WO2018205966A1 - Pyraclostrobin aqueous dispersion solid composition and preparation method therefor - Google Patents

Pyraclostrobin aqueous dispersion solid composition and preparation method therefor Download PDF

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Publication number
WO2018205966A1
WO2018205966A1 PCT/CN2018/086270 CN2018086270W WO2018205966A1 WO 2018205966 A1 WO2018205966 A1 WO 2018205966A1 CN 2018086270 W CN2018086270 W CN 2018086270W WO 2018205966 A1 WO2018205966 A1 WO 2018205966A1
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Prior art keywords
pyraclostrobin
mixture
aqueous dispersion
solid composition
pulverization
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PCT/CN2018/086270
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French (fr)
Chinese (zh)
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吴一凡
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江苏龙灯化学有限公司
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Publication of WO2018205966A1 publication Critical patent/WO2018205966A1/en

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    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N47/00Biocides, pest repellants or attractants, or plant growth regulators containing organic compounds containing a carbon atom not being member of a ring and having no bond to a carbon or hydrogen atom, e.g. derivatives of carbonic acid
    • A01N47/08Biocides, pest repellants or attractants, or plant growth regulators containing organic compounds containing a carbon atom not being member of a ring and having no bond to a carbon or hydrogen atom, e.g. derivatives of carbonic acid the carbon atom having one or more single bonds to nitrogen atoms
    • A01N47/10Carbamic acid derivatives, i.e. containing the group —O—CO—N<; Thio analogues thereof
    • A01N47/24Carbamic acid derivatives, i.e. containing the group —O—CO—N<; Thio analogues thereof containing the groups, or; Thio analogues thereof
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N25/00Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests
    • A01N25/08Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests containing solids as carriers or diluents
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N25/00Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests
    • A01N25/12Powders or granules
    • A01N25/14Powders or granules wettable
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N25/00Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests
    • A01N25/22Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests containing ingredients stabilising the active ingredients
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N37/00Biocides, pest repellants or attractants, or plant growth regulators containing organic compounds containing a carbon atom having three bonds to hetero atoms with at the most two bonds to halogen, e.g. carboxylic acids
    • A01N37/34Nitriles
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N43/00Biocides, pest repellants or attractants, or plant growth regulators containing heterocyclic compounds
    • A01N43/34Biocides, pest repellants or attractants, or plant growth regulators containing heterocyclic compounds having rings with one nitrogen atom as the only ring hetero atom
    • A01N43/40Biocides, pest repellants or attractants, or plant growth regulators containing heterocyclic compounds having rings with one nitrogen atom as the only ring hetero atom six-membered rings

Definitions

  • the invention relates to the field of agricultural chemistry, in particular to a water-dispersible solid composition and a preparation method thereof, in particular to a pyraclostrobin aqueous dispersion solid composition and a preparation method thereof.
  • Pyraclostrobin is a methoxy acrylate fungicide developed by BASF in Germany in 1993 and is a mitochondrial respiratory inhibitor. It inhibits mitochondrial respiration by preventing electron transfer between cytochrome b and c1, preventing mitochondria from producing and providing the energy (ATP) required for normal cell metabolism, ultimately leading to cell death.
  • pyraclostrobin N-[2-[[1-(4-chlorophenyl)pyrazol-3-yl]oxymethyl]phenyl]-N-methoxycarbamic acid
  • Methyl ester belongs to the broad spectrum fungicide of methoxy acrylate.
  • Pyraclostrobin can be used in wheat, peanut, rice, vegetables, fruit trees, tobacco, tea trees, ornamental plants, lawns and other crops to control leaf blight caused by ascomycetes, basidiomycetes, deuteromycetes and oomycetes. , rust, powdery mildew, downy mildew, blight, anthracnose, scab, brown spot, blight and other diseases.
  • the particle size of the solid preparation such as wettable powder (WP) and water-dispersible granule (WDG) has a great influence on the stability and suspension ratio of the preparation.
  • WP wettable powder
  • WDG water-dispersible granule
  • various types of pulverization are necessary.
  • the active compound has a low melting point, especially when the melting point does not exceed 70 ° C, direct pulverization is difficult because the active material is easily melted or softened during the pulverization process, which eventually leads to risk of physical and chemical quality of the product, and heat storage stability. Problems such as unsatisfactory sex and suspension rate.
  • the pyridoxal ester has a low melting point of only 56 to 64 ° C, so that the prepared pyraclostrobin composition has a problem of easy agglomeration after heat storage.
  • the filter and the nozzle may be clogged due to the agglomeration and agglomeration, which may cause inconvenience to the user and affect the absorption of the pyraclostrobin active substance by the plant. , reducing the efficacy.
  • CN102469775A discloses a process for preparing an aqueous suspension of pyraclostrobin by dispersing a large amount of pyraclostrobin in an aqueous phase in the form of amorphous droplets, and then adding a small amount of pyraclostrobin monocrystal A suspension of the type of particles induces the rapid crystallization of the pyridoxine amorphous droplets to form a final aqueous dispersion of the granules.
  • This process requires the melting of pyraclostrobin and is carried out at a temperature above the melting point of the pyraclostrobin active over the heated aqueous phase.
  • the inventors have unexpectedly discovered that a combination of pyraclostrobin, an alkyl sulfonate, a porous carrier, and a functional auxiliary can provide water of pyraclostrobin having improved heat storage stability and avoiding agglomeration and agglomeration.
  • the solid composition is dispersed.
  • the present invention provides a pyraclostrobin aqueous dispersion solid composition
  • a pyraclostrobin aqueous dispersion solid composition comprising, by weight percentage, the following components: pyraclostrobin 5-50%, alkyl sulfonate 0.1-15%,
  • the porous carrier is 5 to 80%, and the functional auxiliary is 1 to 45%.
  • the pyraclostrobin comprises 5 to 50% by weight of the composition, for example, 5%, 8%, 10%, 12%, 15%, 20%, 22%, 25%, 28%. , 30%, 32%, 35%, 40%, 42%, 45% or 50%.
  • the alkyl sulfonate accounts for 0.1 to 15% by weight of the composition, for example, 0.1%, 0.5%, 1%, 2%, 3%, 3.5%, 4%, 5.2%, 6%. , 7%, 8.5%, 9%, 10%, 11%, 12%, 13%, 14% or 15%.
  • the porous carrier accounts for 5 to 80% by weight of the composition, for example, 5%, 8%, 10%, 12%, 13%, 15%, 18%, 20%, 22%, 25 %, 30%, 35%, 40%, 48%, 52%, 60%, 65%, 72%, 79% or 80%.
  • the functional auxiliary agent accounts for 1 to 45% by weight of the composition, for example, 1%, 2%, 3%, 5%, 8%, 10%, 15%, 20%, 22%, 25%, 30%, 35%, 40%, 42%, 43% or 45%.
  • the invention selects the content of pyraclostrobin, the alkali sulfonate, the porous carrier and the functional auxiliary, and the prepared pyraclostrobin aqueous dispersion solid composition has heat storage and normal storage stability. Good sex, no aggregation, no caking, no clogging sprayer filter or spray head phenomenon.
  • the pyraclostrobin aqueous dispersion solid composition may contain other active ingredients, such as tebuconazole, dinotefuran or fluoxazole, in addition to the active ingredient of pyraclostrobin. One or more of them are contained, and the present invention is not particularly limited.
  • the pyraclostrobin aqueous dispersion solid composition consists of the following components by weight:
  • the alkyl sulfonate is selected from the group consisting of alkylnaphthalene sulfonates, alkylnaphthalene sulfonate formaldehyde polycondensates, alkylbenzene sulfonates, alkyl ethyl sulfonates or secondary alkyl sulfonates.
  • the porous carrier is selected from the group consisting of kaolin, montmorillonite, attapulgite, synthetic silicon, plant fiber, mineral fiber or magnesium aluminum silicate, or a mixture of at least two thereof, of which typical but not The limiting mixture is: a mixture of kaolin and montmorillonite clay, a mixture of montmorillonite and attapulgite, a mixture of synthetic silicon and kaolin, a mixture of plant fibers, mineral fibers and synthetic silicon, magnesium aluminum silicate and montmorillonite. a mixture of clays.
  • the kaolin is selected from any one or a mixture of at least two of kaolinite, dickite, pearlite, silica-rich kaolinite, halloysite or multi-water halloysite, of which typical But a non-limiting mixture is: a mixture of kaolinite and dickite, a mixture of pearlite and silicon-rich kaolinite, a mixture of watery halloysite and pearlite; the montmorillonite is selected from the group consisting of beidellite and lithium.
  • any one or a mixture of at least two of smectite, saponite or bentonite wherein a typical but non-limiting mixture is: a mixture of beidellite and hectorite, a mixture of saponite and bentonite, a mixture of hectorite and saponite; the attapulgite is selected from the group consisting of bleaching earth and/or sepiolite; and the synthetic silicon is selected from the group consisting of white carbon black and/or fumed silica.
  • the functional auxiliary agent is selected from the group consisting of a dispersing agent, a wetting agent, an antifoaming agent or an inert carrier, or a mixture of at least two, that is, the pyraclostrobin aqueous dispersion solid composition, Any one of the functional auxiliaries may be contained, or a mixture of two or more kinds may be used.
  • the dispersing agent is selected from any one or a mixture of at least two of lignosulfonate, polycarboxylate, fatty alcohol polyoxyethylene ether or ethylene oxide propylene oxide block copolymer, Typical but non-limiting mixtures thereof are: a mixture of lignosulfonates and polycarboxylates, a mixture of polycarboxylates and fatty alcohol polyoxyethylene ethers, ethylene oxide propylene oxide block copolymers and wood a mixture of sulfonate salts.
  • the wetting agent is selected from any one or a mixture of at least two of nonylphenol ethoxylates, K12 or polyoxyethylene fatty alcohol ethers, wherein a typical but non-limiting mixture is nonylphenol a mixture of polyoxyethylene ether and K12, a mixture of K12 and polyoxyethylene fatty alcohol ether.
