JP2011006396A - Elution-regulating type agrochemical composition, and agrochemical granule - Google Patents

Elution-regulating type agrochemical composition, and agrochemical granule Download PDF

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JP2011006396A
JP2011006396A JP2010119224A JP2010119224A JP2011006396A JP 2011006396 A JP2011006396 A JP 2011006396A JP 2010119224 A JP2010119224 A JP 2010119224A JP 2010119224 A JP2010119224 A JP 2010119224A JP 2011006396 A JP2011006396 A JP 2011006396A
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agrochemical
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JP5550449B2 (en
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Koki Yakaito
弘毅 谷垣内
Kazuteru Ogawa
一輝 小川
Tetsuo Watabe
哲夫 渡部
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Nippon Kayaku Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide agrochemical granules containing a highly water-soluble agrochemical active ingredient, maintaining the elution of the chemical for a long period of time while keeping a sufficient elution efficiency of the chemical, and in addition the inexpensive and easily producible agricultural granules showing the chemical elution-regulating effect and also showing quick sinking property in water at their spraying application on water-filled fields such as the paddy fields of paddy rice cultivation, and also a method for producing the same, avoiding the decomposition of the thermally unstable agrochemical active ingredient in its production processes.SOLUTION: This agrochemical composition comprises (a) the agrochemical active ingredient, (b) a fatty acid and/or fatty acid derivative, (c) hardly water-soluble polysaccharides and (d) an inorganic substance. Further the agrochemical granules are obtained by mixing the agrochemical composition and then granulating.

Description

本発明は水田で発生する害虫を効率よく防除する農薬粒剤に関する。詳しくは、農薬活性成分、脂肪酸及び/又は脂肪酸誘導体、水難溶性多糖類、無機物質を含む農薬活性体組成物に関し、更にこれを造粒して得られる農薬粒剤に関する。水溶解度の高い農薬活性成分の溶出を制御し溶出期間を長期化させ、散布回数を減らし省力化を可能にする農薬粒剤に関する。また、当該農薬粒剤中に界面活性剤を添加及び/又は押出造粒して得られた農薬粒剤の表面にコーティングすることで、脂肪酸誘導体の比重の軽さと撥水性による粒の水面への浮上の結果起きる、流水や風による粒剤の局在化や水田からの流亡を防いで、均一な効力を発揮する農薬粒剤に関する。   The present invention relates to an agrochemical granule for efficiently controlling pests generated in paddy fields. Specifically, the present invention relates to an agrochemical active composition containing an agrochemical active ingredient, a fatty acid and / or a fatty acid derivative, a poorly water-soluble polysaccharide, and an inorganic substance, and further relates to an agrochemical granule obtained by granulating this. The present invention relates to an agrochemical granule that controls the elution of active ingredients with high water solubility, lengthens the elution period, reduces the number of spraying, and saves labor. In addition, by adding a surfactant to the agrochemical granule and / or coating the surface of the agrochemical granule obtained by extrusion granulation, the lightness of the specific gravity of the fatty acid derivative and water repellent to the water surface of the grain The present invention relates to an agrochemical granule that exhibits uniform efficacy by preventing the localization of the granule by flowing water and wind and the runoff from paddy fields that occur as a result of ascent.

近年、農業従事者の高齢化が益々深刻になり、農作業の省力化が求められている。それに伴い農薬も省力散布製剤やその散布方法に関する技術が検討されている。さらに、環境負荷低減という面から農薬の使用量及び使用回数の減少と使用期間の早期化が望まれる。これらの要請を受け、一回の農薬散布において薬剤を持続的長期間に亘り溶出させ得る、農薬活性成分の溶出制御、溶出期間の長期化を目的とした農薬粒剤の開発が行われている。そこで、農薬活性成分の土壌中及び水中における溶出速度を制御する製剤技術の開発が必要となるが、農薬活性成分の溶出を制御する製剤としてはこれまでにも様々な農薬基材を用いた製剤が開発されている。これらの中において脂肪酸及び/又は脂肪酸誘導体や、各種ワックスを用いた溶出制御製剤が知られている。例えば特許文献1にはスルホニルウレア系除草剤、活性炭、パラフィンワックス、及び鉱物質担体からなる除草用粒剤が開示されている。また特許文献2にはアルコール型ワックスを含有することを特徴とする農薬粒剤が開示されている。さらに、特許文献3ではモンタンロウ誘導体混合物を含有することを特徴とする農薬粒剤が開示されている。   In recent years, the aging of farmers has become more and more serious, and labor saving of farm work has been demanded. Along with this, techniques related to labor-saving spray formulations and spraying methods for agricultural chemicals are being studied. Furthermore, from the viewpoint of reducing the environmental burden, it is desirable to reduce the amount and number of use of agricultural chemicals and accelerate the use period. In response to these requests, agrochemical granules have been developed for the purpose of controlling the elution of pesticide active ingredients and extending the elution period so that the drug can be eluted for a long period of time in a single application of pesticide. . Therefore, it is necessary to develop a formulation technology that controls the dissolution rate of agricultural chemical active ingredients in soil and water. Has been developed. Among these, dissolution controlled preparations using fatty acids and / or fatty acid derivatives and various waxes are known. For example, Patent Document 1 discloses a herbicidal granule comprising a sulfonylurea herbicide, activated carbon, paraffin wax, and a mineral carrier. Patent Document 2 discloses an agrochemical granule characterized by containing an alcohol type wax. Furthermore, Patent Document 3 discloses an agrochemical granule characterized by containing a montan wax derivative mixture.

特開昭63−35504号公報JP 63-35504 A 特開平11−292706号公報Japanese Patent Laid-Open No. 11-292706 特開2000−351705号公報JP 2000-351705 A

しかし、特許文献1ないし3に示した溶出制御農薬粒剤は長期持続型の溶出が保てず、十分な生物効果を得られない。あるいは農薬活性成分の溶出効率が十分でなく、農薬粒剤中に薬物が一部もしくは多くの含量が留まってしまい、一定の施用量において生物効果を得るための十分な溶出が得られないといった欠点があった。また、水溶解度の高い農薬活性成分を長期間溶出制御させるには、農薬粒剤中のワックスの割合を多くする必要がある。このような農薬粒剤を田植え後に水田の湛水下に用いる場合、その比重の小ささや撥水性のため粒が水面に浮き、水流による農薬製剤の散布分布のばらつきや薬剤の流亡のため、効力が不十分になる。また風の影響を受けて田面のある一部分に局在化してしまい、均一な効果が得られないばかりか薬害の原因となる可能性がある。さらに、特許文献1ないし3の脂肪酸及び/又は脂肪酸誘導体を基材として用いる農薬粒剤の製造方法は、基材である脂肪酸及び/又は脂肪酸誘導体と農薬活性成分を加熱溶融して混合した後に、冷却固化したものを破砕造粒することによって得られる。しかしながら、熱によって分解を受ける農薬活性成分を用いた場合、上記のような加熱溶融工程を含む製造方法では製造することができない。一方、脂肪酸及び/又は脂肪酸誘導体と農薬活性成分を固体のまま直接混合し、加熱工程を経ずに押出造粒を行うと、得られる粒の硬度が低く、保存や輸送時に粒が割れたり欠けたりすることで、粒剤の総表面積が大きくなり望む溶出速度が得られなくなるおそれがある。
本発明の課題は、水溶性の高い農薬活性成分を含有する農薬粒剤において、十分な薬剤の溶出効率を保ちつつ薬剤の溶出を長期間維持できる農薬組成物、及びそれを用いた農薬粒剤を提供することである。加えて水稲栽培の水田圃場等、湛水圃場に散布施用した際において、前記薬剤溶出制御効果を示すとともに速やかな水中沈降性を示す、安価で製造容易な農薬粒剤を提供すると共に、製造工程において熱に不安定な農薬活性成分の分解を回避できる製造方法により、十分な硬度を有する農薬粒剤を提供することにある。
However, the elution controlled agrochemical granules shown in Patent Documents 1 to 3 cannot maintain long-lasting elution and cannot obtain a sufficient biological effect. Or the elution efficiency of active ingredients of agricultural chemicals is not enough, and some or much of the drug remains in the agricultural chemical granules, so that sufficient elution for obtaining a biological effect at a certain application rate cannot be obtained. was there. Moreover, in order to control the elution of a pesticidal active ingredient having high water solubility for a long period of time, it is necessary to increase the proportion of wax in the pesticidal granules. When such pesticide granules are used under paddy field flooding after rice planting, the grains float on the water surface due to their low specific gravity and water repellency, and due to variations in the distribution of agricultural chemical formulations due to water flow and the loss of drugs Becomes insufficient. In addition, it is localized in a certain part of the rice field under the influence of the wind, which may cause not only a uniform effect but also phytotoxicity. Furthermore, the manufacturing method of the agrochemical granule which uses the fatty acid and / or fatty acid derivative of Patent Documents 1 to 3 as a base material, after heating and melting the base material fatty acid and / or fatty acid derivative and the pesticidal active ingredient, It is obtained by crushing and granulating the cooled and solidified material. However, when an agrochemical active ingredient that is decomposed by heat is used, it cannot be produced by a production method including the heating and melting step as described above. On the other hand, when the fatty acid and / or fatty acid derivative and the agrochemical active ingredient are directly mixed in the solid state and extrusion granulation is carried out without passing through the heating step, the resulting particles have low hardness, and the particles are cracked or chipped during storage and transportation. By doing so, there is a possibility that the total surface area of the granule increases and the desired elution rate cannot be obtained.
An object of the present invention is to provide a pesticide granule containing a pesticide active ingredient having high water solubility, a pesticide composition capable of maintaining elution of the drug for a long time while maintaining sufficient elution efficiency of the drug, and a pesticide granule using the same Is to provide. In addition to providing a low-priced and easy-to-manufacture agricultural chemical granule that exhibits the above-described drug elution control effect when sprayed on a flooded field, such as paddy field for paddy rice cultivation, and a manufacturing process It is an object of the present invention to provide a pesticidal granule having sufficient hardness by a production method capable of avoiding decomposition of a thermally unstable pesticidal active ingredient.

