CN102986659A - Granulation method of novel pesticide water dispersible granules - Google Patents

Granulation method of novel pesticide water dispersible granules Download PDF

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Publication number
CN102986659A
CN102986659A CN 201110268519 CN201110268519A CN102986659A CN 102986659 A CN102986659 A CN 102986659A CN 201110268519 CN201110268519 CN 201110268519 CN 201110268519 A CN201110268519 A CN 201110268519A CN 102986659 A CN102986659 A CN 102986659A
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water dispersible
water
dispersible granules
agent
aqueous suspension
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赤国彤
赵康
庞民好
张汀
刘大群
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Heibei Agricultural University
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Heibei Agricultural University
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Abstract

The invention discloses a granulation method of a novel pesticide water dispersible granule, which aims to overcome the defects of a wet method and a dry method granulation as far as possible and combine the advantages of the two methods as far as possible, so as to achieve the purposes of saving energy, reducing pollution to the environment and improving the product performance by combining the dry method and the wet method. The key step is that the step of kneading water, a binder and wettable powder in a dry method is changed into the step of directly adding the aqueous suspending agent with the highest proportion as possible under the condition of not influencing the performance of extrusion granulation, so that the processed water dispersible granule has smaller particle size when dispersed in water, more environment-friendly and energy-saving production process and better suspension rate and dispersibility in water.