  • the antifoaming agent is selected from the group consisting of silicone antifoaming agents.
  • silicone antifoaming agent type those skilled in the art can make conventional selection according to actual needs, and the invention is not particularly limited.
  • the inert carrier is selected from any one or a mixture of at least two of corn starch, talc, sucrose, potassium sulfate, kaolin or diatomaceous earth, wherein a typical but non-limiting mixture is: corn starch and a mixture of talc, a mixture of sucrose and potassium sulfate, a mixture of kaolin and corn starch.
  • the pyraclostrobin aqueous dispersion solid composition of the present invention is formulated as a wettable powder or a water-dispersible granule.
  • the present invention provides a method for preparing the pyraclostrobin aqueous dispersion solid composition, comprising the steps of:
  • a porous carrier and a functional auxiliary agent are added to the obtained homogeneous mixture, and finely pulverized to obtain the pyrazolidin ester aqueous dispersion solid composition.
  • the present invention firstly mixes pyraclostrobin and an alkyl sulfonate in step (1) without using all components or together with a dispersing agent and an antifoaming agent and a carrier. Carry out a mixed form.
  • the invention firstly mixes the pyraclostrobin and the alkyl sulfonate in the step (1), and the first coarse pulverization makes the pyraclostrobin and the alkyl sulfonate more fully mixed, the alkyl sulfonic acid.
  • the salt adheres more effectively to the surface of the pyraclostrobin particles, effectively preventing contact aggregation between the particles and the particles during storage.
  • the inventors have also unexpectedly discovered that when only pyraclostrobin and the alkyl sulfonate are first mixed, by using coarse pulverization at 35 ° C or lower, the pyraclostrobin can be rendered as a paste having Softening, which further contributes to the problem of agglomeration and agglomeration in the back water-dispersible solid particulate product.
  • the present invention employs pulverization at a low temperature, which is specifically carried out at a low temperature of 35 ° C or lower, for example, a temperature of 0 ° C, 4 °C, 8 ° C, 10 ° C, 12 ° C, 15 ° C, 20 ° C, 22 ° C, 25 ° C, 28 ° C, 30 ° C or 35 ° C, of course, can also be carried out below 0 degrees.
  • the melting point of pyraclostrobin is 56-64 ° C. If it is directly pulverized under normal conditions, the original drug will soften and affect the pulverization efficiency. However, the pulverization at the low temperature of the present invention can effectively solve the problem of particle collision and softening of the pyraclostrobin original drug during the pulverization process, and at the same time, the alkyl sulfonate is sufficiently uniform and closely adhered to the surface of the pyraclostrobin particle. The effect of subsequent secondary jet pulverization on pyraclostrobin particles was solved.
  • the invention adopts a homogeneous mixture obtained after coarse pulverization, and further adds a porous carrier and a functional auxiliary agent, such an operation can make the pulverization temperature relatively loose, and can be carried out at a relatively high temperature, at this time, the function
  • the auxiliaries can play a certain protective role, and further play a role in promoting the agglomeration and agglomeration of the finally formed pyraclostrobin aqueous dispersion solid composition.
  • the operation mode of coarse pulverization combined with fine pulverization at a low temperature is adopted, and by mixing the pulverization into two steps of coarse pulverization and fine pulverization, the mixture of the alkyl sulfonate and the pyraclostrobin is more fully and more. Effective adhesion to the surface of the pyraclostrobin particles further effectively prevents contact agglomeration between the particles and the particles during storage.
  • the wettable powder when preparing a wettable powder, can be directly obtained after the fine pulverization in the above preparation method in the step (3); and when the water-dispersible granule is prepared
  • the granulation drying step is also required to obtain the water-dispersible granule.
  • the granulation and drying technology those skilled in the art should understand that it can adopt various operation modes such as extrusion granulation, spray granulation, rotary granulation, fluidized bed granulation, etc., and the present invention does not specifically limit it. .
  • the coarse pulverization in the step (2) is carried out by airflow pulverization, and the specific operation is as follows: the mixture is passed through the high-speed airflow at a certain speed, so that a strong collision between the particles and the particles, the particles and the inner wall is achieved, and the damage is achieved. It finally makes the particle size after pulverization D90 ⁇ 20 ⁇ m.
  • the invention adopts jet milling to realize uniform mixing of pyraclostrobin and alkylsulfonate, and improves mixing uniformity and heat dissipation effect.
  • the fine pulverization in the step (3) is carried out by secondary gas flow pulverization, which can adjust the pulverization pressure and the feed rate so that the pulverized particle diameter reaches 1 to 15 ⁇ m.
  • pulverization pressure and feed rate used in the secondary air flow pulverization those skilled in the art can also adjust according to the actual pulverized particle size to be achieved.
  • the pyraclostrobin aqueous dispersion solid composition of the present invention may be a wettable powder or a water-dispersible granule.
  • the pyraclostrobin aqueous dispersion solid composition has the advantages of good heat storage and normal storage stability, no aggregation, no agglomeration, no clogging of the filter or the spray head, thereby facilitating storage and user use, and improving pyrazole.
  • the efficacy of ether oxystrobin is a wettable powder or a water-dispersible granule.
  • the present invention has at least the following beneficial effects:
  • the pyraclostrobin aqueous dispersion solid composition of the invention has the advantages of good heat storage and normal storage stability, no aggregation, no agglomeration, no clogging of a filter or a spray head, and good fluidity;
  • Example 1 20% pyraclostrobin wettable powder
  • Soap L sodium tallowate
  • Preparation process the pyraclostrobin original drug and Morwet D425 (alkylnaphthalenesulfonate formaldehyde polycondensate) are mixed in a weight ratio, and after stirring uniformly, the first coarse pulverization is carried out at a temperature of 30 ° C to obtain homogeneity. Mixture; then gas phase white carbon, Soap L (sodium tallow) and corn starch are added to the above coarsely pulverized mixture in a weight ratio, and subjected to a second fine pulverization until the particle diameter D90 ⁇ 10 ⁇ m, that is, the final product.
  • Morwet D425 alkylnaphthalenesulfonate formaldehyde polycondensate
  • Example 2 50% pyraclostrobin water dispersible granules
  • Soap L sodium tallowate
  • the preparation process mixing the pyraclostrobin original drug with Morwet EFW (alkylnaphthalene sulfonate) in a weight ratio, stirring uniformly, and performing the first coarse pulverization at a temperature of 25 ° C to obtain a homogeneous mixture;
  • White carbon black, EO/PO block copolymer, Soap L (sodium tallowate) and diatomaceous earth were added to the above coarsely pulverized mixture in a weight ratio, and subjected to a second fine pulverization to obtain a particle diameter of D90 ⁇ 10 ⁇ m.
  • the mother powder which is kneaded by adding an appropriate amount of water, is dried by extrusion granulation to obtain a final product.
  • Example 3 10% pyraclostrobin wettable powder
  • Soap L sodium tallowate
  • the preparation process mixing the pyraclostrobin original drug with sodium dodecylsulfonate in a weight ratio, stirring uniformly, and performing the first coarse pulverization at a temperature of 22 ° C to obtain a homogeneous mixture; then calcining the kaolin , nonylphenol polyoxyethylene ether phosphate, Soap L (sodium tallow) and potassium sulfate are added to the above coarsely pulverized mixture in a weight ratio, and subjected to a second fine pulverization until the particle diameter D90 ⁇ 10 ⁇ m, which is the final product.
  • Example 4 5% pyraclostrobin + 10% boscalyl wettable powder
  • Soap L sodium tallowate
  • the preparation process mixing the pyraclostrobin original drug with the alkyl ethyl sulfonate in a weight ratio, stirring uniformly, and performing the first coarse pulverization at a temperature of 35 ° C to obtain a homogeneous mixture; then, the acyl bacterium Amine, plant fiber, fatty alcohol polyoxyethylene ether, Soap L (sodium tallow) and talc are added to the above coarsely pulverized mixture in a weight ratio, and subjected to a second fine pulverization until the particle diameter D90 ⁇ 10 ⁇ m. Final product.
  • Example 5 5% pyraclostrobin + 40% chlorothalonil water-dispersible granules
  • Soap L sodium tallowate
  • the preparation process comprises: mixing the pyraclostrobin original drug with the alkylnaphthalenesulfonate formaldehyde polycondensate in a weight ratio, stirring uniformly, and performing the first coarse pulverization at a temperature of 10 ° C to obtain a homogeneous mixture; Chlorothalonil, mineral fiber, polycarboxylate, sodium succinate sulfonate, Soap L (sodium tallowate) and kaolin are added to the above coarsely pulverized mixture in a weight ratio, and subjected to a second fine pulverization to obtain a particle size D90. ⁇ 10 ⁇ m of the mother powder, which is kneaded by adding an appropriate amount of water, and then dried by extrusion granulation to obtain a final product.
  • Preparation process the above composition is subjected to jet milling to make the particle size D90 ⁇ 10 ⁇ m, that is, the final product
  • Preparation process The above composition is subjected to jet milling to obtain a mother powder having a particle diameter of D90 ⁇ 10 ⁇ m.
  • the mother powder is kneaded by adding an appropriate amount of water, and then dried by extrusion granulation to obtain a final product.
  • Preparation process the above composition is subjected to jet milling to make the particle size D90 ⁇ 10 ⁇ m, that is, the final product
  • Formulation process The above composition is subjected to jet milling so that the particle diameter D90 ⁇ 10 ⁇ m, that is, the final product.
  • Preparation process The above composition is subjected to jet milling to obtain a mother powder having a particle diameter of D90 ⁇ 10 ⁇ m.
  • the mother powder is kneaded by adding an appropriate amount of water, and then dried by extrusion granulation to obtain a final product.
  • Formulation process The above composition is subjected to jet milling so that the particle diameter D90 ⁇ 10 ⁇ m, that is, the final product.
  • Preparation process The above composition is subjected to jet milling to obtain a mother powder having a particle diameter of D90 ⁇ 10 ⁇ m.
