溶液型胶粘剂直接对尿素进行包膜形成的膜层的阻水性强。The film-coated slow-release urea prepared in the above examples has basically no urea in the film layer formed by the water-emulsion-type and aqueous-solution-type adhesives, and the water resistance of the film is lower than that of the water-emulsion-type and aqueous-solution-type adhesives. The film layer formed by directly coating the urea has strong water resistance.

Claims (7)

1.一种采用水乳液型和/或水溶液型胶粘剂包膜肥料的方法,其特征在于:依次包括以下步骤:1. a kind of method that adopts water emulsion type and/or aqueous solution type adhesive coating fertilizer, is characterized in that: comprise the following steps successively: 第一步,采用熔体型和/或有机溶液型包膜液对肥料进行包膜,在肥料表面形成疏水性有机物膜层;In the first step, the fertilizer is coated with a melt-type and/or organic solution-type coating solution to form a hydrophobic organic film layer on the surface of the fertilizer; 第二步,采用水乳液型和/或水溶液型胶粘剂对表面有疏水性有机物膜层的预包膜肥料进行包膜,最终得到包膜型缓释肥料;In the second step, the pre-coated fertilizer with a hydrophobic organic film layer on the surface is coated with an aqueous emulsion type and/or aqueous solution type adhesive, and finally a coated slow-release fertilizer is obtained; 其中,疏水性有机物膜层为疏水性低分子有机物膜层、疏水性聚合物膜层或疏水性低分子有机物膜层与疏水性聚合物膜层的复合膜层;疏水性低分子有机物是软化点≥76℃的松香酯及其混合物和熔点或软化点≥76℃的氯化石蜡及其混合物中的一种或多种;疏水性聚合物为疏水性热塑性聚合物和/或疏水性热固性聚合物,疏水性热塑性聚合物为聚烯烃、聚苯乙烯、聚氯乙烯、ABS树脂、流动温度≥76℃的聚乙烯蜡、流动温度≥76℃的聚异丁烯、流动温度≥76℃的石油树脂、流动温度≥76℃的古马隆-茚树脂、流动温度≥76℃的苯乙烯-茚树脂和流动温度≥76℃的芳香烃树脂中的一种或多种。Wherein, the hydrophobic organic film layer is a hydrophobic low molecular organic film layer, a hydrophobic polymer film layer or a composite film layer of a hydrophobic low molecular organic film layer and a hydrophobic polymer film layer; the hydrophobic low molecular organic film layer is the softening point One or more of rosin esters ≥76°C and their mixtures and chlorinated paraffins with a melting point or softening point ≥76°C and their mixtures; hydrophobic polymers are hydrophobic thermoplastic polymers and/or hydrophobic thermosetting polymers , the hydrophobic thermoplastic polymer is polyolefin, polystyrene, polyvinyl chloride, ABS resin, polyethylene wax with flow temperature ≥76°C, polyisobutylene with flow temperature ≥76°C, petroleum resin with flow temperature ≥76°C, flow One or more of coumarone-indene resin with temperature ≥76°C, styrene-indene resin with flow temperature ≥76°C and aromatic hydrocarbon resin with flow temperature ≥76°C. 2.根据权利要求1所述的采用水乳液型和/或水溶液型胶粘剂包膜肥料的方法,其特征在于:疏水性热固性聚合物为聚氨酯、环氧树脂、不饱和聚酯、酚醛树脂、呋喃树脂、不饱和油树脂、顺丁橡胶、天然橡胶、聚异戊二烯橡胶、丁苯橡胶、丁腈橡胶、丁基橡胶和乙丙橡胶及三元乙丙橡胶中的一种或多种。2. the method for adopting water emulsion type and/or aqueous solution type adhesive coating fertilizer according to claim 1, is characterized in that: hydrophobic thermosetting polymer is polyurethane, epoxy resin, unsaturated polyester, phenolic resin, furan One or more of resin, unsaturated oleoresin, butadiene rubber, natural rubber, polyisoprene rubber, styrene-butadiene rubber, nitrile rubber, butyl rubber, ethylene-propylene rubber and EPDM rubber. 3.根据权利要求1所述的采用水乳液型和/或水溶液型胶粘剂包膜肥料的方法,其特征在于:采用的水乳液型胶粘剂为聚合物乳液胶粘剂。3. The method according to claim 1, wherein the water-emulsion type adhesive and/or aqueous solution type adhesive is used to coat the fertilizer, characterized in that: the water-emulsion type adhesive used is a polymer emulsion adhesive. 4.根据权利要求3所述的采用水乳液型和/或水溶液型胶粘剂包膜肥料的方法,其特征在于:聚合物乳液胶粘剂为聚丙烯酸酯乳液、聚醋酸乙烯酯乳液、聚苯乙烯及其共聚物乳液、聚氯乙烯乳液、聚偏二氯乙烯乳液、聚烯烃乳液、环氧树脂乳液和聚氨酯乳液中的一种或多种。4. the method for adopting water emulsion type and/or aqueous solution type adhesive coating fertilizer according to claim 3, is characterized in that: polymer emulsion adhesive is polyacrylate emulsion, polyvinyl acetate emulsion, polystyrene and its One or more of copolymer emulsion, polyvinyl chloride emulsion, polyvinylidene chloride emulsion, polyolefin emulsion, epoxy resin emulsion and polyurethane emulsion. 5.根据权利要求1所述的采用水乳液型和/或水溶液型胶粘剂包膜肥料的方法,其特征在于:采用的水溶液型胶粘剂为水溶液型聚合物胶粘剂和/或水溶液型无机胶粘剂。5. The method according to claim 1, wherein the water emulsion type and/or aqueous solution type adhesive coating fertilizer is characterized in that: the aqueous solution type adhesive used is an aqueous solution type polymer adhesive and/or an aqueous solution type inorganic adhesive. 6.根据权利要求5所述的采用水乳液型和/或水溶液型胶粘剂包膜肥料的方法,其特征在于:水溶液型聚合物胶粘剂为氨基树脂预聚物溶液和聚乙烯醇及其共聚物的缩醛树脂溶液中的一种或多种;水溶液型无机胶粘剂为磷酸盐胶粘剂和硅酸盐胶粘剂中的一种或多种。6. the method for adopting water emulsion type and/or aqueous solution type adhesive coating fertilizer according to claim 5, is characterized in that: aqueous solution type polymer adhesive is amino resin prepolymer solution and polyvinyl alcohol and copolymer thereof One or more of the acetal resin solution; the aqueous solution type inorganic adhesive is one or more of the phosphate adhesive and the silicate adhesive. 7.根据权利要求1~6任一项所述的采用水乳液型和/或水溶液型胶粘剂包膜肥料的方法,其特征在于:疏水性有机物膜层的厚度为2~25μm。7. The method for coating fertilizer with water emulsion type and/or water solution type adhesive according to any one of claims 1-6, characterized in that: the thickness of the hydrophobic organic film layer is 2-25 μm.
CN200510094536A 2005-09-26 2005-09-26 Method for coating fertilizer by emulsified and/or soluble adhesive Expired - Fee Related CN1939878B (en)

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