本発明者らは、農薬粒剤に使用され得る種々の基材、増量剤、賦形剤を用いて検討した結果、農薬活性成分(a)、脂肪酸及び/又は脂肪酸誘導体(b)、水難溶性多糖類(c)、無機物質(d)を含有する農薬粒剤用組成物、及びこれを造粒してなる農薬粒剤が、水溶解度の高い農薬活性成分を水田湛水下で長期間溶出を制御できることを見出した。また、水難溶性多糖類(c)を添加することにより、加熱溶融工程を経ずに押出造粒のみで粒剤成形ができるとともに、十分な硬度を持った農薬粒剤を製造し得ることを見出した。さらに、用いる脂肪酸類によって引き起こされる農薬粒剤の浮上をより効率的に抑えて、水田における当該農薬粒剤の局在化や水田からの流亡を防ぐことのできる処方を見出した。すなわち、農薬活性成分とその他原材料を混合してなる農薬粒剤用組成物を、押出造粒機にて造粒して得られる農薬粒剤であり、さらに界面活性剤の添加によって脂肪酸誘導体由来の撥水性による粒の水面への浮上を抑えることができる農薬粒剤である。また、上記の水難溶性多糖類、無機物質、及び場合によって添加される界面活性剤は、農薬活性成分の水中への溶出を調整する効果を併せ持ち、その化合物の種類や添加量によって農薬活性成分の溶出特性を自在にコントロールすることができる。本願に係る農薬粒剤は、水溶解度の高い農薬活性成分の溶出を制御し溶出期間を長期化させることで、散布回数を減らして省力化を可能にするものである。   As a result of studies using various base materials, extenders and excipients that can be used in agricultural chemical granules, the present inventors have found that the agricultural chemical active ingredient (a), fatty acid and / or fatty acid derivative (b), poorly water-soluble A composition for agrochemical granules containing a polysaccharide (c) and an inorganic substance (d), and an agrochemical granule formed by granulating the composition, elutes a pesticide active ingredient with high water solubility under paddy paddy water for a long time. I found that I can control. Also, it has been found that by adding a poorly water-soluble polysaccharide (c), it is possible to form granules by extrusion granulation alone without going through a heating and melting step, and to produce agricultural chemical granules having sufficient hardness. It was. Furthermore, the present inventors have found a prescription that can more effectively suppress the floating of agricultural chemical granules caused by fatty acids to be used, and can prevent the localization of the agricultural chemical granules in paddy fields and the runoff from paddy fields. That is, it is an agrochemical granule obtained by granulating a composition for an agrochemical granule obtained by mixing an agrochemical active ingredient and other raw materials with an extrusion granulator, and further derived from a fatty acid derivative by adding a surfactant. It is an agrochemical granule which can suppress the floating of the grain to the water surface by water repellency. In addition, the poorly water-soluble polysaccharides, inorganic substances, and surfactants added in some cases have the effect of adjusting the dissolution of the agricultural chemical active ingredient into water, and depending on the type and amount of the compound, Elution characteristics can be controlled freely. The agrochemical granule according to the present application controls the elution of an agrochemical active ingredient having a high water solubility and lengthens the elution period, thereby reducing the number of spraying and enabling labor saving.

本発明の農薬組成物は、基材に用いる脂肪酸及び/又は脂肪酸誘導体、水難溶性多糖類、無機物質の種類や組合せ組成、及び含有量、並びに界面活性剤の種類や含有量を種々調整することにより、種々の農薬活性成分の溶出速度を制御することができる。これにより用いる農薬活性成分の至適濃度、対象とする病害虫、散布時期、作用期間に応じた製剤をデザインすることができ、その結果、用いる農薬活性成分の効力が十分に発揮される。また、田面水への沈降性も良好で、水田からの流亡や局在化もなく、その結果、作物に対する薬害のない優れた農薬粒剤として用いることができる。更に本願に係る農薬組成物は、加熱溶融混合工程を必要とせず、粒剤調製において混合容易な組成物であり、粒剤成形性に優れる一方で、十分な粒剤硬度が確保されるものである。   The agrochemical composition of the present invention adjusts various types of fatty acids and / or fatty acid derivatives, poorly water-soluble polysaccharides, inorganic substances, combinations and contents of inorganic substances, and types and contents of surfactants. Can control the elution rate of various agrochemical active ingredients. As a result, it is possible to design a preparation according to the optimum concentration of the pesticidal active ingredient to be used, the target pest, the spraying time, and the action period, and as a result, the efficacy of the pesticidal active ingredient to be used is fully exhibited. Moreover, the sedimentation property to paddy water is also good, there is no runaway and localization from the paddy field, and as a result, it can be used as an excellent pesticide granule having no phytotoxicity to crops. Furthermore, the agrochemical composition according to the present application does not require a heat-melt mixing step, is a composition that can be easily mixed in the preparation of a granule, and has excellent granule moldability, while ensuring sufficient granule hardness. is there.

以下に本発明の農薬組成物、それを用いた農薬粒剤、及びその農薬粒剤の製造方法についてより詳しく説明する。
本発明の農薬組成物に使用される農薬活性成分(a)は、通常、農薬殺虫活性成分または農薬殺菌活性成分であればいずれでもよく、基本的には制限はない。これらの中でも水中への溶解度が高い農薬活性成分が特に適している。具体的には、20℃における水溶解度が100ppm以上であり、水溶解度として0.01〜50重量%の範囲である水中溶出性が高い農薬活性成分に好適に使用できる。農薬活性成分としては、具体的には例えば次のようなものが挙げられるがこれに限定されるものではない。
農薬殺虫活性成分としては、例えば1,3−ジカルバモイルチオ−2−(N、N−ジメチルアミノ)−プロパン塩酸塩(カルタップ塩酸塩)、5−ジメチルアミノ−1,2,3−トリチアンシュウ酸塩(チオシクラムシュウ酸塩)、S,S'‐2‐ジメチルアミノトリメチレン−ジ(ベンゼンチオスルホナート)(ベンスルタップ)等のネライストキシン系殺虫剤;1‐(6‐クロロ‐3‐ピリジルメチル)‐N‐ニトロイミダゾリジン‐2‐イリデンアミン(イミダクロプリド)、3‐(2‐クロロ‐1,3‐チアゾール‐5‐イルメチル)‐5‐メチル‐1,3,5‐オキサジアジナン‐4‐イリデン(ニトロ)アミン(チアメトキサム)、(E)‐1‐(2‐クロロ‐1,3‐チアゾール‐5‐イルメチル)‐3‐メチル‐2‐ニトログアニジン(クロチアニジン)、(RS)‐1‐メチル‐2‐ニトロ‐3‐(テトラヒドロ‐3‐フリルメチル)グアニジン(ジノテフラン)、3‐(6‐クロロ‐3‐ピリジルメチル)‐1,3‐チアゾリジン‐2‐イリデンシアナミド(チアクロプリド)、(E)‐N‐(6‐クロロ‐3‐ピリジルメチル)‐N‐エチル‐N'‐メチル‐2‐ニトロビニリデンジアミン(ニテンピラム)、(E)‐N‐[(6‐クロロ‐3‐ピリジル)メチル]‐N'‐シアノ‐N‐メチルアセトアニジン(アセタミプリド)等のネオニコチノイド系殺虫剤;S−メチル−N−[(メチルカルバモイル)オキシ]チオアセトイミデート(メソミル)、2−セコンダリーブチルフェニル−N−メチルカーバメート(BPMC)等のカーバメイト系殺虫剤、及び(E)−4,5−ジヒドロ−6−メチル−4−(3−ピリジルメチレンアミノ)−1,2,4−トリアジン−3(2H)−オン(ピメトロジン)が挙げられる。
農薬殺菌活性成分としては、例えば、3−アリルオキシ−1,2−ベンゾイソチアゾール−1,1−ジオキシド(プロベナゾール)、1,2,5,6−テトラヒドロピロロ[3,2,1−ij]キノリン−4−オン(ピロキロン)、(E)−2−メトキシイミノ−N−メチル−2−(2−フェノキシフェニル)アセトアミド(メトミノストロピン)、5−メチル−1,2,4―トリアゾロ[3,4−b]ベンゾチアゾール(トリシクラゾール)、3'-クロロ−4,4'−ジメチル−1,2,3−チアジアゾール−5−カルボキサニリド(チアジニル)、[5−アミノ−2−メチル−6−(2,3,4,5,6−ペンタヒドロキシシクロヘキシロキシ)テトラヒドロピラン−3−イル]アミノ−α−イミノ酢酸(一般名:カスガマイシン)等が挙げられる。本発明に於いてはこれらの中でも、ネライストキシン系農薬活性成分の溶出制御型農薬粒剤の調製に好適である。またはネオニコチノイド系農薬活性成分の溶出制御型農薬粒剤を調製する目的にも好適である。農薬活性成分としてより好ましくはチオシクラムシュウ酸塩、並びにイミダクロプリド、またはチアメトキサムである。本発明の農薬粒剤にはこれらの農薬活性成分を単独又は2種以上を併用してもよい。
The agrochemical composition of the present invention, the agrochemical granule using the agrochemical composition, and the method for producing the agrochemical granule will be described in more detail below.
The pesticidal active ingredient (a) used in the pesticidal composition of the present invention may be any pesticidal active ingredient or pesticidal active ingredient, and is basically not limited. Among these, pesticidal active ingredients having high solubility in water are particularly suitable. Specifically, the water solubility at 20 ° C. is 100 ppm or more, and the water solubility is in the range of 0.01 to 50% by weight, and it can be suitably used for an agrochemical active ingredient having high water elution. Specific examples of the agrochemical active ingredient include, but are not limited to, the following.
Examples of the agrochemical insecticidal active ingredient include 1,3-dicarbamoylthio-2- (N, N-dimethylamino) -propane hydrochloride (cartap hydrochloride), 5-dimethylamino-1,2,3-trithianshu Nereistoxin insecticides such as acid salts (thiocyclam oxalate), S, S′-2-dimethylaminotrimethylene-di (benzenethiosulfonate) (bensultap); 1- (6-chloro-3 -Pyridylmethyl) -N-nitroimidazolidin-2-ylideneamine (imidacloprid), 3- (2-chloro-1,3-thiazol-5-ylmethyl) -5-methyl-1,3,5-oxadiazinan-4-ylidene ( Nitro) amine (thiamethoxam), (E) -1- (2-chloro-1,3-thiazol-5-ylmethyl) -3-methyl-2-nitrog Anidine (clothianidin), (RS) -1-methyl-2-nitro-3- (tetrahydro-3-furylmethyl) guanidine (dinotefuran), 3- (6-chloro-3-pyridylmethyl) -1,3-thiazolidine -2-Iridenecyanamide (thiacloprid), (E) -N- (6-Chloro-3-pyridylmethyl) -N-ethyl-N'-methyl-2-nitrovinylidenediamine (Nitenpyram), (E) -N -Neonicotinoid insecticides such as [(6-chloro-3-pyridyl) methyl] -N′-cyano-N-methylacetanidin (acetamipride); S-methyl-N-[(methylcarbamoyl) oxy] Carbamate insecticides such as thioacetimidate (mesomyl), 2-secondary butylphenyl-N-methyl carbamate (BPMC), and E)-4,5-dihydro-6-methyl-4- (3-pyridylmethylene amino) -1,2,4-triazine -3 (2H) - one (pymetrozine) and the like.
Examples of agricultural chemical bactericidal active ingredients include 3-allyloxy-1,2-benzisothiazole-1,1-dioxide (provenazole), 1,2,5,6-tetrahydropyrrolo [3,2,1-ij] quinoline. -4-one (pyroxylone), (E) -2-methoxyimino-N-methyl-2- (2-phenoxyphenyl) acetamide (methinostropine), 5-methyl-1,2,4-triazolo [3 4-b] benzothiazole (tricyclazole), 3′-chloro-4,4′-dimethyl-1,2,3-thiadiazole-5-carboxanilide (thiazinyl), [5-amino-2-methyl-6- (2 , 3,4,5,6-pentahydroxycyclohexyloxy) tetrahydropyran-3-yl] amino-α-iminoacetic acid (generic name: kasugamycin) It is. Among these, the present invention is suitable for preparing an elution-controlled pesticide granule for nereistoxin pesticide active ingredients. Or it is suitable also for the purpose of preparing the elution control type agricultural chemical granule of a neonicotinoid type agricultural chemical active ingredient. More preferred as the pesticidal active ingredient are thiocyclam oxalate, imidacloprid, and thiamethoxam. These agrochemical active ingredients may be used alone or in combination of two or more in the agrochemical granule of the present invention.