  • the mother powder is kneaded by adding an appropriate amount of water, and then dried by extrusion granulation to obtain a final product.
  • the preparation process the pyraclostrobin and the polycarboxylate sodium salt are mixed in a weight ratio, and after being uniformly stirred, the first coarse pulverization is carried out at a temperature of 30 ° C, and then the gas phase white carbon black, Soap L (sodium borate) And the corn starch is added to the above coarse powder mixture in a weight ratio, and the second fine pulverization is carried out until the particle diameter D90 ⁇ 10 ⁇ m, that is, the final product is obtained.
  • the preparation process comprises: mixing pyraclostrobin and sodium dodecylsulfonate in a weight ratio, stirring uniformly, performing the first coarse pulverization at a temperature of 30 ° C, and then adding nonylphenol ethoxylate phosphate, Soap L (sodium tallowate) and potassium sulfate are added to the above coarse powder mixture in a weight ratio, and subjected to a second fine pulverization until the particle diameter D90 ⁇ 10 ⁇ m, that is, the final product is obtained.
  • the preparation process the pyraclostrobin and Morwet EFW (alkylnaphthalene sulfonate) are mixed in a weight ratio, and after being uniformly stirred, the first coarse pulverization is carried out at a temperature of 30 ° C, and then the EO/PO block copolymer is used. Soap L (sodium tallow) and sodium sulfate are added to the above coarse powder mixture in a weight ratio, and subjected to a second fine pulverization to obtain a mother powder having a particle diameter of D90 ⁇ 10 ⁇ m, and the mother powder is kneaded by adding an appropriate amount of water. The final product is obtained by extrusion granulation and drying.
  • Morwet EFW alkylnaphthalene sulfonate
  • the heat storage stability test was carried out in an oven at 54 °C. After heat storage in an oven at 54 ° C, the samples were removed from the oven. After cooling to room temperature, each test sample was poured out to observe the fluidity of the sample. The wettable powder sample was then passed directly through a 325 mesh screen; the water dispersed granule sample was diluted with water and passed through a 325 mesh screen.
  • the test results in Table 1 show that the pyraclostrobin aqueous dispersion solid composition prepared according to the present invention has good fluidity at room temperature, uniform sample, no agglomeration, no sticking phenomenon, especially with the comparative phase. Compared with a higher suspension rate, it basically reaches a suspension rate of more than 85%, which is far from being comparable.
  • the pyraclostrobin aqueous dispersion solid composition of the present invention has more outstanding heat storage stability performance, good fluidity, no agglomeration, no clogging screen, and therefore has more It is convenient for users to use and improve the outstanding advantages of pyraclostrobin.

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  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Dentistry (AREA)
  • Plant Pathology (AREA)
  • Engineering & Computer Science (AREA)
  • Pest Control & Pesticides (AREA)
  • Agronomy & Crop Science (AREA)
  • Wood Science & Technology (AREA)
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  • Environmental Sciences (AREA)
  • Toxicology (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

Provided in the present invention is a pyraclostrobin aqueous dispersion solid composition, which comprises the following components by weight percentage: pyraclostrobin 5-50%, alkyl sulfonate 0.1-15%, a porous carrier 5-80% and a functional additive 1-45%. Further provided in the present invention is a preparation method for the composition, which comprises: first mixing pyraclostrobin and alkyl naphthalene sulfonate according to a ratio; coarsely crushing the obtained mixture at 35°C or lower to obtain a homogeneous mixture; adding a porous carrier and a functional additive into the obtained homogeneous mixture; finely crushing so as to obtain the pyraclostrobin aqueous dispersion solid composition. The pyraclostrobin aqueous dispersion solid composition prepared in the present invention has good stability in storage at high and normal temperatures, does not collect, does not agglomerate, and will not clog a sprayer filter or spray head, thus making said composition easier for a user to use and increasing the efficiency thereof as a pesticide.

Description

一种吡唑醚菌酯水分散固体组合物及其制备方法Pyraclostrobin aqueous dispersion solid composition and preparation method thereof
本申请要求于2017年5月10日提交中国专利局,申请号为201710324705.2,发明名称为“一种吡唑醚菌酯水分散固体组合物及其制备方法”的中国专利申请的优先权,其全部内容通过引用结合在本申请中。This application claims priority to Chinese Patent Application No. 201710324705.2, entitled "A pyraclostrobin aqueous dispersion solid composition and its preparation method", which is filed on May 10, 2017. The entire contents are incorporated herein by reference.
技术领域Technical field
本发明涉及农业化学领域,具体涉及一种水分散固体组合物及其制备方法,尤其涉及一种吡唑醚菌酯水分散固体组合物及其制备方法。The invention relates to the field of agricultural chemistry, in particular to a water-dispersible solid composition and a preparation method thereof, in particular to a pyraclostrobin aqueous dispersion solid composition and a preparation method thereof.
背景技术Background technique
吡唑醚菌酯是由德国巴斯夫公司于1993年开发的兼具吡唑结构的甲氧基丙烯酸酯类杀菌剂,是一种线粒体呼吸抑制剂。它通过阻止细胞色素b和c1间电子传递而抑制线粒体呼吸作用,使线粒体不能产生和提供细胞正常代谢所需要的能量(ATP),最终导致细胞死亡。Pyraclostrobin is a methoxy acrylate fungicide developed by BASF in Germany in 1993 and is a mitochondrial respiratory inhibitor. It inhibits mitochondrial respiration by preventing electron transfer between cytochrome b and c1, preventing mitochondria from producing and providing the energy (ATP) required for normal cell metabolism, ultimately leading to cell death.
吡唑醚菌酯(pyraclostrobin)化学名称为:N-[2-[[1-(4-氯苯基)吡唑-3-基]氧甲基]苯基]-N-甲氧基氨基甲酸甲酯,属于甲氧基丙烯酸酯类广谱杀菌剂。吡唑醚菌酯可用于小麦、花生、水稻、蔬菜、果树、烟草、茶树、观赏植物、草坪等各种作物,防治子囊菌、担子菌、半知菌和卵菌纲真菌引起的叶枯病、锈病、白粉病、霜霉病、疫病、炭疽病、疮痂病、褐斑病、立枯病等多种病害。目前市面上主要以吡唑醚菌酯乳油、水乳剂产品来使用。然而这些剂型都具有一个共同的缺点,即乳油制剂中含有大量的有机溶剂,其对生态环境和水生生物危害极大。随着人们对环境保护的意识逐步加强,这类产品必将逐步淘汰。现在各个农化公司都在朝着环保型剂型水剂化、颗粒化产品加大研发力度,逐步开发吡唑醚菌酯的悬浮剂、种衣剂、颗粒剂等剂型,以减少使用有机溶剂对环境的危害。The chemical name of pyraclostrobin is: N-[2-[[1-(4-chlorophenyl)pyrazol-3-yl]oxymethyl]phenyl]-N-methoxycarbamic acid Methyl ester belongs to the broad spectrum fungicide of methoxy acrylate. Pyraclostrobin can be used in wheat, peanut, rice, vegetables, fruit trees, tobacco, tea trees, ornamental plants, lawns and other crops to control leaf blight caused by ascomycetes, basidiomycetes, deuteromycetes and oomycetes. , rust, powdery mildew, downy mildew, blight, anthracnose, scab, brown spot, blight and other diseases. At present, the market mainly uses pyraclostrobin emulsion and water emulsion products. However, these dosage forms all have a common disadvantage that the emulsifiable concentrate contains a large amount of organic solvents, which are extremely harmful to the ecological environment and aquatic organisms. As people's awareness of environmental protection gradually strengthens, such products will be phased out. Nowadays, various agrochemical companies are stepping up research and development efforts towards environmentally-friendly dosage forms of water-based and granulated products, and gradually developing dosage forms such as suspensions, seed coatings and granules of pyraclostrobin to reduce the use of organic solvents. Environmental hazards.
但是水分散剂型中,固体制剂例如可湿性粉剂(WP)、水分散颗粒剂(WDG)的粒径对制剂的稳定性和悬浮率有很大的影响。为了得到粒径在1~15μm的固体制剂,各种方式的粉碎是必须的。但由于活性物熔点低,尤其 是熔点不超过70℃时,直接粉碎是比较困难的,因为在粉碎过程中,活性物很容易被熔化或软化,最终会导致产品理化质量存在风险,热贮稳定性和悬浮率不合格等问题。However, in the aqueous dispersion type, the particle size of the solid preparation such as wettable powder (WP) and water-dispersible granule (WDG) has a great influence on the stability and suspension ratio of the preparation. In order to obtain a solid preparation having a particle diameter of 1 to 15 μm, various types of pulverization are necessary. However, since the active compound has a low melting point, especially when the melting point does not exceed 70 ° C, direct pulverization is difficult because the active material is easily melted or softened during the pulverization process, which eventually leads to risk of physical and chemical quality of the product, and heat storage stability. Problems such as unsatisfactory sex and suspension rate.
吡唑醚菌酯的熔点较低,仅为56~64℃,因而制备成的吡唑醚菌酯组合物存在热贮后容易团聚结块的问题。对于长期贮存后的制剂,在农药喷雾使用时,也会因为团聚结块的问题导致堵塞过滤器和喷头,从而给用户使用带来不便,且影响了植物对吡唑醚菌酯活性物的吸收,降低了药效。这些技术困难,使得吡唑醚菌酯水分散制剂没有得到广泛使用。The pyridoxal ester has a low melting point of only 56 to 64 ° C, so that the prepared pyraclostrobin composition has a problem of easy agglomeration after heat storage. For the long-term storage of the preparation, when the pesticide spray is used, the filter and the nozzle may be clogged due to the agglomeration and agglomeration, which may cause inconvenience to the user and affect the absorption of the pyraclostrobin active substance by the plant. , reducing the efficacy. These technical difficulties make the pyraclostrobin aqueous dispersion preparation not widely used.