Description

A kind of prilling process of novel agrochemical water dispersible granules
Technical field
The invention belongs to formulations of pesticide field, the present invention relates to the manufacture method of the pesticide water dispersible granules such as a kind of novel insecticide, bactericide, weed killer herbicide.
Background technology
In a sense, water dispersible granules is the reprocessing on wetting powder or aqueous suspension agent basis.Its Recipe requires high, and manufacturing procedure is comparatively complicated.However because it has compared high-definition characteristic with conventional dosage forms, therefore quite favored.(1) water dispersible granules has widely adaptability to pesticide species and formulation content.(2) water dispersible granules has good matching to the super-high-efficient agricultural chemicals.(3) the water-dispersible grain agent producing process has diversity.That adopts at present usually has extruder grain, fluid-bed granulation, disk granulation, a mist projection granulating etc., and process choice is fully according to the physical and chemical performance of process agricultural chemicals, the machining process route of definite the best.(4) water dispersible granules has friendly to environment.The pollution of current chemical pesticide has become a serious social concern, in biopesticide complete today of substituting chemical pesticide also, how to reduce to greatest extent chemical pesticide to the pollution of environment, and it is very urgent to have become.
The distinct characteristic of these of water dispersible granules has determined that it has the not available unique advantage of conventional dosage forms, does not have dust from flying that is:, has reduced the pollution to environment, to user's safety, and can make that the toxic articles kind is low to be poisoned; Compare with suspending agent with wetting powder, active constituent content is high, and the product relative density is large, and volume is little, is convenient to packing, stores and transportation; Bin stability and physical and chemical stability are better, particularly to unsettled agricultural chemicals in water, make this formulation ensures active ingredient than suspending agent stability.
The prilling process of water dispersible granules is divided into " wet method " and " dry method "." wet method " is that former medicine, auxiliary agent, filler and water are mixed into suspension, carries out mist projection granulating again.The advantage of this technique be in the process of suspending agent without dust to the pollution of environment, can reduce energy consumption than wetting powder when making former medicine particle reach identical fineness, the suspensibility of product in water and dispersed relatively good; Shortcoming is in the mist projection granulating stage, will consume very high-energy because needing the TRANSIENT HIGH TEMPERATURE drying, and the finished granule rate is also low than " dry method " simultaneously; Some pesticide species can't adapt to the condition of high-temperature spray to thermo-responsive, and this has limited to the selectivity of processing technology greatly." dry method " is former medicine to be mixed with auxiliary agent, filler through ultramicro grinding make wetting powder, then adds suitable water and binding agent, disintegrant carries out extruder grain.The advantage of this technique is that the granulation stage is simple fast, free from environmental pollution, and energy consumption is low, and the finished granule rate is high; Shortcoming is more serious to the damage ratio of environment at wettable powder process segment dust, and energy consumption is high, and former powder directly is difficult to reach the fineness that is processed into aqueous suspension agent, and the suspensibility of product in water is about 80%, and dispersiveness is also poor;
Summary of the invention
The objective of the invention is to overcome as much as possible some shortcomings that two kinds of methods of " wet method " and " dry method " granulation exist separately, as much as possible do not combine simultaneously person's advantage, " doing wet method " of " dry method " and " wet method " the two combination saved the energy to reach, reduced the pollution of environment, the purpose of enhancing product performance.Its committed step is that the step that adds water, binding agent and wetting powder kneading in " dry method " is changed under the condition of the performance that does not affect extruding pelletization, directly add a high proportion of as far as possible aqueous suspension agent, thereby the particle diameter the when water dispersible granules that processes is disperseed is less, more environmental protection of production process, energy-conservation, while have more excellent suspensibility and dispersiveness in water in water.
Purpose of the present invention can reach by following measures:
A kind of new prilling process of water dispersible granules.At first former medicine, auxiliary agent, filler etc. are made ultra-fine wetting powder, its fineness is 800~1000 orders; Secondly former medicine, auxiliary agent, water etc. are ground through sand mill and make aqueous suspension agent, particle size range is 1~3um.Then wetting powder, aqueous suspension agent, disintegrant are added in the kneader simultaneously and mediate, make plastic material, at last this material is sent into Squeezinggranulator, carry out granulation, by drying, screening obtains the water dispersible granules product.The percentage of its each composition is:
Figure BSA00000571823300021
Its Central Plains cartridge bag is drawn together the agricultural chemicals such as various insecticides, bactericide, weed killer herbicide, such as Diacloden, first dimension salt, Imidacloprid, tribenuron-methyl, metsulfuron-methyl, bensulfuron-methyl, tpn etc.
The optional dispersant with water dispersible granules of dispersant wherein is such as lignosulfonates, alkylnaphthalene sulfonate, alkylbenzenesulfonate, naphthalene sulfonic acids and formaldehyde condensation products, thiazolinyl phenol polyethenoxy ether, alkylphenol-polyethenoxy polypropylene ether, alkylphenol polyoxyethylene formaldehyde condensation products sulphate, alkylphenol polyoxyethylene formaldehyde condensation products, polyoxyethylene carboxylate, petroleum sodium sulfonate etc.Preferred dispersant has lignosulfonates, alkylphenol polyoxyethylene formaldehyde condensation products sulphate, fatty alcohol-polyoxyethylene ether, aliphatic alcohol sodium sulfate, ethylene oxide propylene oxide block copolymer.
Wherein disintegrant can be selected the disintegrant of common moisture shot agent, such as starch, mineral salt, sodium carboxymethyl starch or polyvidone etc.Wherein preferred disintegrant is the mineral salt such as sodium sulphate, ammonium sulfate, ammonium chloride, sodium chloride or sodium chloride.
Wherein wetting agent can be selected the wetting agent of water dispersible granules commonly used; such as aliphatic alcohol sulfate; the a-alkene sulfonate; sodium alkyl sulfate; naphthalene sulfonic acid-formaldehyde condensation product; the styryl phenol polyethenoxy ether; alkylaryl polyoxyethylene polypropylene ether; fatty acid amide N methyl taurine sodium salt; alkylphenol polyoxyethylene; fatty alcohol-polyoxyethylene ether; alkyl sulfonic acid salt anionic surfactant or phosphate type anion surfactant etc., the moistening neopelex that is of excellent usefulness; lauryl sodium sulfate; to the basic sodium sulfonate of methoxyl group fatty acid amide or sodium butylnaphthalenesulfonate.
Wherein binding agent can be selected the binding agent of common moisture shot agent, such as xanthans, gum Arabic, cellulose base compound or starch compound etc.Preferred binding agent is sodium carboxymethylcellulose, xanthans, polyvinyl alcohol, polyethylene glycol, Ac-Di-Sol or gum Arabic.
Wherein filler can be selected the filler of common moisture shot agent, such as bentonite, white carbon, carclazyte, kaolin, mineral salt etc., and preferred filler precipitated calcium carbonate, sodium sulphate or urea etc.
The inventive method has enlarged that the employing extruder grain is made the pesticide water dispersible granule kind, dust pollution when having reduced production and processing, saved the energy.
Embodiment
Embodiment 1:
With Diacloden 6.26 gram, neopelex 0.1 gram, naphthalene sulfonic acid-formaldehyde condensation product 0.3 gram, precipitated calcium carbonate 3.34 grams, after they are mixed, after airslide disintegrating mill is pulverized fineness is 800-1000 purpose wetting powder; Then Diacloden 15.66 grams, silicone defoaming agent 1 gram, Macrogol 6000 one gram, neopelex 0.25 gram, naphthalene sulfonic acid-formaldehyde condensation product 1 gram, water 31.09 grams were ground 2.5 hours in sand mill, can obtain the aqueous suspension agent of 1-3um.At last the above-mentioned aqueous suspension agent of 3 grams, the above-mentioned wetting powder of 4.3 grams, 0.4 gram ammonium chloride are added in the kneader and mediate; make plastic material; at last this material is sent into the rotary extrusion comminutor; carry out granulation; by drying; screening obtains 60.13% Diacloden water dispersible granules finished product, suspensibility 94.13%, and dispersive property is excellent.
Embodiment 2
With Imidacloprid 6.25 gram, sodium alkyl benzene sulfonate 0.2 gram, naphthalene sulfonic acid-formaldehyde condensation product 0.5 gram, precipitated calcium carbonate 3.05 grams, after they are mixed, after airslide disintegrating mill is pulverized fineness is 800-1000 purpose wetting powder; Then Imidacloprid 15.62 grams, silicone defoaming agent 1 gram, Macrogol 6000 one gram, sodium alkyl benzene sulfonate 0.8 gram, naphthalene sulfonic acid-formaldehyde condensation product 2 grams, water 29.58 grams were ground 2.5 hours in sand mill, can obtain the aqueous suspension agent of 1-3um.At last the above-mentioned aqueous suspension agent of 3 grams, the above-mentioned wetting powder of 4.3 grams, 0.4 gram ammonium chloride are added in the kneader and mediate; make plastic material; at last this material is sent into the rotary extrusion comminutor; carry out granulation; by drying; screening obtains 58.73% imidacloprid water dispersible granule finished product, suspensibility 92.33%, and dispersive property is excellent.