ネライストキシン系農薬活性成分、ネオニコチノイド系農薬活性成分以外にも、本発明の農薬組成物においては以下の農薬活性成分も、ネライストキシン系及びネオニコチノイド系農薬活性成分に対して化学的安定性の面で影響を与えない範囲であれば1種類以上併用することができる。具体的には、例えば次のようなものが挙げられるが、これに限定されるものではない。例えば殺虫活性成分としては、BPMC(2‐sec‐ブチルフェニル‐N‐メチルカーバメート)、MIPC(2‐イソプロピルフェニル‐N‐メチルカーバメート)、NAC(1‐ナフチル‐N‐メチルカーバメート)、ピラクロホス((RS)‐〔O‐1‐(4‐クロロフェニル)ピラゾール‐4‐イル〕‐O‐エチル‐S‐プロピル‐ホスホロチオエート)、ブプロフェジン(2‐tert‐ブチルイミノ‐3‐イソプロピル‐5‐フェニル‐3,4,5,6‐テトラヒドロ‐2H‐1,3,5‐チアジアジン‐4‐オン)、フルシトリネート((RS)‐α‐シアノ‐3‐フェノキシベンジル‐(S)‐2‐(4‐ジフルオロメトキシフェニル)‐3‐メチルブチラート)、メソミル(S‐メチル‐N‐〔(メチルカルバモイル)オキシ〕チオアセトイミデート)、エトフェンプロックス(2‐(4‐エトキシフェニル)‐2‐メチルプロピル‐3‐フェノキシベンジル−エーテル)、XMC(3,5‐キシリル‐N‐メチルカーバメート)などが挙げられる。
殺菌活性成分としては、IBP(O,O‐ジイソプロピル‐S‐ベンジルチオホスフェート)、トリシクラゾール(5‐メチル‐1,2,4−トリアゾロ〔3,4−b〕ベンゾチアゾール)、フサライド(4,5,6,7‐テトラクロロフタリド)、バリダマイシン、プロベナゾール(3‐アリルオキシ‐1,2‐ベンゾイソチアゾール‐1,1‐ジオキシド)、フェリムゾン((Z)‐2'‐メチルアセトフェノン=4,6‐ジメチルピリミジン‐2‐イルヒドラジン)、フルトラニル(α,α,α‐トリフルオロ‐3'‐イソプロポキシ‐O‐トルアニリド)、フラメトピル((RS)‐5‐クロロ‐N‐(1,3‐ジヒドロ‐1,1,3‐トリメチルイソベンゾフラン‐4‐イル)‐1,3‐ジメチルピラゾール‐4‐カルボキサミド、ペンシクロン(1‐(4‐クロロベンジル)‐1‐シクロペンチル‐3‐フェニル尿素、ジクロメジン(6‐(3,5‐ジクロロ‐4‐メチルフェニル)‐3(2H)‐ピリダジノン)、カスガマイシン一塩酸塩などが挙げられる。
In addition to the nereistoxin pesticide active ingredient and the neonicotinoid pesticide active ingredient, the following pesticide active ingredients are also chemically active against the nereistoxin and neonicotinoid pesticide active ingredients in the composition of the present invention. One or more types can be used in combination as long as they do not affect the stability of the product. Specific examples include the following, but are not limited thereto. For example, pesticidal active ingredients include BPMC (2-sec-butylphenyl-N-methylcarbamate), MIPC (2-isopropylphenyl-N-methylcarbamate), NAC (1-naphthyl-N-methylcarbamate), pyraclophos (( RS)-[O-1- (4-chlorophenyl) pyrazol-4-yl] -O-ethyl-S-propyl-phosphorothioate), buprofezin (2-tert-butylimino-3-isopropyl-5-phenyl-3,4 , 5,6-tetrahydro-2H-1,3,5-thiadiazin-4-one), flucitrinate ((RS) -α-cyano-3-phenoxybenzyl- (S) -2- (4-difluoromethoxy) Phenyl) -3-methylbutyrate), mesomil (S-methyl-N-[(methylcarbamoyl)) Xy] thioacetimidate), etofenprox (2- (4-ethoxyphenyl) -2-methylpropyl-3-phenoxybenzyl-ether), XMC (3,5-xylyl-N-methylcarbamate), etc. It is done.
Bactericidal active ingredients include IBP (O, O-diisopropyl-S-benzylthiophosphate), tricyclazole (5-methyl-1,2,4-triazolo [3,4-b] benzothiazole), and fusalide (4,5 , 6,7-tetrachlorophthalide), validamycin, probenazole (3-allyloxy-1,2-benzisothiazole-1,1-dioxide), ferimzone ((Z) -2′-methylacetophenone = 4,6- Dimethylpyrimidin-2-ylhydrazine), flutolanil (α, α, α-trifluoro-3'-isopropoxy-O-toluanilide), furametopyl ((RS) -5-chloro-N- (1,3-dihydro-) 1,1,3-trimethylisobenzofuran-4-yl) -1,3-dimethylpyrazole-4-carboxamide, pe Cyclone (1- (4-chlorobenzyl) -1-cyclopentyl-3-phenylurea, dichromedin (6- (3,5-dichloro-4-methylphenyl) -3 (2H) -pyridazinone), kasugamycin monohydrochloride, etc. Is mentioned.

本発明の農薬組成物中の農薬活性成分(a)の含有割合は、通常3〜25質量%、好ましくは4〜15質量%である。農薬組成物中の含有量が3質量%に満たない場合は農薬活性成分の十分な効力発現が期待できず、25質量%を超えると農薬活性成分の水中への溶出が十分に制御し得ないために長期の残効を期待できない。   The content ratio of the pesticidal active ingredient (a) in the pesticidal composition of the present invention is usually 3 to 25% by mass, preferably 4 to 15% by mass. When the content in the agrochemical composition is less than 3% by mass, sufficient efficacy of the agrochemical active ingredient cannot be expected, and when it exceeds 25% by mass, the elution of the agrochemical active ingredient into water cannot be controlled sufficiently. Therefore, long-term aftereffects cannot be expected.