CN102469775A公开了一种制备吡唑醚菌酯的含水悬浮液的方法,该方法通过大量的吡唑醚菌酯以无定型液滴形式分散在水相中,然后加入少量吡唑醚菌酯单一晶型颗粒的悬浮液,诱导吡唑醚菌酯无定型液滴快速结晶形成最终的颗粒水分散悬浮液。该方法需要熔融吡唑醚菌酯并且在加热水相超过吡唑醚菌酯活性物熔点以上的温度下进行。因此该方法实际生产加工能耗比较大,可操作性比较复杂,对设备要求也很高。因此如何提供一种热贮和常贮稳定性好,不易聚集和结块,且制备简便的组合物是目前迫切需要的。CN102469775A discloses a process for preparing an aqueous suspension of pyraclostrobin by dispersing a large amount of pyraclostrobin in an aqueous phase in the form of amorphous droplets, and then adding a small amount of pyraclostrobin monocrystal A suspension of the type of particles induces the rapid crystallization of the pyridoxine amorphous droplets to form a final aqueous dispersion of the granules. This process requires the melting of pyraclostrobin and is carried out at a temperature above the melting point of the pyraclostrobin active over the heated aqueous phase. Therefore, the actual production and processing energy consumption of the method is relatively large, the operability is relatively complicated, and the equipment requirements are also high. Therefore, how to provide a composition which has good heat storage and storage stability, is not easy to aggregate and agglomerate, and is easy to prepare is currently urgently needed.
发明内容Summary of the invention
发明人意外发现:采用吡唑醚菌酯、烷基磺酸盐、多孔性载体以及功能性助剂的组合,可以得到具有改进热贮稳定性,避免团聚结块的吡唑醚菌酯的水分散固体组合物。The inventors have unexpectedly discovered that a combination of pyraclostrobin, an alkyl sulfonate, a porous carrier, and a functional auxiliary can provide water of pyraclostrobin having improved heat storage stability and avoiding agglomeration and agglomeration. The solid composition is dispersed.
基于上述发现,本发明提供了以下技术方案:Based on the above findings, the present invention provides the following technical solutions:
第一方面,本发明提供了一种吡唑醚菌酯水分散固体组合物,其按重量百分比包括以下组分:吡唑醚菌酯5~50%,烷基磺酸盐0.1~15%,多孔性载体5~80%,功能性助剂1~45%。In a first aspect, the present invention provides a pyraclostrobin aqueous dispersion solid composition comprising, by weight percentage, the following components: pyraclostrobin 5-50%, alkyl sulfonate 0.1-15%, The porous carrier is 5 to 80%, and the functional auxiliary is 1 to 45%.
本发明中,所述吡唑醚菌酯占组合物的重量百分比为5~50%,例如5%、8%、10%、12%、15%、20%、22%、25%、28%、30%、32%、35%、40%、42%、45%或50%。In the present invention, the pyraclostrobin comprises 5 to 50% by weight of the composition, for example, 5%, 8%, 10%, 12%, 15%, 20%, 22%, 25%, 28%. , 30%, 32%, 35%, 40%, 42%, 45% or 50%.
本发明中,所述烷基磺酸盐占组合物的重量百分比为0.1~15%,例如0.1%、0.5%、1%、2%、3%、3.5%、4%、5.2%、6%、7%、8.5%、9%、10%、11%、 12%、13%、14%或15%。In the present invention, the alkyl sulfonate accounts for 0.1 to 15% by weight of the composition, for example, 0.1%, 0.5%, 1%, 2%, 3%, 3.5%, 4%, 5.2%, 6%. , 7%, 8.5%, 9%, 10%, 11%, 12%, 13%, 14% or 15%.
本发明中,所述多孔性载体占组合物的重量百分比为5~80%,例如5%、8%、10%、12%、13%、15%、18%、20%、22%、25%、30%、35%、40%、48%、52%、60%、65%、72%、79%或80%。In the present invention, the porous carrier accounts for 5 to 80% by weight of the composition, for example, 5%, 8%, 10%, 12%, 13%, 15%, 18%, 20%, 22%, 25 %, 30%, 35%, 40%, 48%, 52%, 60%, 65%, 72%, 79% or 80%.
本发明中,所述功能性助剂占组合物的重量百分比为1~45%,例如1%、2%、3%、5%、8%、10%、15%、20%、22%、25%、30%、35%、40%、42%、43%或45%。In the present invention, the functional auxiliary agent accounts for 1 to 45% by weight of the composition, for example, 1%, 2%, 3%, 5%, 8%, 10%, 15%, 20%, 22%, 25%, 30%, 35%, 40%, 42%, 43% or 45%.
本发明通过对吡唑醚菌酯、烷基磺酸盐、多孔性载体以及功能性助剂的含量进行选择,其配制得到的吡唑醚菌酯水分散固体组合物具有热贮和常贮稳定性好,不聚集、不结块,无堵塞喷雾器过滤器或喷雾头现象。The invention selects the content of pyraclostrobin, the alkali sulfonate, the porous carrier and the functional auxiliary, and the prepared pyraclostrobin aqueous dispersion solid composition has heat storage and normal storage stability. Good sex, no aggregation, no caking, no clogging sprayer filter or spray head phenomenon.
该吡唑醚菌酯水分散固体组合物中,除了含有吡唑醚菌酯这一活性成分外,还可以含有其它活性成分,例如戊唑醇、呋虫胺或氟唑环菌胺等,可以含有其中一种或多种,本发明不做特殊限定。The pyraclostrobin aqueous dispersion solid composition may contain other active ingredients, such as tebuconazole, dinotefuran or fluoxazole, in addition to the active ingredient of pyraclostrobin. One or more of them are contained, and the present invention is not particularly limited.
优选地,所述吡唑醚菌酯水分散固体组合物按重量百分比由如下组分组成:Preferably, the pyraclostrobin aqueous dispersion solid composition consists of the following components by weight:
吡唑醚菌酯6~30%,烷基磺酸盐2~5%,多孔性载体10~70%,余量为功能性助剂。Pyraclostrobin 6 to 30%, alkyl sulfonate 2 to 5%, porous carrier 10 to 70%, and the balance is a functional auxiliary.
优选地,所述烷基磺酸盐选自烷基萘磺酸盐、烷基萘磺酸盐甲醛缩聚物、烷基苯磺酸盐、烷基乙基磺酸盐或仲烷基磺酸盐中的任意一种或至少两种的混合物,其中典型但非限制性的混合物为:烷基萘磺酸盐和烷基萘磺酸盐甲醛缩聚物的混合物,烷基萘磺酸盐和烷基苯磺酸盐的混合物,烷基乙基磺酸盐和烷基萘磺酸盐甲醛缩聚物的混合物,仲烷基磺酸盐和烷基苯磺酸盐的混合物;优选烷基萘磺酸盐甲醛缩聚物。Preferably, the alkyl sulfonate is selected from the group consisting of alkylnaphthalene sulfonates, alkylnaphthalene sulfonate formaldehyde polycondensates, alkylbenzene sulfonates, alkyl ethyl sulfonates or secondary alkyl sulfonates. Any one or a mixture of at least two, wherein a typical but non-limiting mixture is: a mixture of an alkylnaphthalenesulfonate and an alkylnaphthalenesulfonate formaldehyde polycondensate, an alkylnaphthalenesulfonate and an alkyl group a mixture of besylate, a mixture of alkyl ethyl sulfonate and alkylnaphthalene sulfonate formaldehyde polycondensate, a mixture of a secondary alkyl sulfonate and an alkyl benzene sulfonate; preferably an alkylnaphthalene sulfonate Formaldehyde polycondensate.
优选地,所述多孔性载体选自高岭土、蒙脱粘土、绿坡缕石、合成硅、植物纤维、矿物纤维或硅酸镁铝中的任意一种或至少两种的混合物,其中典型但非限制性的混合物为:高岭土和蒙脱粘土的混合物,蒙脱粘土和绿坡缕石的混合物,合成硅和高岭土的混合物,植物纤维、矿物纤维和合成硅的混合物,硅酸镁铝和蒙脱粘土的混合物。Preferably, the porous carrier is selected from the group consisting of kaolin, montmorillonite, attapulgite, synthetic silicon, plant fiber, mineral fiber or magnesium aluminum silicate, or a mixture of at least two thereof, of which typical but not The limiting mixture is: a mixture of kaolin and montmorillonite clay, a mixture of montmorillonite and attapulgite, a mixture of synthetic silicon and kaolin, a mixture of plant fibers, mineral fibers and synthetic silicon, magnesium aluminum silicate and montmorillonite. a mixture of clays.
优选地,所述高岭土选自高岭石、迪开石、珍珠陶土、富硅高岭石、多 水高岭石或多水埃洛石中的任意一种或至少两种的混合物,其中典型但非限制性的混合物为:高岭石和迪开石的混合物,珍珠陶土和富硅高岭石的混合物,多水埃洛石和珍珠陶土的混合物;所述蒙脱粘土选自贝得石、锂蒙脱石、皂石或斑脱土中的任意一种或至少两种的混合物,其中典型但非限制性的混合物为:贝得石和锂蒙脱石的混合物,皂石和斑脱土的混合物,锂蒙脱石和皂石的混合物;所述绿坡缕石选自漂白土和/或海泡石;所述合成硅选自白炭黑和/或气相白炭黑。Preferably, the kaolin is selected from any one or a mixture of at least two of kaolinite, dickite, pearlite, silica-rich kaolinite, halloysite or multi-water halloysite, of which typical But a non-limiting mixture is: a mixture of kaolinite and dickite, a mixture of pearlite and silicon-rich kaolinite, a mixture of watery halloysite and pearlite; the montmorillonite is selected from the group consisting of beidellite and lithium. Any one or a mixture of at least two of smectite, saponite or bentonite, wherein a typical but non-limiting mixture is: a mixture of beidellite and hectorite, a mixture of saponite and bentonite, a mixture of hectorite and saponite; the attapulgite is selected from the group consisting of bleaching earth and/or sepiolite; and the synthetic silicon is selected from the group consisting of white carbon black and/or fumed silica.