Claims (3)

1. the prilling process of a novel agrochemical water dispersible granules is characterized in that a certain proportion of pesticide original medicine, auxiliary agent, filler etc. are made ultra-fine wetting powder; Simultaneously remaining pesticide original medicine, auxiliary agent, water, binding agent etc. are ground through sand mill and make aqueous suspension agent.Then wetting powder, aqueous suspension agent, disintegrant are added in the kneader simultaneously according to certain ratio and mediate, make plastic material, at last this material is sent into Squeezinggranulator, carry out granulation, by drying, screening obtains the water dispersible granules product.
2. the prilling process of pesticide water dispersible granules according to claim 1 is characterized in that water, binding agent, auxiliary agent directly grind to obtain particle diameter 1~5um aqueous suspension agent that the ratio of its consumption and wetting powder weight is 1: 0.5~1.35 in sand mill.
According to claim 1 with the prilling process of 2 described pesticide water dispersible granules, it is characterized in that described binding agent is Macrogol 2000-6000, xanthans, polyvinyl alcohol, gum Arabic, sodium carboxymethylcellulose, Magnesiumaluminumsilicate, Sodium Polyacrylate.
CN 201110268519 2011-09-08 2011-09-08 Granulation method of novel pesticide water dispersible granules Pending CN102986659A (en)

Priority Applications (1)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105248445A (en) * 2015-11-16 2016-01-20 河北德瑞化工有限公司 Slow-release thiamethoxam water dispersible granule and preparing method thereof
CN107006461A (en) * 2017-05-19 2017-08-04 发事达(南通)化工有限公司 A kind of preparation method of pesticide water dispersible granules
CN115316396A (en) * 2022-09-19 2022-11-11 镇江先锋植保科技有限公司 Preparation process and application method of cloransulam-methyl and sulfentrazone composition

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105248445A (en) * 2015-11-16 2016-01-20 河北德瑞化工有限公司 Slow-release thiamethoxam water dispersible granule and preparing method thereof
CN107006461A (en) * 2017-05-19 2017-08-04 发事达(南通)化工有限公司 A kind of preparation method of pesticide water dispersible granules
CN115316396A (en) * 2022-09-19 2022-11-11 镇江先锋植保科技有限公司 Preparation process and application method of cloransulam-methyl and sulfentrazone composition

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Application publication date: 20130327