本発明の農薬組成物は脂肪酸及び/又は脂肪酸誘導体(b)が製剤基材の一つとして適用される。当該脂肪酸及び脂肪酸誘導体は加工性に優れており、溶融等の加熱工程を経なくても、混合及び押出造粒によって均一で所望の粒径及び粒長の粒剤に調製することができる。そのため脂肪酸及び/又は脂肪酸誘導体と農薬活性成分、その他原材料を加熱溶融する工程を経ることなく農薬粒剤を製造することができ、熱に不安定な農薬活性成分にも適用できる。本発明に使用できる脂肪酸及び脂肪酸誘導体は、農薬活性成分しても不活性であれば特に限定されずに使用することができる。
本発明に好適な脂肪酸及び脂肪酸誘導体は、C8〜C40アルキル鎖カルボン酸及びその誘導体である。より好ましくは、C10〜C30アルキル鎖カルボン酸及びその誘導体である。これらの脂肪酸及び脂肪酸誘導体は、総じて常温固体のものであり、農薬活性成分を含浸保持する粒剤基材として適用できるものである。粒剤調製における加工性を勘案すると、当該脂肪酸及び脂肪酸誘導体の融点が45〜100℃の範囲の物性のものが特に好適に使用され得る。より好ましくは、融点が50〜90℃の範囲の脂肪酸及び脂肪酸誘導体が優れた物性の粒剤を調製し得る。
脂肪酸としては例えばステアリン酸、ミリスチン酸、ベヘン酸、パルミチン酸、ラウリン酸といったものが挙げられる。脂肪酸誘導体としては例えば12−ヒドロキシステアリン酸といったものが挙げられる。さらに、牛硬化油、ヒマシ硬化油、大豆硬化油、パーム硬化油、菜種硬化油といった動物性油脂若しくは植物性油脂等の脂肪酸エステルを水素添加して得られたワックス状物質なども含まれる。上記の中から選ばれる1種または2種以上の混合物で、これらは任意に組み合わせて使用することができる。これら脂肪酸及び脂肪酸誘導体の中でも、ヒマシ硬化油単独、及び牛硬化油とステアリン酸の組合せ、及びヒマシ硬化油とステアリン酸の組合せが、農薬活性成分の良好な溶出性を示すことから好ましい。更にヒマシ油、菜種油、パーム油、大豆油、綿実油、亜麻仁油等の常温液体の植物性油脂を適宜添加することで、造粒性を向上させることができる。
脂肪酸及び/又は脂肪酸誘導体は本発明の農薬粒剤中に10〜80質量%の割合で含有させることができる。好ましくは20〜70質量%である。10質量%未満では脂肪酸及び脂肪酸誘導体による溶出制御効果が期待できず、また農薬粒剤の形状に成形することが困難となる。また、80質量%を超えると農薬活性成分が十分に水中に溶出されず、粒剤中に残留するため十分な効果が発揮できない可能性がある。本発明に係る農薬粒剤において、脂肪酸及び/又は脂肪酸誘導体の含量を多くすると薬剤溶出速度が遅く制御された粒剤を調製できる。逆に脂肪酸及び/又は脂肪酸誘導体の含量を少なくすると、早い薬剤溶出パターンを示す粒剤を調製できる。
In the agrochemical composition of the present invention, fatty acid and / or fatty acid derivative (b) is applied as one of the preparation bases. The fatty acids and fatty acid derivatives are excellent in processability, and can be prepared into granules having a desired particle size and length by mixing and extrusion granulation without passing through a heating step such as melting. Therefore, the agrochemical granule can be produced without going through the step of heating and melting the fatty acid and / or fatty acid derivative and the agrochemical active ingredient and other raw materials, and can be applied to the agrochemical active ingredient which is unstable to heat. The fatty acid and fatty acid derivative that can be used in the present invention can be used without particular limitation as long as they are inactive even if they are active as an agrochemical active ingredient.
Fatty acids and fatty acid derivatives suitable for the present invention are C8-C40 alkyl chain carboxylic acids and derivatives thereof. More preferred are C10-C30 alkyl chain carboxylic acids and derivatives thereof. These fatty acids and fatty acid derivatives are generally solid at room temperature and can be applied as a granule base material impregnated and held with an agrochemical active ingredient. Considering the processability in the preparation of granules, those having physical properties in which the melting point of the fatty acid and fatty acid derivative is in the range of 45 to 100 ° C. can be used particularly suitably. More preferably, it is possible to prepare granules having excellent physical properties of fatty acids and fatty acid derivatives having a melting point in the range of 50 to 90 ° C.
Examples of fatty acids include stearic acid, myristic acid, behenic acid, palmitic acid, and lauric acid. Examples of fatty acid derivatives include 12-hydroxystearic acid. Furthermore, wax-like substances obtained by hydrogenating fatty acid esters such as animal fats and vegetable oils such as cow oil, castor oil, soybean oil, palm oil, and rapeseed oil are also included. One or a mixture of two or more selected from the above can be used in any combination. Among these fatty acids and fatty acid derivatives, castor hydrogenated oil alone, a combination of beef hydrogenated oil and stearic acid, and a combination of castor hydrogenated oil and stearic acid are preferable because they exhibit good dissolution properties of the agrochemical active ingredient. Furthermore, granulation property can be improved by adding room temperature liquid vegetable oils such as castor oil, rapeseed oil, palm oil, soybean oil, cottonseed oil and linseed oil as appropriate.
The fatty acid and / or fatty acid derivative can be contained in the agrochemical granule of the present invention in a proportion of 10 to 80% by mass. Preferably it is 20-70 mass%. If it is less than 10 mass%, the elution control effect by a fatty acid and a fatty acid derivative cannot be expected, and it becomes difficult to form the shape of an agrochemical granule. On the other hand, if it exceeds 80% by mass, the pesticidal active ingredient is not sufficiently dissolved in water and remains in the granule, so that there is a possibility that sufficient effects cannot be exhibited. In the agrochemical granule according to the present invention, when the content of fatty acid and / or fatty acid derivative is increased, a granule in which the drug elution rate is controlled slowly can be prepared. On the contrary, if the content of fatty acid and / or fatty acid derivative is decreased, a granule showing a fast drug elution pattern can be prepared.

本願に係る発明は、脂肪酸及び/又は脂肪酸誘導体を製剤基材としながらも、加熱溶融工程を経ずに、十分な硬度を保った粒剤を製造見出すことを課題として鋭意検討を実施した結果、農薬活性成分と脂肪酸及び/又は脂肪酸誘導体に水難溶性多糖類(c)を添加し、よく混合したものが、押出造粒機で造粒でき農薬粒剤として望ましい物性と示すことを見出した。脂肪酸及び/又は脂肪酸誘導体に水難溶性多糖類を加えることで、圧縮成形性を付与して溶融混合工程を経ることなく、押出造粒による圧縮のみで十分な硬度を持った粒剤を得られた。また水難溶性多糖類は、脂肪酸及び/又は脂肪酸誘導体を基材とする当該農薬粒剤中でネットワークを形成して粒の硬度を高めると同時に、粒内部から農薬活性成分の水中への溶出を調整する働きがある。
本発明の農薬組成物に適用される水難溶性多糖類(c)としては、押出造粒による造粒性を向上し得るもので、当該農薬粒剤中の農薬活性成分の安定性を損なうものでなければこれに限るものではないが、具体的には結晶セルロース、水不溶性ペクチン、及びキチン・キトサン等が挙げられる。水難溶性多糖類の平均粒子径は1μm〜45μmのものが本願農薬組成物において好適であり、望ましい特性の薬剤溶出制御型粒剤を得るために必須である。好ましくは平均粒径1μm〜30μmであり、より好ましくは平均粒径5μm〜20μmである。通常、水難溶性多糖類の含有量が多くなるにつれて農薬活性成分の水中溶出速度は速くなる。当該農薬粒剤には水難溶性多糖類を0.5〜20質量%用いることで十分な硬度を与えることができる。0.5質量%未満では水難溶性多糖類による圧縮形成性と硬度を与えることができない。また、20質量%を超えると農薬粒剤としての形状に成形することが難しくなる。
The invention according to the present application is the result of carrying out diligent studies with the object of producing and finding a granule having sufficient hardness without going through a heating and melting step, while using a fatty acid and / or a fatty acid derivative as a preparation base, It was found that a poorly water-soluble polysaccharide (c) added to an agrochemical active ingredient and a fatty acid and / or a fatty acid derivative and mixed well can be granulated with an extrusion granulator and exhibited desirable physical properties as an agrochemical granule. By adding a poorly water-soluble polysaccharide to a fatty acid and / or fatty acid derivative, a granule having sufficient hardness was obtained only by compression by extrusion granulation without giving a compression moldability and passing through a melt mixing step. . In addition, poorly water-soluble polysaccharides form a network in the agricultural chemical granules based on fatty acids and / or fatty acid derivatives to increase the hardness of the grains, and at the same time, adjust the elution of agricultural chemical active ingredients from the inside of the grains into water. There is work to do.
The poorly water-soluble polysaccharide (c) applied to the agrochemical composition of the present invention can improve the granulation properties by extrusion granulation, and impairs the stability of the agrochemical active ingredient in the agrochemical granule. Specific examples include crystalline cellulose, water-insoluble pectin, and chitin / chitosan. A poorly water-soluble polysaccharide having an average particle size of 1 μm to 45 μm is suitable for the agricultural chemical composition of the present application, and is essential for obtaining a drug elution control type granule having desirable characteristics. The average particle size is preferably 1 μm to 30 μm, and more preferably the average particle size is 5 μm to 20 μm. Usually, as the content of the poorly water-soluble polysaccharide increases, the dissolution rate of the agrochemical active ingredient in water increases. Sufficient hardness can be given to the said agrochemical granule by using 0.5-20 mass% of poorly water-soluble polysaccharides. If it is less than 0.5% by mass, the compression-forming property and hardness due to the poorly water-soluble polysaccharide cannot be provided. Moreover, when it exceeds 20 mass%, it will become difficult to shape | mold into the shape as an agrochemical granule.

本発明の農薬組成物は無機物質(d)を含有する。当該農薬組成物は、比重が1に近い脂肪酸及び/又は脂肪酸誘導体が基材であり、その比重と基材由来の撥水性によって湛水圃場に散布すると水面に浮上する。浮上した粒は風の影響を受けて圃場の一部に局在化して効力が不均一になるだけでなく、水流の影響を受けて圃場から流亡し、期待される効力を発揮できないおそれがある。比重の軽さによる効力低下を防ぐために、当該農薬組成物は無機物質を含んでいる。本発明に係る農薬粒剤を湛水圃場に散布した際、無機物質の比重の大きさによって当該農薬粒剤の比重を大きく調整することが可能で、水中沈降性を改善し速やかに水中に沈降する機能を付与させるものである。また、無機物質は当該農薬粒剤の内部の構造を粗くすることで、粒内部に存在する農薬活性成分の水中への溶出を適宜調整する役割をも有する。
本発明に用いられる無機物質はクレー、珪石、タルク、白土、珪藻土、アッシュメント、非晶質二酸化珪素(通称:ホワイトカーボン)、硫酸バリウム、二酸化チタン、塩化ナトリウム、塩化カリウム、二水石膏、半水石膏などから選ばれる1種または2種以上の組合せで用いられるが、農薬活性成分の安定性を損なうものでなければこれに限るものではない。無機物質の粒径は様々なものが使用できるが、その中でも20μm〜200μmのものが製造上及び/又は農薬活性成分の溶出を促す作用を導き出すのに好ましい。
当該無機物質は、本発明の農薬粒剤中に10〜60質量%の割合で含有させることができる。より好ましくは20〜50重量%を含有するものである。10質量%未満では比重調整の効果が期待できず、60質量%を超えると農薬活性成分の溶出制御が困難となるばかりでなく、農薬粒剤としての形状に成形することが難しくなる。
The agrochemical composition of the present invention contains an inorganic substance (d). The pesticide composition has a base material of a fatty acid and / or a fatty acid derivative having a specific gravity close to 1, and floats on the water surface when sprayed on a flooded field due to the specific gravity and water repellency derived from the base material. The floating particles are not only localized in a part of the field under the influence of the wind and become non-uniform in effectiveness, but also run away from the field under the influence of the water flow and may not exhibit the expected effect. . In order to prevent a decrease in efficacy due to light specific gravity, the agrochemical composition contains an inorganic substance. When the agrochemical granule according to the present invention is sprayed on a flooded field, it is possible to greatly adjust the specific gravity of the agrochemical granule by the magnitude of the specific gravity of the inorganic substance, improving the sedimentation property in water and promptly submerging in water. The function to perform is given. In addition, the inorganic substance also has a role of appropriately adjusting the elution of the pesticidal active ingredient existing in the grain into water by roughening the internal structure of the pesticidal granule.
The inorganic substance used in the present invention is clay, silica, talc, white clay, diatomaceous earth, ashment, amorphous silicon dioxide (common name: white carbon), barium sulfate, titanium dioxide, sodium chloride, potassium chloride, dihydrate gypsum, semi-solid Although it is used by 1 type, or 2 or more types of combinations chosen from a water gypsum etc., if it does not impair the stability of an agrochemical active ingredient, it will not restrict to this. Various inorganic particle diameters can be used. Among them, those having a particle size of 20 μm to 200 μm are preferable for deriving the effect of promoting the elution of the agrochemical active ingredient in production and / or agricultural chemicals.
The said inorganic substance can be contained in the ratio of 10-60 mass% in the agrochemical granule of this invention. More preferably, it contains 20 to 50% by weight. If it is less than 10% by mass, the effect of adjusting the specific gravity cannot be expected. If it exceeds 60% by mass, it becomes difficult not only to control the elution of the pesticidal active ingredient but also to form it into a shape as an agrochemical granule.