优选地,所述功能性助剂选自分散剂、润湿剂、消泡剂或惰性载体中的任意一种或至少两种的混合物,即所述吡唑醚菌酯水分散固体组合物中,可以含有其中任意一种功能性助剂,也可以采用两种或多种的混合形式。Preferably, the functional auxiliary agent is selected from the group consisting of a dispersing agent, a wetting agent, an antifoaming agent or an inert carrier, or a mixture of at least two, that is, the pyraclostrobin aqueous dispersion solid composition, Any one of the functional auxiliaries may be contained, or a mixture of two or more kinds may be used.
优选地,所述分散剂选自木质素磺酸盐、聚羧酸盐、脂肪醇聚氧乙烯醚或环氧乙烷环氧丙烷嵌段共聚物中的任意一种或至少两种的混合物,其中典型但非限制性的混合物为:木质素磺酸盐和聚羧酸盐的混合物,聚羧酸盐和脂肪醇聚氧乙烯醚的混合物,环氧乙烷环氧丙烷嵌段共聚物和木质素磺酸盐的混合物。Preferably, the dispersing agent is selected from any one or a mixture of at least two of lignosulfonate, polycarboxylate, fatty alcohol polyoxyethylene ether or ethylene oxide propylene oxide block copolymer, Typical but non-limiting mixtures thereof are: a mixture of lignosulfonates and polycarboxylates, a mixture of polycarboxylates and fatty alcohol polyoxyethylene ethers, ethylene oxide propylene oxide block copolymers and wood a mixture of sulfonate salts.
优选地,所述润湿剂选自壬基酚聚氧乙烯醚、K12或聚氧乙烯脂肪醇醚中的任意一种或至少两种的混合物,其中典型但非限制性的混合物为壬基酚聚氧乙烯醚和K12的混合物,K12和聚氧乙烯脂肪醇醚的混合物。Preferably, the wetting agent is selected from any one or a mixture of at least two of nonylphenol ethoxylates, K12 or polyoxyethylene fatty alcohol ethers, wherein a typical but non-limiting mixture is nonylphenol a mixture of polyoxyethylene ether and K12, a mixture of K12 and polyoxyethylene fatty alcohol ether.
优选地,所述消泡剂选自硅氧烷类消泡剂,至于具体的硅氧烷类消泡剂种类,本领域技术人员可以根据实际需要进行常规选择,本发明不做特殊限定。Preferably, the antifoaming agent is selected from the group consisting of silicone antifoaming agents. As for the specific silicone antifoaming agent type, those skilled in the art can make conventional selection according to actual needs, and the invention is not particularly limited.
优选地,所述惰性载体选自玉米淀粉、滑石粉、蔗糖、硫酸钾、高岭土或硅藻土中的任意一种或至少两种的混合物,其中典型但非限制性的混合物为:玉米淀粉和滑石粉的混合物,蔗糖和硫酸钾的混合物,高岭土和玉米淀粉的混合物。Preferably, the inert carrier is selected from any one or a mixture of at least two of corn starch, talc, sucrose, potassium sulfate, kaolin or diatomaceous earth, wherein a typical but non-limiting mixture is: corn starch and a mixture of talc, a mixture of sucrose and potassium sulfate, a mixture of kaolin and corn starch.
本发明所述的吡唑醚菌酯水分散固体组合物,其制剂为可湿性粉剂或水分散颗粒剂。The pyraclostrobin aqueous dispersion solid composition of the present invention is formulated as a wettable powder or a water-dispersible granule.
进一步,本发明提供了所述吡唑醚菌酯水分散固体组合物的制备方法,包括以下步骤:Further, the present invention provides a method for preparing the pyraclostrobin aqueous dispersion solid composition, comprising the steps of:
(1)按配比将吡唑醚菌酯与烷基磺酸盐混合;(1) mixing pyraclostrobin and an alkyl sulfonate according to a ratio;
(2)将得到的混合物在35℃以下进行粗粉碎,得到均质混合物;(2) coarsely pulverizing the obtained mixture at 35 ° C or lower to obtain a homogeneous mixture;
(3)在得到的均质混合物中,加入多孔性载体和功能性助剂,进行细粉碎,得到所述吡唑醚菌酯水分散固体组合物。(3) A porous carrier and a functional auxiliary agent are added to the obtained homogeneous mixture, and finely pulverized to obtain the pyrazolidin ester aqueous dispersion solid composition.
不同于以往公开的制备方法,本发明在步骤(1)中首先只将吡唑醚菌酯与烷基磺酸盐进行混合,而不采用将所有组分或者连同分散剂和消泡剂以及载体进行一块混合的形式。Unlike the previously disclosed preparation method, the present invention firstly mixes pyraclostrobin and an alkyl sulfonate in step (1) without using all components or together with a dispersing agent and an antifoaming agent and a carrier. Carry out a mixed form.
本发明通过在步骤(1)中先将吡唑醚菌酯与烷基磺酸盐混合,经第一次粗粉碎使得吡唑醚菌酯与烷基磺酸盐混合更充分,烷基磺酸盐更有效地在吡唑醚菌酯颗粒表面附着吸附,有效阻止了在存储过程中颗粒与颗粒之间的接触聚集。The invention firstly mixes the pyraclostrobin and the alkyl sulfonate in the step (1), and the first coarse pulverization makes the pyraclostrobin and the alkyl sulfonate more fully mixed, the alkyl sulfonic acid. The salt adheres more effectively to the surface of the pyraclostrobin particles, effectively preventing contact aggregation between the particles and the particles during storage.
发明人还意外发现,当只将吡唑醚菌酯与烷基磺酸盐进行先混合时,通过采用在35℃以下进行粗粉碎,其能够使吡唑醚菌酯呈现为膏状物,具有软化现象,从而更进一步有助于后面水分散固体颗粒物成品避免团聚结块问题。The inventors have also unexpectedly discovered that when only pyraclostrobin and the alkyl sulfonate are first mixed, by using coarse pulverization at 35 ° C or lower, the pyraclostrobin can be rendered as a paste having Softening, which further contributes to the problem of agglomeration and agglomeration in the back water-dispersible solid particulate product.
对于将吡唑醚菌酯与烷基磺酸盐混合后得到的混合物,本发明采用了在低温下进行粉碎,其具体采用的是在35℃以下的低温下进行,例如温度为0℃、4℃、8℃、10℃、12℃、15℃、20℃、22℃、25℃、28℃、30℃或35℃,当然也可以在0度以下进行。For the mixture obtained by mixing pyraclostrobin and the alkyl sulfonate, the present invention employs pulverization at a low temperature, which is specifically carried out at a low temperature of 35 ° C or lower, for example, a temperature of 0 ° C, 4 °C, 8 ° C, 10 ° C, 12 ° C, 15 ° C, 20 ° C, 22 ° C, 25 ° C, 28 ° C, 30 ° C or 35 ° C, of course, can also be carried out below 0 degrees.
吡唑醚菌酯原药熔点为56~64℃,如果采用常规条件下直接粉碎,原药会发生软化现象,影响粉碎效率,。而采用在本发明的低温下粉碎可有效解决吡唑醚菌酯原药在粉碎过程中颗粒碰撞而软化现象,同时使得烷基磺酸盐充分均匀并紧密附着在吡唑醚菌酯颗粒表面,解决了后续二次气流粉碎对吡唑醚菌酯颗粒的影响。The melting point of pyraclostrobin is 56-64 ° C. If it is directly pulverized under normal conditions, the original drug will soften and affect the pulverization efficiency. However, the pulverization at the low temperature of the present invention can effectively solve the problem of particle collision and softening of the pyraclostrobin original drug during the pulverization process, and at the same time, the alkyl sulfonate is sufficiently uniform and closely adhered to the surface of the pyraclostrobin particle. The effect of subsequent secondary jet pulverization on pyraclostrobin particles was solved.
本发明采用在粗粉碎后得到的均质混合物中,再加入多孔性载体和功能性助剂,这样的操作能够使粉碎的温度相对宽松,其可以采用相对较高的温度下进行,此时功能性助剂能起到一定的保护作用,进一步起到对最终形成的吡唑醚菌酯水分散固体组合物避免团聚和结块产生促进作用。The invention adopts a homogeneous mixture obtained after coarse pulverization, and further adds a porous carrier and a functional auxiliary agent, such an operation can make the pulverization temperature relatively loose, and can be carried out at a relatively high temperature, at this time, the function The auxiliaries can play a certain protective role, and further play a role in promoting the agglomeration and agglomeration of the finally formed pyraclostrobin aqueous dispersion solid composition.
本发明的制备方法中,采用了低温下粗粉碎结合细粉碎的操作方式,通过将粉碎分成粗粉碎和细粉碎两步操作,烷基磺酸盐与吡唑醚菌酯的混合更 充分,更有效地在吡唑醚菌酯颗粒表面附着吸附,进一步有效阻止了在存储过程中颗粒与颗粒之间的接触团聚现象。In the preparation method of the present invention, the operation mode of coarse pulverization combined with fine pulverization at a low temperature is adopted, and by mixing the pulverization into two steps of coarse pulverization and fine pulverization, the mixture of the alkyl sulfonate and the pyraclostrobin is more fully and more. Effective adhesion to the surface of the pyraclostrobin particles further effectively prevents contact agglomeration between the particles and the particles during storage.
本发明在制备不同形式的水分散固体组合物时,例如制备可湿性粉剂时,上述制备方法中在步骤(3)进行细粉碎后,直接可以得到该可湿性粉剂;而当制备水分散颗粒剂时,在步骤(3)进行细粉碎后,还需经造粒烘干步骤,才可得到该水分散颗粒剂。对于造粒烘干技术,本领域技术人员应当明了,其可以采用例如挤压造粒、喷雾造粒、旋转造粒、流化床造粒等多种操作方式,本发明对其不做特殊限定。In the preparation of different forms of the water-dispersible solid composition of the present invention, for example, when preparing a wettable powder, the wettable powder can be directly obtained after the fine pulverization in the above preparation method in the step (3); and when the water-dispersible granule is prepared When the fine pulverization is carried out in the step (3), the granulation drying step is also required to obtain the water-dispersible granule. For the granulation and drying technology, those skilled in the art should understand that it can adopt various operation modes such as extrusion granulation, spray granulation, rotary granulation, fluidized bed granulation, etc., and the present invention does not specifically limit it. .