本発明の農薬組成物は界面活性剤(e)を含有することが好ましい。当該界面活性剤はノニオン性及び/又はアニオン性界面活性剤が適用される。アニオン性界面活性剤及び/又はノニオン性界面活性剤は、湛水圃場に本発明に係る農薬粒剤を散布した際、その水親和性によって本発明の農薬粒剤の撥水性を抑えて、水中沈降性を改善し速やかに水中に沈降する機能を付与させるものである。また、本発明に用いられる界面活性剤は、当該農薬粒剤の親水性を高めて、粒内部に存在する農薬活性成分の水中への溶出を適宜調整する役割をも有する。
本発明に用いられるノニオン性界面活性剤としてはポリオキシエチレンアルキルエーテル、ポリオキシエチレンスチリルフェニルエーテル、ポリオキシエチレンアルキルエステル、ポリオキシエチレンフェニルエーテルポリマー、ポリオキシエチレンアルキレンアリールフェニルエーテル、ポリオキシエチレンポリオキシプロピレンブロックポリマー、ポリオキシエチレン化ヒマシ油、ポリオキシエチレン化硬化ヒマシ油、グリセリルモノステアレート、グリセリルジステアレート、ポリオキシエチレンソルビタンモノオレエートなどが挙げられ、アニオン性界面活性剤としてはポリオキシエチレンスチリルフェニルエーテルサルフェート、リグニンスルホン酸塩、アルキルアリールスルホン酸塩、アルキルナフタレンスルホン酸塩等のアニオン性界面活性剤が挙げられるが、農薬活性成分の安定性を損なうものでなければこれに限るものではない。これらノニオン性及びアニオン性界面活性剤の群より選ばれる1種又は2種以上の組合せによって、水中沈降性効果を発揮することができる。
当該界面活性剤がその効果を発揮する使用の形態は、農薬活性成分やその他原材料と共に混合して押出造粒して農薬粒剤に形成してもよいし、農薬活性成分やその他原材料を混合、押出造粒してできた農薬粒剤の粒表面に水中沈降性付与剤を均一にコーティングすることも可能である。また、その両方を併用することも可能である。
当該界面活性剤は本発明の農薬粒剤中に0.1〜30質量%の割合で含有させることができる。より好ましくは0.1%〜10質量%である。0.1質量%未満では当該農薬粒剤を水中に沈降させるために十分な機能を発揮するには足りず、30質量%を超えると良好な水中沈降性は得られるものの、界面活性剤によって農薬活性成分の水中溶出速度が大幅に促進されるため、溶出制御が困難になる。
The agrochemical composition of the present invention preferably contains a surfactant (e). As the surfactant, a nonionic and / or anionic surfactant is applied. When an anionic surfactant and / or a nonionic surfactant is sprayed with an agrochemical granule according to the present invention in a flooded field, the water repellency of the agrochemical granule of the present invention is suppressed due to its water affinity. It improves the sedimentation property and imparts a function to quickly settle in water. The surfactant used in the present invention also has a role of increasing the hydrophilicity of the agrochemical granule and appropriately adjusting the elution of the agrochemical active ingredient present in the grain into water.
Nonionic surfactants used in the present invention include polyoxyethylene alkyl ether, polyoxyethylene styryl phenyl ether, polyoxyethylene alkyl ester, polyoxyethylene phenyl ether polymer, polyoxyethylene alkylene aryl phenyl ether, polyoxyethylene poly Examples include an oxypropylene block polymer, polyoxyethylenated castor oil, polyoxyethylenated hydrogenated castor oil, glyceryl monostearate, glyceryl distearate, and polyoxyethylene sorbitan monooleate. Animates such as oxyethylene styryl phenyl ether sulfate, lignin sulfonate, alkyl aryl sulfonate, alkyl naphthalene sulfonate, etc. Emissions surfactants including but not limited to this as long as they do not impair the stability of the agrochemical active ingredient. By one or a combination of two or more selected from the group of these nonionic and anionic surfactants, an underwater sedimentation effect can be exhibited.
The form of use in which the surfactant exerts its effect may be formed by mixing with an agrochemical active ingredient and other raw materials and extrusion granulation to form an agrochemical granule, or mixing an agrochemical active ingredient and other raw materials, It is also possible to uniformly coat an underwater sedimentation-imparting agent on the surface of the agrochemical granules produced by extrusion granulation. Moreover, it is also possible to use both together.
The said surfactant can be contained in the ratio of 0.1-30 mass% in the agrochemical granule of this invention. More preferably, it is 0.1% to 10% by mass. If it is less than 0.1% by mass, it is not sufficient to exhibit a sufficient function for precipitating the agricultural chemical granules in water, and if it exceeds 30% by mass, good subsidence in water can be obtained. Since the elution rate of the active ingredient in water is greatly accelerated, elution control becomes difficult.

本発明の水難溶性多糖類、無機物質、及び場合によって添加される界面活性剤は、当該農薬粒剤に良好な水中沈降性を付与すると共に、農薬活性成分の水中溶出速度を調整する役割をも果たしている。水難溶性多糖類、無機物質、及び界面活性剤の種類、含有量、及びこれらの組合せ組成を適宜調整することで、粒剤への良好な成形性を保ち、かつ良好な水中沈降性を保ちつつ所望の水中溶出速度を有する農薬粒剤を得ることができる。通常、本発明の農薬粒剤は農薬活性成分を3〜25質量%、脂肪酸及び/又は脂肪酸誘導体を10〜80質量%、水難溶性多糖類を0.5〜20質量%、無機物質を10〜60質量%を含有し、この範囲内で適宜調整することで所望の水中溶出速度を得ることができる。加えて、当該農薬粒剤には界面活性剤を0.1〜10質量%の割合で含有することができ、当該農薬粒剤の水中沈降性ならびに農薬活性成分の水中溶出速度を適宜調整することができる。界面活性剤は、農薬活性成分、脂肪酸及び/又は脂肪酸誘導体、水難溶性多糖類及び無機物質、及び場合によって界面活性剤の添加で構成される農薬組成物を造粒してなる農薬粒剤の、粒表面にコーティングすることが可能であるし、本発明の農薬組成物中に予め含有させて造粒することも可能である。場合によっては、更に粒表面にコーティングすることも可能である。
2種以上の農薬活性成分を本発明の農薬粒剤に含有させる場合には、農薬活性成分の種類によっては農薬活性成分が脂肪酸及び/又は脂肪酸誘導体の内部構造を粗くする作用が生じる場合があり、この場合、農薬活性成分が水中溶出を調整する効果を発揮する。そのため所望の溶出制御を発現させるには、用いる農薬活性成分の物性や固形粒子径、及びその含有量を、その溶出速度に応じて適宜調整することが好ましい。
The poorly water-soluble polysaccharides, inorganic substances, and surfactants added in some cases according to the present invention have a role of adjusting the dissolution rate of agrochemical active ingredients in water while imparting good underwater sedimentation to the agrochemical granules. Plays. By appropriately adjusting the kind, content, and combination composition of poorly water-soluble polysaccharides, inorganic substances, and surfactants, while maintaining good moldability to granules and maintaining good sedimentation in water Agrochemical granules having a desired dissolution rate in water can be obtained. Usually, the agrochemical granule of the present invention comprises 3 to 25% by mass of an agrochemical active ingredient, 10 to 80% by mass of a fatty acid and / or a fatty acid derivative, 0.5 to 20% by mass of a poorly water-soluble polysaccharide, and 10 to 10% of an inorganic substance. It contains 60% by mass, and a desired dissolution rate in water can be obtained by appropriately adjusting within this range. In addition, the pesticide granule may contain a surfactant in a proportion of 0.1 to 10% by mass, and the water sedimentation rate of the pesticide granule and the elution rate of the pesticide active ingredient in water should be adjusted as appropriate. Can do. The surfactant is an agrochemical granule formed by granulating an agrochemical composition composed of an agrochemical active ingredient, a fatty acid and / or a fatty acid derivative, a poorly water-soluble polysaccharide and an inorganic substance, and optionally a surfactant. It can be coated on the surface of the grains, or it can be granulated by previously containing it in the agrochemical composition of the present invention. In some cases, it is also possible to coat the grain surface.
When two or more kinds of pesticidal active ingredients are contained in the pesticidal granules of the present invention, the pesticidal active ingredient may act to roughen the internal structure of the fatty acid and / or fatty acid derivative depending on the type of the pesticidal active ingredient. In this case, the pesticidal active ingredient exerts the effect of adjusting elution in water. Therefore, in order to express desired elution control, it is preferable to appropriately adjust the physical properties, solid particle diameter, and content of the pesticidal active ingredient used according to the elution rate.

本発明の農薬粒剤の製造方法は以下の2通りがある。
1)農薬活性成分、脂肪酸及び/又は脂肪酸誘導体、無機物質、水難溶性多糖類をよく混合した後に造粒機に投入して造粒する方法。場合により、更に得られた粒剤表面に界面活性剤をコーティングする方法。
2)農薬活性成分、脂肪酸及び/又は脂肪酸誘導体、無機物質、水難溶性多糖類、界面活性剤をよく混合した後に造粒機に投入して造粒する方法。場合によって、得られた粒剤表面に、更に界面活性剤をコーティングする方法。
本発明の農薬組成物を造粒する際、その粒径は2〜10mmであることが好ましい。2mm未満では造粒の際に当該農薬組成物にかかる圧力が足りず、粒剤としての形に成形することが困難となる。また、水田に散布する際に風などの影響を受けて当該農薬粒剤が狙う水田以外の畦畔等に落下するおそれがある。10mmを超える場合も造粒が難しくなるばかりか、単位面積当たりの散布粒数が少なくなり散布ムラや効力が不均一化する等の問題が起きるおそれがある。
There are the following two methods for producing the agrochemical granule of the present invention.
1) A method in which an agrochemical active ingredient, a fatty acid and / or a fatty acid derivative, an inorganic substance, and a poorly water-soluble polysaccharide are mixed well and then put into a granulator for granulation. Optionally, a method of coating the surface of the obtained granule with a surfactant.
2) A method in which an agrochemical active ingredient, a fatty acid and / or a fatty acid derivative, an inorganic substance, a poorly water-soluble polysaccharide, and a surfactant are mixed well and then put into a granulator for granulation. In some cases, the surface of the obtained granule is further coated with a surfactant.
When granulating the agricultural chemical composition of the present invention, the particle size is preferably 2 to 10 mm. If it is less than 2 mm, the pressure applied to the agrochemical composition is insufficient at the time of granulation, and it becomes difficult to form it into a form as a granule. Moreover, when spraying on a paddy field, there exists a possibility that it may fall to the shore etc. other than the paddy field which the said agrochemical granule aims at under the influence of a wind. When it exceeds 10 mm, not only granulation becomes difficult, but the number of sprayed particles per unit area decreases, and there may be problems such as uneven spraying and non-uniform effects.