本发明中,步骤(2)所述粗粉碎采用气流粉碎,其具体操作为:将混合料以一定的速度通过高速气流,使得颗粒与颗粒、颗粒与内壁之间产生强烈碰撞而达到破损的效果,其最终使得粉碎后粒径D90≤20μm。In the present invention, the coarse pulverization in the step (2) is carried out by airflow pulverization, and the specific operation is as follows: the mixture is passed through the high-speed airflow at a certain speed, so that a strong collision between the particles and the particles, the particles and the inner wall is achieved, and the damage is achieved. It finally makes the particle size after pulverization D90 ≤ 20 μm.
至于上述气流粉碎所采用的具体气流速度,本领域技术人员可以根据实际要粉碎后的粒径大小进行调整,本发明不做特殊限定。As for the specific gas flow rate used in the above-mentioned airflow pulverization, those skilled in the art can adjust the particle size according to the actual pulverization, and the present invention is not particularly limited.
本发明采用气流粉碎能够实现吡唑醚菌酯与烷基磺酸盐的均匀混合,提高混合的均匀度和散热效果。The invention adopts jet milling to realize uniform mixing of pyraclostrobin and alkylsulfonate, and improves mixing uniformity and heat dissipation effect.
本发明中,步骤(3)所述细粉碎采用二次气流粉碎,其可以调整粉碎压力和进料速度,以使粉碎后粒径达到1~15μm。In the present invention, the fine pulverization in the step (3) is carried out by secondary gas flow pulverization, which can adjust the pulverization pressure and the feed rate so that the pulverized particle diameter reaches 1 to 15 μm.
至于二次气流粉碎所采用的具体气流速度、粉碎压力以及进料速度,本领域技术人员也是可以根据实际要达到的粉碎后粒径大小进行调整的。As for the specific gas flow rate, pulverization pressure and feed rate used in the secondary air flow pulverization, those skilled in the art can also adjust according to the actual pulverized particle size to be achieved.
本发明的吡唑醚菌酯水分散固体组合物可以是可湿性粉剂或者水分散颗粒剂。该吡唑醚菌酯水分散固体组合物具有热贮和常贮稳定性好,不聚集、不结块,不堵塞过滤器或喷雾头等优点,从而方便了贮存和用户使用,并提高了吡唑醚菌酯的药效。The pyraclostrobin aqueous dispersion solid composition of the present invention may be a wettable powder or a water-dispersible granule. The pyraclostrobin aqueous dispersion solid composition has the advantages of good heat storage and normal storage stability, no aggregation, no agglomeration, no clogging of the filter or the spray head, thereby facilitating storage and user use, and improving pyrazole. The efficacy of ether oxystrobin.
与现有技术相比,本发明至少具有以下有益效果:Compared with the prior art, the present invention has at least the following beneficial effects:
(1)本发明的吡唑醚菌酯水分散固体组合物,具有热贮和常贮稳定性好,不聚集、不结块,不堵塞过滤器或喷雾头等优点,流动性好;(1) The pyraclostrobin aqueous dispersion solid composition of the invention has the advantages of good heat storage and normal storage stability, no aggregation, no agglomeration, no clogging of a filter or a spray head, and good fluidity;
(2)本发明制备吡唑醚菌酯水分散固体组合物的方法操作简便,经济成本低,可实现性强。(2) The method for preparing a pyridoxazole aqueous dispersion solid composition of the present invention is simple in operation, low in economic cost, and achievable.
具体实施方式detailed description
为便于理解本发明,本发明列举实施例如下。本领域技术人员应该明了,所述实施例仅仅是帮助理解本发明,不应视为对本发明的具体限制。以下“%”均指重量百分比。To facilitate an understanding of the invention, the invention is set forth below. It should be understood by those skilled in the art that the present invention is not to be construed as limited. The following "%" refers to the weight percentage.
实施例1:20%吡唑醚菌酯 可湿性粉剂Example 1: 20% pyraclostrobin wettable powder
吡唑醚菌酯 20%Pyraclostrobin 20%
Morwet D425(烷基萘磺酸盐甲醛缩聚物) 8%Morwet D425 (alkylnaphthalene sulfonate formaldehyde polycondensate) 8%
气相白炭黑 10%Gas phase white carbon black 10%
Soap L(牛脂酸钠) 2%Soap L (sodium tallowate) 2%
玉米淀粉 60%Corn starch 60%
配制过程:将吡唑醚菌酯原药与Morwet D425(烷基萘磺酸盐甲醛缩聚物)按重量比例混合,搅拌均匀后,在温度为30℃下进行第一次粗粉碎,得到均质混合物;然后将气相白炭黑、Soap L(牛脂酸钠)和玉米淀粉按重量比例加入到上述粗粉碎混料中,进行第二次细粉碎,直到粒径D90<10μm,即得最终产品。Preparation process: the pyraclostrobin original drug and Morwet D425 (alkylnaphthalenesulfonate formaldehyde polycondensate) are mixed in a weight ratio, and after stirring uniformly, the first coarse pulverization is carried out at a temperature of 30 ° C to obtain homogeneity. Mixture; then gas phase white carbon, Soap L (sodium tallow) and corn starch are added to the above coarsely pulverized mixture in a weight ratio, and subjected to a second fine pulverization until the particle diameter D90 < 10 μm, that is, the final product.
实施例2:50%吡唑醚菌酯 水分散粒剂Example 2: 50% pyraclostrobin water dispersible granules
吡唑醚菌酯 50%Pyraclostrobin 50%
Morwet EFW(烷基萘磺酸盐) 10%Morwet EFW (alkylnaphthalene sulfonate) 10%
白炭黑 20%White carbon black 20%
EO/PO嵌段共聚物 5%EO/PO block copolymer 5%
Soap L(牛脂酸钠) 2%Soap L (sodium tallowate) 2%
硅藻土 13%Diatomaceous earth 13%
配制过程:将吡唑醚菌酯原药与Morwet EFW(烷基萘磺酸盐)按重量比例混合,搅拌均匀后,在温度为25℃下进行第一次粗粉碎,得到均质混合物;然后将白炭黑、EO/PO嵌段共聚物、Soap L(牛脂酸钠)和硅藻土按重量比例加入到上述粗粉碎混料中,进行第二次细粉碎,得到粒径D90<10μm的母粉, 该母粉加入适量的水捏合后,经过挤压造粒烘干得到最终产品。The preparation process: mixing the pyraclostrobin original drug with Morwet EFW (alkylnaphthalene sulfonate) in a weight ratio, stirring uniformly, and performing the first coarse pulverization at a temperature of 25 ° C to obtain a homogeneous mixture; White carbon black, EO/PO block copolymer, Soap L (sodium tallowate) and diatomaceous earth were added to the above coarsely pulverized mixture in a weight ratio, and subjected to a second fine pulverization to obtain a particle diameter of D90 < 10 μm. The mother powder, which is kneaded by adding an appropriate amount of water, is dried by extrusion granulation to obtain a final product.
实施例3:10%吡唑醚菌酯 可湿性粉剂Example 3: 10% pyraclostrobin wettable powder
吡唑醚菌酯 10%Pyraclostrobin 10%
十二烷基磺酸钠 5%Sodium dodecyl sulfonate 5%
煅烧高岭土 20%Calcined kaolin 20%
壬基酚聚氧乙烯醚磷酸酯 5%Nonylphenol polyoxyethylene ether phosphate 5%
Soap L(牛脂酸钠) 1%Soap L (sodium tallowate) 1%
硫酸钾 59%Potassium sulfate 59%
配制过程:将吡唑醚菌酯原药与十二烷基磺酸钠按重量比例混合,搅拌均匀后,在温度为22℃下进行第一次粗粉碎,得到均质混合物;然后将煅烧高岭土、壬基酚聚氧乙烯醚磷酸酯、Soap L(牛脂酸钠)和硫酸钾按重量比例加入到上述粗粉碎混料中,进行第二次细粉碎,直到粒径D90<10μm,即得最终产品。The preparation process: mixing the pyraclostrobin original drug with sodium dodecylsulfonate in a weight ratio, stirring uniformly, and performing the first coarse pulverization at a temperature of 22 ° C to obtain a homogeneous mixture; then calcining the kaolin , nonylphenol polyoxyethylene ether phosphate, Soap L (sodium tallow) and potassium sulfate are added to the above coarsely pulverized mixture in a weight ratio, and subjected to a second fine pulverization until the particle diameter D90 < 10 μm, which is the final product.
实施例4:5%吡唑醚菌酯+10%啶酰菌胺 可湿性粉剂Example 4: 5% pyraclostrobin + 10% boscalyl wettable powder
吡唑醚菌酯 5%Pyraclostrobin 5%
啶酰菌胺 10%Boscalid 10%
烷基乙基磺酸盐 5%Alkyl ethyl sulfonate 5%
植物纤维 10%Plant fiber 10%
脂肪醇聚氧乙烯醚 10%Fatty alcohol polyoxyethylene ether 10%
Soap L(牛脂酸钠) 2%Soap L (sodium tallowate) 2%
滑石粉 58%Talc 58%
配制过程:将吡唑醚菌酯原药与烷基乙基磺酸盐按重量比例混合,搅拌均匀后,在温度35℃下进行第一次粗粉碎,得到均质混合物;然后将啶酰菌胺、植物纤维、脂肪醇聚氧乙烯醚、Soap L(牛脂酸钠)和滑石粉按重量比例加入到上述粗粉碎混料中,进行第二次细粉碎,直到粒径D90<10μm,即得最终产品。The preparation process: mixing the pyraclostrobin original drug with the alkyl ethyl sulfonate in a weight ratio, stirring uniformly, and performing the first coarse pulverization at a temperature of 35 ° C to obtain a homogeneous mixture; then, the acyl bacterium Amine, plant fiber, fatty alcohol polyoxyethylene ether, Soap L (sodium tallow) and talc are added to the above coarsely pulverized mixture in a weight ratio, and subjected to a second fine pulverization until the particle diameter D90 < 10 μm. Final product.