本発明の農薬粒剤の製造に用いられる押出造粒機は縦型押出造粒機が好ましく、原材料をよく混合した後に当該造粒機に投入して造粒する。このとき、ダイスの厚さが10mm以上、粒径が2〜10mmであることが粒剤を製造する上で重要になる。ダイスの厚さが10mmに満たない場合、原材料にかかる圧力が足りず粒剤としての形に成形することが困難となる。また、粒径が2〜10mmの範囲外の場合、やはり原材料にかかる圧力が足りず粒剤として成形することが難しくなる。縦型押出造粒機は、一般に被造粒組成物に圧力をかけて水平に設置されたダイスから押出して造粒する機器の一般名称で、ディスクペレッター(不二パウダル社製)等が挙げられる。
上記の方法で得られた粒剤の界面活性剤コーティングにはコンクリートミキサーやコーティングパンなどが用いられる。ミキサーに上記の方法で得られた粒剤、界面活性剤の順に投入し、撹拌することで粒剤表面に均一に界面活性剤をコーティングすることができる。
The extrusion granulator used for production of the agrochemical granule of the present invention is preferably a vertical extrusion granulator, and the raw materials are mixed well and then put into the granulator for granulation. At this time, it is important to manufacture the granule that the die has a thickness of 10 mm or more and a particle size of 2 to 10 mm. When the thickness of the die is less than 10 mm, the pressure applied to the raw material is insufficient, and it becomes difficult to form into a shape as a granule. Moreover, when the particle size is outside the range of 2 to 10 mm, the pressure applied to the raw materials is still insufficient, and it becomes difficult to form the granules. A vertical extrusion granulator is a general name for a device that is generally granulated by extruding from a horizontally installed die by applying pressure to the composition to be granulated, and includes a disk pelleter (manufactured by Fuji Powder Co., Ltd.). It is done.
A concrete mixer, a coating pan, etc. are used for surfactant coating of the granule obtained by said method. The surfactant can be uniformly coated on the surface of the granule by adding the granule and the surfactant obtained by the above method to the mixer in this order and stirring.

以下に実施例により本発明を更に詳細に説明するが、本発明はこれにより何ら限定されるものではない。なお、農薬活性成分として供試したチオシクラムシュウ酸塩の純度は約89.9%のものを用いた。イミダクロプリド、ピメトロジン、チアメトキサムは何れも純度98%以上のものを供した。   The present invention will be described in more detail with reference to the following examples, but the present invention is not limited thereto. The purity of thiocyclam oxalate used as an agrochemical active ingredient was about 89.9%. All of imidacloprid, pymetrozine and thiamethoxam had a purity of 98% or more.

実施例1
チオシクラムシュウ酸塩11.5重量部、ステアリン酸15.8重量部、ヒマシ硬化油37.3重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)30重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)5.0重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、ペグノールST−9(商品名、東邦化学工業社製、POEアルキルエーテル、HLB:13.3)0.3重量部をコーティングし、チオシクラムシュウ酸塩10.3%粒剤を得た。
Example 1
11.5 parts by weight of thiocyclam oxalate, 15.8 parts by weight of stearic acid, 37.3 parts by weight of castor oil hardened, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle size: about 40 μm ) 30 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemical Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm) Product name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10 mm, particle size 4.0 mm), granulated and sieved with 2 mm (8.6 mesh) sieve Put into a concrete mixer, coat 0.3 parts by weight of Pegnol ST-9 (trade name, manufactured by Toho Chemical Industry Co., Ltd., POE alkyl ether, HLB: 13.3), and 10.3% granules of thiocyclam oxalate Got the agent .

実施例2
チオシクラムシュウ酸塩11.5重量部、ステアリン酸12.9重量部、ヒマシ硬化油30.2重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)40重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)5.0重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、ペグノールST−9(商品名、東邦化学工業社製、POEアルキルエーテル、HLB:13.3)0.3重量部をコーティングし、チオシクラムシュウ酸塩10.3%粒剤を得た。
Example 2
11.5 parts by weight of thiocyclam oxalate, 12.9 parts by weight of stearic acid, 30.2 parts by weight of castor oil, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle size: about 40 μm ) 40 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemicals Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm) Product name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10 mm, particle size 4.0 mm), granulated and sieved with 2 mm (8.6 mesh) sieve Put into a concrete mixer, coat 0.3 parts by weight of Pegnol ST-9 (trade name, manufactured by Toho Chemical Industry Co., Ltd., POE alkyl ether, HLB: 13.3), and 10.3% granules of thiocyclam oxalate Got the agent .

実施例3
チオシクラムシュウ酸塩11.5重量部、ステアリン酸9.9重量部、ヒマシ硬化油23.2重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)50重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)5.0重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、ペグノールST−9(商品名、東邦化学工業社製、POEアルキルエーテル、HLB:13.3)0.3重量部をコーティングし、チオシクラムシュウ酸塩10.3%粒剤を得た。
Example 3
11.5 parts by weight of thiocyclam oxalate, 9.9 parts by weight of stearic acid, 23.2 parts by weight of castor hardened oil, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle size: about 40 μm ) 50 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemical Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm) Product name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10 mm, particle size 4.0 mm), granulated and sieved with 2 mm (8.6 mesh) sieve Put into a concrete mixer, coat 0.3 parts by weight of Pegnol ST-9 (trade name, manufactured by Toho Chemical Industry Co., Ltd., POE alkyl ether, HLB: 13.3), and 10.3% granules of thiocyclam oxalate An agent was obtained.

実施例4
チオシクラムシュウ酸塩11.5重量部、ステアリン酸19.2重量部、ヒマシ硬化油36.4重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)30重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)2.5重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、ペグノールST−9(商品名、東邦化学工業社製、POEアルキルエーテル、HLB:13.3)0.3重量部をコーティングし、チオシクラムシュウ酸塩10.3%粒剤を得た。
Example 4
11.5 parts by weight of thiocyclam oxalate, 19.2 parts by weight of stearic acid, 36.4 parts by weight of castor hydrogenated oil, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle diameter: about 40 μm ) 30 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemicals Co., Ltd., finely divided crystalline cellulose, average particle diameter: 10 μm) 2.5 parts by weight well mixed with a disk pelleter ( Product name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10 mm, particle size 4.0 mm), granulated and sieved with 2 mm (8.6 mesh) sieve Put into a concrete mixer, coat 0.3 parts by weight of Pegnol ST-9 (trade name, manufactured by Toho Chemical Industry Co., Ltd., POE alkyl ether, HLB: 13.3), and 10.3% granules of thiocyclam oxalate Got the agent .

実施例5
チオシクラムシュウ酸塩11.5重量部、ステアリン酸15.7重量部、ヒマシ硬化油29.9重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)40重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)2.5重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、ペグノールST−9(商品名、東邦化学工業社製、POEアルキルエーテル、HLB:13.3)0.3重量部をコーティングし、チオシクラムシュウ酸塩10.3%粒剤を得た。
Example 5
11.5 parts by weight of thiocyclam oxalate, 15.7 parts by weight of stearic acid, 29.9 parts by weight of castor oil, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle diameter: about 40 μm ) 40 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemicals Co., Ltd., finely divided crystalline cellulose, average particle diameter: 10 μm) 2.5 parts by weight well mixed with a disk pelleter ( Product name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10 mm, particle size 4.0 mm), granulated and sieved with 2 mm (8.6 mesh) sieve Put into a concrete mixer, coat 0.3 parts by weight of Pegnol ST-9 (trade name, manufactured by Toho Chemical Industry Co., Ltd., POE alkyl ether, HLB: 13.3), and 10.3% granules of thiocyclam oxalate Got the agent .

実施例6
チオシクラムシュウ酸塩11.5重量部、ステアリン酸19.7重量部、ヒマシ硬化油37.4重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)30重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)1.0重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、ペグノールST−9(商品名、東邦化学工業社製、POEアルキルエーテル、HLB:13.3)0.3重量部をコーティングし、チオシクラムシュウ酸塩10.3%粒剤を得た。
Example 6
11.5 parts by weight of thiocyclam oxalate, 19.7 parts by weight of stearic acid, 37.4 parts by weight of castor hydrogenated oil, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle size: about 40 μm ) 30 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemicals Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm) well mixed with 1.0 part by weight is a disk pelleter ( Product name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10 mm, particle size 4.0 mm), granulated and sieved with 2 mm (8.6 mesh) sieve Put into a concrete mixer, coat 0.3 parts by weight of Pegnol ST-9 (trade name, manufactured by Toho Chemical Industry Co., Ltd., POE alkyl ether, HLB: 13.3), and 10.3% granules of thiocyclam oxalate Got the agent .

実施例7
チオシクラムシュウ酸塩11.5重量部、ステアリン酸16.2重量部、ヒマシ硬化油30.9重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)40重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)1.0重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、ペグノールST−9(商品名、東邦化学工業社製、POEアルキルエーテル、HLB:13.3)0.3重量部をコーティングし、チオシクラムシュウ酸塩10.3%粒剤を得た。
Example 7
11.5 parts by weight of thiocyclam oxalate, 16.2 parts by weight of stearic acid, 30.9 parts by weight of castor oil, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle size: about 40 μm ) 40 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemicals Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm) Product name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10 mm, particle size 4.0 mm), granulated and sieved with 2 mm (8.6 mesh) sieve Put into a concrete mixer, coat 0.3 parts by weight of Pegnol ST-9 (trade name, manufactured by Toho Chemical Industry Co., Ltd., POE alkyl ether, HLB: 13.3), and 10.3% granules of thiocyclam oxalate Got the agent .

実施例8
チオシクラムシュウ酸塩11.5重量部、ステアリン酸19.2重量部、ヒマシ硬化油36.4重量部、セイコーライト(商品名、セイコー産業社製、珪藻土)30重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)2.5重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、ペグノールST−9(商品名、東邦化学工業社製、POEアルキルエーテル、HLB:13.3)0.3重量部をコーティングし、チオシクラムシュウ酸塩10.3%粒剤を得た。
Example 8
11.5 parts by weight of thiocyclam oxalate, 19.2 parts by weight stearic acid, 36.4 parts by weight castor oil, 30 parts by weight Seikolite (trade name, manufactured by Seiko Sangyo Co., Ltd., diatomaceous earth), 0. 35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemical Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm) well mixed with a disk pelleter (trade name, manufactured by Fuji Powder Co., Ltd.) Put into a vertical extrusion granulator, die thickness 10mm, particle size 4.0mm), granulate, and sieved with 2mm (8.6 mesh) sieve, put into concrete mixer, Pegnol ST- 9 (trade name, manufactured by Toho Chemical Industry Co., Ltd., POE alkyl ether, HLB: 13.3) 0.3 parts by weight was coated to obtain 10.3% thiocyclam oxalate granules.

実施例9
チオシクラムシュウ酸塩11.5重量部、ステアリン酸12.3重量部、ヒマシ硬化油23.3重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)50重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)2.5重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、ペグノールST−9(商品名、東邦化学工業社製、POEアルキルエーテル、HLB:13.3)0.3重量部をコーティングし、チオシクラムシュウ酸塩10.3%粒剤を得た。
Example 9
11.5 parts by weight of thiocyclam oxalate, 12.3 parts by weight of stearic acid, 23.3 parts by weight of castor oil, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle size: about 40 μm ) 50 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemicals Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm) well mixed with 2.5 parts by weight is a disk pelleter ( Product name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10 mm, particle size 4.0 mm), granulated and sieved with 2 mm (8.6 mesh) sieve Put into a concrete mixer, coat 0.3 parts by weight of Pegnol ST-9 (trade name, manufactured by Toho Chemical Industry Co., Ltd., POE alkyl ether, HLB: 13.3), and 10.3% granules of thiocyclam oxalate Got the agent .

実施例10
チオシクラムシュウ酸塩11.5重量部、ステアリン酸19.2重量部、ヒマシ硬化油36.4重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)30重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)2.5重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別してチオシクラムシュウ酸塩10.3%粒剤を得た。
Example 10
11.5 parts by weight of thiocyclam oxalate, 19.2 parts by weight of stearic acid, 36.4 parts by weight of castor hydrogenated oil, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle diameter: about 40 μm ) 30 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemicals Co., Ltd., finely divided crystalline cellulose, average particle diameter: 10 μm) 2.5 parts by weight well mixed with a disk pelleter ( Product name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10mm, particle size 4.0mm), granulated, sieved with 2mm (8.6 mesh) sieve, thiocyclam Oxalate 10.3% granules were obtained.

実施例11
チオシクラムシュウ酸塩11.5重量部、ステアリン酸15.7重量部、ヒマシ硬化油29.9重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)40重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)2.5重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別してチオシクラムシュウ酸塩10.3%粒剤を得た。
Example 11
11.5 parts by weight of thiocyclam oxalate, 15.7 parts by weight of stearic acid, 29.9 parts by weight of castor oil, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle diameter: about 40 μm ) 40 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemicals Co., Ltd., finely divided crystalline cellulose, average particle diameter: 10 μm) 2.5 parts by weight well mixed with a disk pelleter ( Product name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10mm, particle size 4.0mm), granulated, sieved with 2mm (8.6 mesh) sieve, thiocyclam Oxalate 10.3% granules were obtained.

実施例12
チオシクラムシュウ酸塩11.5重量部、ステアリン酸12.3重量部、ヒマシ硬化油23.3重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)50重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)2.5重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別してチオシクラムシュウ酸塩10.3%粒剤を得た。
Example 12
11.5 parts by weight of thiocyclam oxalate, 12.3 parts by weight of stearic acid, 23.3 parts by weight of castor oil, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle size: about 40 μm ) 50 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemicals Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm) well mixed with 2.5 parts by weight is a disk pelleter ( Product name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10mm, particle size 4.0mm), granulated, sieved with 2mm (8.6 mesh) sieve, thiocyclam Oxalate 10.3% granules were obtained.

実施例13
チオシクラムシュウ酸塩11.5重量部、ステアリン酸15.7重量部、ヒマシ硬化油29.9重量部、DL−クレー(商品名、日東製粉社製、クレー、平均粒子径:約25μm)30.0重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)2.5重量部、リケマールS−200(商品名、理研ビタミン社製、グリセリンステアレート)10.1重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別してチオシクラムシュウ酸塩10.3%粒剤を得た。
Example 13
11.5 parts by weight of thiocyclam oxalate, 15.7 parts by weight of stearic acid, 29.9 parts by weight of castor oil hardened, DL-clay (trade name, manufactured by Nitto Seiyaku Co., Ltd., clay, average particle size: about 25 μm) 30.0 parts by weight, castor oil 0.35 parts by weight, NP fiber (trade name, manufactured by Nippon Paper Chemical Co., Ltd., fine crystalline cellulose, average particle size: 10 μm), 2.5 parts by weight, Riquemar S-200 (trade name, A disk pelleter (trade name, manufactured by Fuji Powder Co., Ltd., vertical extrusion granulator, die thickness 10 mm, particle size 4.0 mm) was prepared by mixing 10.1 parts by weight of Riken Vitamin Co., Ltd. (glyceryl stearate). ) And granulated with a 2 mm (8.6 mesh) sieve to obtain 10.3% thiocyclam oxalate granules.

実施例14
イミダクロプリド10.5重量部、ステアリン酸18.7重量部、ヒマシ硬化油35.5重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)30重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)5.0重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、ペグノールST−9(商品名、東邦化学工業社製、POEアルキルエーテル、HLB:13.3)0.3重量部をコーティングし、イミダクロプリド10.3%粒剤を得た。
Example 14
Imidacloprid 10.5 parts by weight, stearic acid 18.7 parts by weight, castor hydrogenated oil 35.5 parts by weight, silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle size: about 40 μm), A disk pelleter (trade name, Fuji) was prepared by mixing 0.35 parts by weight of castor oil and 5.0 parts by weight of NP fiber (trade name, manufactured by Nippon Paper Chemical Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm). Pourdal made, vertical extrusion granulator, put into a 10 mm die thickness, 4.0 mm particle size), granulated, and sieved with a 2 mm (8.6 mesh) sieve and put into a concrete mixer Pegnol ST-9 (trade name, manufactured by Toho Chemical Industry Co., Ltd., POE alkyl ether, HLB: 13.3) 0.3 parts by weight was coated to obtain imidacloprid 10.3% granules.

実施例15
イミダクロプリド2.0重量部、ステアリン酸15.6重量部、ヒマシ硬化油29.6重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)50重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)2.5重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、レオドールTW-O120V(商品名、花王社製、POEソルビタンモノオレエート、HLB:15)0.3重量部をコーティングし、イミダクロプリド2.0%粒剤を得た。
Example 15
2.0 parts by weight of imidacloprid, 15.6 parts by weight of stearic acid, 29.6 parts by weight of castor oil, 50 parts by weight of silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle size: about 40 μm), A disk pelleter (trade name, Fuji) was prepared by mixing 0.35 parts by weight of castor oil and 2.5 parts by weight of NP fiber (trade name, manufactured by Nippon Paper Chemical Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm). Pourdal made, vertical extrusion granulator, put into a 10 mm die thickness, 4.0 mm particle size), granulated, and sieved with a 2 mm (8.6 mesh) sieve and put into a concrete mixer , Rhedol TW-O120V (trade name, manufactured by Kao Corporation, POE sorbitan monooleate, HLB: 15) 0.3 parts by weight was coated to obtain 2.0% granules of imidacloprid.

実施例16
ピメトロジン3.0重量部、ステアリン酸15.2重量部、ヒマシ硬化油28.9重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)50重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)2.5重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、レオドールTW-O120V(商品名、花王社製、POEソルビタンモノオレエート、HLB:15)0.3重量部をコーティングし、ピメトロジン3.0%粒剤を得た。
Example 16
3.0 parts by weight of pymetrozine, 15.2 parts by weight of stearic acid, 28.9 parts by weight of castor oil, 50 parts by weight of silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle size: about 40 μm), A disk pelleter (trade name, Fuji) was prepared by mixing 0.35 parts by weight of castor oil and 2.5 parts by weight of NP fiber (trade name, manufactured by Nippon Paper Chemical Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm). Pourdal made, vertical extrusion granulator, put into a 10 mm die thickness, 4.0 mm particle size), granulated, and sieved with a 2 mm (8.6 mesh) sieve and put into a concrete mixer , Rhedol TW-O120V (trade name, manufactured by Kao Corporation, POE sorbitan monooleate, HLB: 15) 0.3 parts by weight was coated to obtain 3.0% pymetrozine granules.

実施例17
チアメトキサム2.0重量部、ステアリン酸15.6重量部、ヒマシ硬化油29.6重量部、シルト#500(商品名、丸中白土社製、白土、平均粒子径:約40μm)50重量部、ヒマシ油0.35重量部、NPファイバー(商品名、日本製紙ケミカル社製、微粉結晶セルロース、平均粒子径:10μm)2.5重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別したものをコンクリートミキサーに投入し、レオドールTW-O120V(商品名、花王社製、POEソルビタンモノオレエート、HLB:15)0.3重量部をコーティングし、チアメトキサム2.0%粒剤を得た。
Example 17
2.0 parts by weight of thiamethoxam, 15.6 parts by weight of stearic acid, 29.6 parts by weight of castor oil, 50 parts by weight of silt # 500 (trade name, manufactured by Marunaka Shiratosha, white clay, average particle size: about 40 μm), A disk pelleter (trade name, Fuji) was prepared by mixing 0.35 parts by weight of castor oil and 2.5 parts by weight of NP fiber (trade name, manufactured by Nippon Paper Chemical Co., Ltd., finely divided crystalline cellulose, average particle size: 10 μm). Pourdal made, vertical extrusion granulator, put into a 10 mm die thickness, 4.0 mm particle size), granulated, and sieved with a 2 mm (8.6 mesh) sieve and put into a concrete mixer , Rhedol TW-O120V (trade name, manufactured by Kao Corporation, POE sorbitan monooleate, HLB: 15) 0.3 parts by weight was coated to obtain 2.0% thiamethoxam granules.