实施例5:5%吡唑醚菌酯+40%百菌清 水分散颗粒剂Example 5: 5% pyraclostrobin + 40% chlorothalonil water-dispersible granules
吡唑醚菌酯 5%Pyraclostrobin 5%
百菌清 40%Chlorothalonil 40%
烷基萘磺酸盐甲醛缩聚物 5%Alkylnaphthalene sulfonate formaldehyde polycondensate 5%
矿物纤维 10%Mineral fiber 10%
聚羧酸盐 10%Polycarboxylate 10%
琥珀酸磺酸钠 5%Sodium succinate 5%
Soap L(牛脂酸钠) 2%Soap L (sodium tallowate) 2%
高岭土 23%Kaolin 23%
配制过程:将吡唑醚菌酯原药与烷基萘磺酸盐甲醛缩聚物按重量比例混合,搅拌均匀后,在温度为10℃下进行第一次粗粉碎,得到均质混合物;然后将百菌清、矿物纤维、聚羧酸盐、琥珀酸磺酸钠、Soap L(牛脂酸钠)和高岭土按重量比例加入到上述粗粉碎混料中,进行第二次细粉碎,得到粒径D90<10μm的母粉,该母粉加入适量的水捏合后,经过挤压造粒烘干得到最终产品。The preparation process comprises: mixing the pyraclostrobin original drug with the alkylnaphthalenesulfonate formaldehyde polycondensate in a weight ratio, stirring uniformly, and performing the first coarse pulverization at a temperature of 10 ° C to obtain a homogeneous mixture; Chlorothalonil, mineral fiber, polycarboxylate, sodium succinate sulfonate, Soap L (sodium tallowate) and kaolin are added to the above coarsely pulverized mixture in a weight ratio, and subjected to a second fine pulverization to obtain a particle size D90. <10 μm of the mother powder, which is kneaded by adding an appropriate amount of water, and then dried by extrusion granulation to obtain a final product.
对比例1:20%吡唑醚菌酯 可湿性粉剂Comparative Example 1: 20% pyraclostrobin WP
Figure PCTCN2018086270-appb-000001
Figure PCTCN2018086270-appb-000001
配制过程:将上述组合物进行气流粉碎,使得粒径D90<10μm,即得最终产品Preparation process: the above composition is subjected to jet milling to make the particle size D90 <10 μm, that is, the final product
对比例2:50%吡唑醚菌酯 水分散粒剂Comparative Example 2: 50% pyraclostrobin water dispersible granules
Figure PCTCN2018086270-appb-000002
Figure PCTCN2018086270-appb-000002
配制过程:将上述组合物进行气流粉碎,得到粒径D90<10μm的母粉,该母粉加入适量的水捏合后,经过挤压造粒烘干得到最终产品。Preparation process: The above composition is subjected to jet milling to obtain a mother powder having a particle diameter of D90 < 10 μm. The mother powder is kneaded by adding an appropriate amount of water, and then dried by extrusion granulation to obtain a final product.
对比例3:10%吡唑醚菌酯 可湿性粉剂Comparative Example 3: 10% pyraclostrobin wettable powder
Figure PCTCN2018086270-appb-000003
Figure PCTCN2018086270-appb-000003
配制过程:将上述组合物进行气流粉碎,使得粒径D90<10μm,即得最终产品Preparation process: the above composition is subjected to jet milling to make the particle size D90 <10 μm, that is, the final product
对比例4:10%吡唑醚菌酯 可湿性粉剂Comparative Example 4: 10% pyraclostrobin wettable powder
Figure PCTCN2018086270-appb-000004
Figure PCTCN2018086270-appb-000004
Figure PCTCN2018086270-appb-000005
Figure PCTCN2018086270-appb-000005
配制过程:将上述组合物进行气流粉碎,使得粒径D90<10μm,即得最终产品。Formulation process: The above composition is subjected to jet milling so that the particle diameter D90 < 10 μm, that is, the final product.
对比例5:50%吡唑醚菌酯 水分散粒剂Comparative Example 5: 50% pyraclostrobin water dispersible granules
Figure PCTCN2018086270-appb-000006
Figure PCTCN2018086270-appb-000006
配制过程:将上述组合物进行气流粉碎,得到粒径D90<10μm的母粉,该母粉加入适量的水捏合后,经过挤压造粒烘干得到最终产品。Preparation process: The above composition is subjected to jet milling to obtain a mother powder having a particle diameter of D90 < 10 μm. The mother powder is kneaded by adding an appropriate amount of water, and then dried by extrusion granulation to obtain a final product.
对比例6:5%吡唑醚菌酯+10%啶酰菌胺 可湿性粉剂Comparative Example 6: 5% pyraclostrobin + 10% boscalid wettable powder
Figure PCTCN2018086270-appb-000007
Figure PCTCN2018086270-appb-000007
Figure PCTCN2018086270-appb-000008
Figure PCTCN2018086270-appb-000008
配制过程:将上述组合物进行气流粉碎,使得粒径D90<10μm,即得最终产品。Formulation process: The above composition is subjected to jet milling so that the particle diameter D90 < 10 μm, that is, the final product.
对比例7:5%吡唑醚菌酯+40%百菌清 水分散颗粒剂Comparative Example 7: 5% pyraclostrobin + 40% chlorothalonil Water-dispersible granules
Figure PCTCN2018086270-appb-000009
Figure PCTCN2018086270-appb-000009
配制过程:将上述组合物进行气流粉碎,得到粒径D90<10μm的母粉,该母粉加入适量的水捏合后,经过挤压造粒烘干得到最终产品。Preparation process: The above composition is subjected to jet milling to obtain a mother powder having a particle diameter of D90 < 10 μm. The mother powder is kneaded by adding an appropriate amount of water, and then dried by extrusion granulation to obtain a final product.
对比例8:Comparative example 8:
与对比例1相同的组分,采用本发明的配制相似的方法进行制备。The same components as in Comparative Example 1 were prepared by a similar method of the present invention.
配制过程:将吡唑醚菌酯与聚羧酸钠盐按重量比混合,搅拌均匀后,在 温度30℃下进行第一次粗粉碎,然后将气相白炭黑、Soap L(牛脂酸钠)和玉米淀粉按重量比例加入到上述粗粉混料中,进行第二次细粉碎,直到粒径D90<10μm,即得最终产品。The preparation process: the pyraclostrobin and the polycarboxylate sodium salt are mixed in a weight ratio, and after being uniformly stirred, the first coarse pulverization is carried out at a temperature of 30 ° C, and then the gas phase white carbon black, Soap L (sodium borate) And the corn starch is added to the above coarse powder mixture in a weight ratio, and the second fine pulverization is carried out until the particle diameter D90 < 10 μm, that is, the final product is obtained.
对比例9:Comparative example 9:
与对比例4相同的组分,采用本发明的配制方法进行制备。The same components as in Comparative Example 4 were prepared by the formulation method of the present invention.
配制过程:将吡唑醚菌酯与十二烷基磺酸钠按重量比混合,搅拌均匀后,在温度30℃下进行第一次粗粉碎,然后将壬基酚聚氧乙烯醚磷酸酯、Soap L(牛脂酸钠)和硫酸钾按重量比例加入到上述粗粉混料中,进行第二次细粉碎,直到粒径D90<10μm,即得最终产品。The preparation process comprises: mixing pyraclostrobin and sodium dodecylsulfonate in a weight ratio, stirring uniformly, performing the first coarse pulverization at a temperature of 30 ° C, and then adding nonylphenol ethoxylate phosphate, Soap L (sodium tallowate) and potassium sulfate are added to the above coarse powder mixture in a weight ratio, and subjected to a second fine pulverization until the particle diameter D90 < 10 μm, that is, the final product is obtained.
对比例10:Comparative example 10:
与对比例5相同的组分。采用本发明的配制方法进行制备。The same components as in Comparative Example 5. The preparation is carried out using the formulation method of the present invention.
配制过程:将吡唑醚菌酯与Morwet EFW(烷基萘磺酸盐)按重量比混合,搅拌均匀后,在温度30℃下进行第一次粗粉碎,然后将EO/PO嵌段共聚物、Soap L(牛脂酸钠)和硫酸钠按重量比例加入到上述粗粉混料中,进行第二次细粉碎,得到粒径D90<10μm的母粉,该母粉加入适量的水捏合后,经过挤压造粒烘干得到最终产品。The preparation process: the pyraclostrobin and Morwet EFW (alkylnaphthalene sulfonate) are mixed in a weight ratio, and after being uniformly stirred, the first coarse pulverization is carried out at a temperature of 30 ° C, and then the EO/PO block copolymer is used. Soap L (sodium tallow) and sodium sulfate are added to the above coarse powder mixture in a weight ratio, and subjected to a second fine pulverization to obtain a mother powder having a particle diameter of D90 < 10 μm, and the mother powder is kneaded by adding an appropriate amount of water. The final product is obtained by extrusion granulation and drying.
测试上述实施例1~5和对比例1~10制备的样品的理化稳定性,包括常温稳定性和热贮稳定性。The physical and chemical stability of the samples prepared in the above Examples 1 to 5 and Comparative Examples 1 to 10, including room temperature stability and heat storage stability, were tested.
常温稳定性测试常温样品性状和悬浮率指标(CIPAC MT184方法)。Normal temperature stability test at room temperature sample traits and levitation rate indicators (CIPAC MT184 method).
热贮稳定性试验是在54℃烘箱中进行。在54℃的烘箱中热贮后,将样品从烘箱中取出。冷却至室温,将各测试样品倒出,观察样品流动性。然后 将可湿性粉剂样品直接过325目筛子;水分散颗粒剂样品用水稀释后,过325目筛子。The heat storage stability test was carried out in an oven at 54 °C. After heat storage in an oven at 54 ° C, the samples were removed from the oven. After cooling to room temperature, each test sample was poured out to observe the fluidity of the sample. The wettable powder sample was then passed directly through a 325 mesh screen; the water dispersed granule sample was diluted with water and passed through a 325 mesh screen.
测试的结果如表1所示。The results of the test are shown in Table 1.
表1Table 1
Figure PCTCN2018086270-appb-000010
Figure PCTCN2018086270-appb-000010
Figure PCTCN2018086270-appb-000011
Figure PCTCN2018086270-appb-000011
表1中的测试结果表明,根据本发明制备的吡唑醚菌酯水分散固体组合物在常温下,有较好的流动性,样品均匀,无团聚、无粘结现象,尤其与对比例相比有较高的悬浮率,基本上达到85%以上的悬浮率,这是对比例远远达不到的。而在热贮稳定性测试中,本发明的吡唑醚菌酯水分散固体组合物对比例相比热贮稳定性性能更突出,流动性好,无结块,无堵塞筛网,因此具有更方便用户使用和提高吡唑醚菌酯药效的突出优势。The test results in Table 1 show that the pyraclostrobin aqueous dispersion solid composition prepared according to the present invention has good fluidity at room temperature, uniform sample, no agglomeration, no sticking phenomenon, especially with the comparative phase. Compared with a higher suspension rate, it basically reaches a suspension rate of more than 85%, which is far from being comparable. In the heat storage stability test, the pyraclostrobin aqueous dispersion solid composition of the present invention has more outstanding heat storage stability performance, good fluidity, no agglomeration, no clogging screen, and therefore has more It is convenient for users to use and improve the outstanding advantages of pyraclostrobin.
申请人声明,本发明通过上述实施例来说明本发明的详细工艺设备和工艺流程,但本发明并不局限于上述详细的技术方案,即不意味着本发明必须依赖上述详细的技术方案才能实施。所属技术领域的技术人员应该明了,对本发明的任何改进,对本发明产品各原料的等效替换及辅助成分的添加、具体方式的选择等,均落在本发明的保护范围和公开范围之内。The Applicant declares that the present invention illustrates the detailed process equipment and process flow of the present invention by the above embodiments, but the present invention is not limited to the above detailed technical solutions, that is, it does not mean that the present invention must rely on the above detailed technical solutions to implement. . It should be apparent to those skilled in the art that any modifications of the present invention, equivalent substitution of the various materials of the products of the present invention, addition of auxiliary components, selection of specific means, and the like, are all within the scope of the present invention.

Claims (9)

  1. 一种吡唑醚菌酯水分散固体组合物,其特征在于,按重量百分比包括以下组分:吡唑醚菌酯5~50%,烷基磺酸盐0.1~15%,多孔性载体5~80%,功能性助剂1~45%。A liquid dispersion solid composition of pyraclostrobin characterized by comprising the following components in a weight percentage: 5-50% of pyraclostrobin, 0.1-15% of an alkyl sulfonate, and a porous carrier 5~ 80%, functional additives 1 to 45%.
  2. 如权利要求1所述的吡唑醚菌酯水分散固体组合物,其特征在于,按重量百分比由以下组分组成:吡唑醚菌酯6~30%,烷基磺酸盐2~5%,多孔性载体10~70%,余量为功能性助剂。The pyraclostrobin aqueous dispersion solid composition according to claim 1, which is composed of the following components in a weight percentage: 6 to 30% of pyraclostrobin and 2 to 5% of an alkyl sulfonate. The porous carrier is 10 to 70%, and the balance is a functional auxiliary.
  3. 如权利要求1或2所述的吡唑醚菌酯水分散固体组合物,其特征在于,所述烷基磺酸盐选自烷基萘磺酸盐、烷基萘磺酸盐甲醛缩聚物、烷基苯磺酸盐、烷基乙基磺酸盐或仲烷基磺酸盐中的任意一种或至少两种的混合物,优选烷基萘磺酸盐甲醛缩聚物;The pyraclostrobin aqueous dispersion solid composition according to claim 1 or 2, wherein the alkyl sulfonate is selected from the group consisting of alkyl naphthalene sulfonates, alkyl naphthalene sulfonate formaldehyde polycondensates, Any one or a mixture of at least two alkylbenzene sulfonates, alkyl ethyl sulfonates or secondary alkyl sulfonates, preferably alkylnaphthalene sulfonate formaldehyde polycondensates;
    优选地,所述多孔性载体选自高岭土、蒙脱粘土、绿坡缕石、合成硅、植物纤维、矿物纤维或硅酸镁铝中的任意一种或至少两种的混合物;Preferably, the porous carrier is selected from the group consisting of kaolin, montmorillonite, attapulgite, synthetic silicon, plant fiber, mineral fiber or magnesium aluminum silicate, or a mixture of at least two;
    优选地,所述高岭土选自高岭石、迪开石、珍珠陶土、富硅高岭石、多水高岭石或多水埃洛石中的任意一种或至少两种的混合物;所述蒙脱粘土选自贝得石、锂蒙脱石、皂石或斑脱土中的任意一种或至少两种的混合物;所述绿坡缕石选自漂白土和/或海泡石;所述合成硅选自白炭黑和/或气相白炭黑;Preferably, the kaolin is selected from any one or a mixture of at least two of kaolinite, dickite, pearlite, silicon-rich kaolinite, halloysite or multi-water halloysite; The montmorillonite clay is selected from any one or a mixture of at least two of beidellite, hectorite, saponite or bentonite; the attapulgite is selected from the group consisting of bleaching earth and/or sepiolite; Said synthetic silicon is selected from the group consisting of white carbon black and/or fumed silica;
    优选地,所述功能性助剂选自分散剂、润湿剂、消泡剂或惰性载体中的任意一种或至少两种的混合物。Preferably, the functional adjuvant is selected from any one or a mixture of at least two of a dispersing agent, a wetting agent, an antifoaming agent or an inert carrier.
  4. 如权利要求3所述的吡唑醚菌酯水分散固体组合物,其特征在于,所述分散剂选自木质素磺酸盐、聚羧酸盐、脂肪醇聚氧乙烯醚或环氧乙烷环氧丙烷嵌段共聚物中的任意一种或至少两种的混合物;The pyraclostrobin aqueous dispersion solid composition according to claim 3, wherein the dispersing agent is selected from the group consisting of lignosulfonates, polycarboxylates, fatty alcohol polyoxyethylene ethers or ethylene oxide. Any one or a mixture of at least two of propylene oxide block copolymers;
    优选地,所述润湿剂选自壬基酚聚氧乙烯醚、K12或聚氧乙烯脂肪醇醚中的任意一种或至少两种的混合物;Preferably, the wetting agent is selected from any one or a mixture of at least two of nonylphenol ethoxylate, K12 or polyoxyethylene fatty alcohol ether;
    优选地,所述消泡剂选自硅氧烷类消泡剂;Preferably, the antifoaming agent is selected from the group consisting of silicone antifoaming agents;
    优选地,所述惰性载体选自玉米淀粉、滑石粉、蔗糖、硫酸钾、高岭土或硅藻土中的任意一种或至少两种的混合物。Preferably, the inert carrier is selected from any one or a mixture of at least two of corn starch, talc, sucrose, potassium sulfate, kaolin or diatomaceous earth.
  5. 如权利要求1-4之一所述的吡唑醚菌酯水分散固体组合物,其特征在于,所述组合物制剂为可湿性粉剂或水分散颗粒剂。The pyraclostrobin aqueous dispersion solid composition according to any one of claims 1 to 4, wherein the composition preparation is a wettable powder or a water-dispersible granule.
  6. 如权利要求1-5之一所述的吡唑醚菌酯水分散固体组合物的制备方法,其特征在于,包括以下步骤:The method for preparing a pyraclostrobin aqueous dispersion solid composition according to any one of claims 1 to 5, which comprises the steps of:
    (1)按配比将吡唑醚菌酯与烷基磺酸盐混合;(1) mixing pyraclostrobin and an alkyl sulfonate according to a ratio;
    (2)将得到的混合物在35℃以下进行粗粉碎,得到均质混合物;(2) coarsely pulverizing the obtained mixture at 35 ° C or lower to obtain a homogeneous mixture;
    (3)在得到的均质混合物中,加入多孔性载体和功能性助剂,进行细粉碎,得到所述吡唑醚菌酯水分散固体组合物。(3) A porous carrier and a functional auxiliary agent are added to the obtained homogeneous mixture, and finely pulverized to obtain the pyrazolidin ester aqueous dispersion solid composition.
  7. 如权利要求6所述的方法,其特征在于,步骤(3)所述细粉碎后,经造粒烘干,得到吡唑醚菌酯水分散颗粒剂。The method according to claim 6, wherein after the fine pulverization in the step (3), granulation and drying are carried out to obtain pyraclostrobin aqueous dispersion granules.
  8. 如权利要求6或7所述的方法,其特征在于,步骤(2)所述粗粉碎采用气流粉碎,并使粉碎后粒径D90≤20μm;The method according to claim 6 or 7, wherein the coarse pulverization in step (2) is carried out by air flow pulverization, and the particle size after pulverization is D90 ≤ 20 μm;
    优选地,步骤(3)所述细粉碎采用二次气流粉碎进行,并使粉碎后粒径达到1~15μm。Preferably, the fine pulverization in the step (3) is carried out by secondary air flow pulverization, and the particle diameter after pulverization is 1 to 15 μm.
  9. 如权利要求6-8之一所述的方法制备得到的吡唑醚菌酯水分散固体组合物。The pyraclostrobin aqueous dispersion solid composition prepared by the method of any one of claims 6-8.
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