比較例1
チオシクラムシュウ酸塩11.5重量部、ヒマシ油0.2重量部、ステアリン酸20重量部、ヒマシ硬化油37.8重量部、DL−クレー(商品名、日東製粉社製、クレー、平均粒子径:約25μm)30.0重量部、カープレックス#80(商品名、デグサジャパン社製、非晶質二酸化珪素)0.5重量部をよく混合したものをディスクペレッター(商品名、不二パウダル社製、縦型押出造粒機、ダイス厚さ10mm、粒径4.0mm)に投入して造粒し、2mm(8.6メッシュ)の篩で篩別してチオシクラムシュウ酸塩10.3%粒剤を得た。
Comparative Example 1
11.5 parts by weight of thiocyclam oxalate, 0.2 part by weight of castor oil, 20 parts by weight of stearic acid, 37.8 parts by weight of castor oil hardened, DL-clay (trade name, manufactured by Nitto Flour Mills, clay, average Particle pellet (about 25 μm) 30.0 parts by weight and Carplex # 80 (trade name, manufactured by Degussa Japan, amorphous silicon dioxide) 0.5 part by weight was mixed well with a disk pelleter (trade name, Thiocyclam oxalate 10 produced by Nipowdar Co., Ltd., vertical extrusion granulator, put into a die 10 mm thick, particle size 4.0 mm), granulated and sieved with a 2 mm (8.6 mesh) sieve A 3% granule was obtained.

比較例2
チオシクラムシュウ酸塩11.7重量部を加熱溶融したステアリン酸88.3重量部に溶融機にて混合溶融し、金属製のバットに流し込み、冷却してシート化したものをペレタイザーで破砕し、1mm(16メッシュ)〜1.7mm(10メッシュ)の範囲で篩別してチオシクラムシュウ酸塩10.3%粒剤を得た。
Comparative Example 2
11.7 parts by weight of thiocyclam oxalate is mixed and melted in 88.3 parts by weight of stearic acid heated and melted in a melting machine, poured into a metal vat, cooled and crushed with a pelletizer. Sieving in the range of 1 mm (16 mesh) to 1.7 mm (10 mesh) gave thiocyclam oxalate 10.3% granules.

比較例3
チオシクラムシュウ酸塩11.7重量部を加熱溶融したベヘン酸88.3重量部に溶融機にて混合溶融し、金属製のバットに流し込み、冷却してシート化したものをペレタイザーで破砕し、1mm(16メッシュ)〜1.7mm(10メッシュ)の範囲で篩別してチオシクラムシュウ酸塩10.3%粒剤を得た。
Comparative Example 3
11.7 parts by weight of thiocyclam oxalate was mixed and melted in 88.3 parts by weight of behenic acid heated and melted in a melting machine, poured into a metal bat, cooled, and crushed with a pelletizer. Sieving in the range of 1 mm (16 mesh) to 1.7 mm (10 mesh) gave thiocyclam oxalate 10.3% granules.

比較例4
チオシクラムシュウ酸塩11.7重量部を加熱溶融したグリセリンモノステアレート88.3重量部に溶融機にて混合溶融し、金属製のバットに流し込み、冷却してシート化したものをペレタイザーで破砕し、1mm(16メッシュ)〜1.7mm(10メッシュ)の範囲で篩別してチオシクラムシュウ酸塩10.3%粒剤を得た。
Comparative Example 4
11.7 parts by weight of thiocyclam oxalate was mixed and melted in 88.3 parts by weight of glycerin monostearate with a melting machine, poured into a metal bat, cooled and formed into a sheet with a pelletizer. The mixture was crushed and sieved in the range of 1 mm (16 mesh) to 1.7 mm (10 mesh) to obtain 10.3% thiocyclam oxalate granules.

比較例5
チオシクラムシュウ酸塩11.7重量部、DL−クレー(商品名、日東製粉社製、クレー、平均粒子径:約25μm)30重量部を加熱溶融したグリセリンモノステアレート58.3重量部に溶融機にて混合溶融し、金属製のバットに流し込み、冷却してシート化したものをペレタイザーで破砕し、1mm(16メッシュ)〜1.7mm(10メッシュ)の範囲で篩別してチオシクラムシュウ酸塩10.3%粒剤を得た。
Comparative Example 5
To 58.3 parts by weight of glycerol monostearate obtained by heating and melting 11.7 parts by weight of thiocyclam oxalate and 30 parts by weight of DL-clay (trade name, manufactured by Nitto Seiyaku Co., Ltd., clay, average particle size: about 25 μm) It is mixed and melted in a melting machine, poured into a metal bat, cooled and crushed with a pelletizer, sieved in the range of 1 mm (16 mesh) to 1.7 mm (10 mesh), and thiocyclam Shu An acid salt 10.3% granule was obtained.

比較例6
チオシクラムシュウ酸塩11.7重量部、DL−クレー(商品名、日東製粉社製、クレー、平均粒子径:約25μm)30重量部、グリセリンモノステアレート10重量部を加熱溶融した牛硬化油48.3重量部に溶融機にて混合溶融し、金属製のバットに流し込み、冷却してシート化したものをペレタイザーで破砕し、1mm(16メッシュ)〜1.7mm(10メッシュ)の範囲で篩別してチオシクラムシュウ酸塩10.3%粒剤を得た。
Comparative Example 6
Beef cured by heating and melting 11.7 parts by weight of thiocyclam oxalate, 30 parts by weight of DL-clay (trade name, manufactured by Nitto Flour Mills, clay, average particle size: about 25 μm), and 10 parts by weight of glycerol monostearate 48.3 parts by weight of oil is mixed and melted with a melting machine, poured into a metal bat, cooled and formed into a sheet, and crushed with a pelletizer, in the range of 1 mm (16 mesh) to 1.7 mm (10 mesh) And thiocyclam oxalate 10.3% granules were obtained.

比較例7
チオシクラムシュウ酸塩11.7重量部、DL−クレー(商品名、日東製粉社製、クレー、平均粒子径:約25μm)30重量部、グリセリンモノステアレート20重量部を加熱溶融したヒマシ硬化油38.3重量部に溶融機にて混合溶融し、金属製のバットに流し込み、冷却してシート化したものをペレタイザーで破砕し、1mm(16メッシュ)〜1.7mm(10メッシュ)の範囲で篩別してチオシクラムシュウ酸塩10.3%粒剤を得た。
Comparative Example 7
Castor curing in which 11.7 parts by weight of thiocyclam oxalate, 30 parts by weight of DL-clay (trade name, manufactured by Nitto Flour Mills Co., Ltd., clay, average particle size: about 25 μm) and 20 parts by weight of glycerin monostearate are heated and melted. 38.3 parts by weight of oil is mixed and melted with a melting machine, poured into a metal bat, cooled and formed into a sheet, and crushed with a pelletizer, in the range of 1 mm (16 mesh) to 1.7 mm (10 mesh) And thiocyclam oxalate 10.3% granules were obtained.

試験例1 水中沈降性試験
本発明の粒剤及び比較例1,6,7について、水面での浮遊状況を目視にて調査した。粒剤5粒を1Lの蒸留水に満たされた1Lビーカーに投じ、粒の様子の変化を経時的に確認し、以下の3段階で評価し、結果を表1にまとめた。
○:全ての粒が沈んでいる
△:過半数の粒が沈んでいる
×:過半数の粒が水面に浮上している
Test Example 1 Underwater Sedimentability Test The floating state on the water surface was examined visually for the granules of the present invention and Comparative Examples 1, 6, and 7. Five granules were poured into a 1 L beaker filled with 1 L of distilled water, changes in the appearance of the grains were confirmed over time, evaluated in the following three stages, and the results are summarized in Table 1.
○: All grains are sinking △: A majority of grains are sinking
X: A majority of the grains floated on the water surface

試験例2 硬度試験
本発明の粒剤及び比較例1,6,7をそれぞれ100gを、磁製ボール3個(合計105g)と共にボールミルポットに投入し、毎分75回転で15分間回転させた。その後、ボールミルポット内の内容物を取り出し、目開き0.5mmの篩にかけて通過した小粒を秤量し、その値を硬度とした。値が小さいほど硬度が高いと判断する。試験例1及び試験例2の結果を表1に示した。
Test Example 2 Hardness Test 100 g each of the granule of the present invention and Comparative Examples 1, 6, and 7 were put into a ball mill pot together with three magnetic balls (total of 105 g), and rotated at 75 rpm for 15 minutes. Thereafter, the contents in the ball mill pot were taken out, and the small particles passed through a sieve having an opening of 0.5 mm were weighed, and the value was taken as the hardness. The smaller the value, the higher the hardness. The results of Test Example 1 and Test Example 2 are shown in Table 1.

表1 粒剤の水中沈降性と硬度試験結果
供試試料 投下直後 3時間後 6時間後 硬度
実施例1 ○ ○ ○ 3.6
実施例2 ○ ○ ○ 1.6
実施例3 ○ ○ ○ 1.6
実施例4 ○ ○ ○ 4.7
実施例5 ○ ○ ○ 4.5
実施例6 ○ ○ ○ 2.7
実施例7 ○ ○ ○ 2.8
実施例8 ○ ○ ○ 3.7
実施例9 ○ ○ ○ 2.0
実施例10 ○ △ △ 3.8
実施例11 ○ △ △ 4.0
実施例12 ○ △ △ 2.5
実施例13 △ △ △ 7.4
実施例15 ○ ○ ○ 3.6
実施例16 ○ ○ ○ 4.5
実施例17 ○ ○ ○ 2.9
比較例1 ○ △ × 29.1
比較例6 ○ ○ ○ 7.2
比較例7 ○ ○ ○ 8.5
Table 1 Sedimentability and hardness test results of granules in water Test sample Immediately after dropping 3 hours later 6 hours later Hardness Example 1 ○ ○ ○ 3.6
Example 2 ○ ○ ○ 1.6
Example 3 ○ ○ ○ 1.6
Example 4 ○ ○ ○ 4.7
Example 5 ○ ○ ○ 4.5
Example 6 ○ ○ ○ 2.7
Example 7 ○ ○ ○ 2.8
Example 8 ○ ○ ○ 3.7
Example 9 ○ ○ ○ 2.0
Example 10 ○ △ △ 3.8
Example 11 ○ △ △ 4.0
Example 12 ○ △ △ 2.5
Example 13 Δ Δ Δ 7.4
Example 15 ○ ○ ○ 3.6
Example 16 ○ ○ ○ 4.5
Example 17 ○ ○ ○ 2.9
Comparative Example 1 ○ Δ × 29.1
Comparative Example 6 ○ ○ ○ 7.2
Comparative Example 7 ○ ○ ○ 8.5

試験例3 水中溶出試験1
チオシクラムシュウ酸塩を農薬活性成分とした実施例1〜9及び13、並びに比較例1〜7の農薬粒剤0.5gを100mL共栓付き三角フラスコに入れ、100mLの蒸留水を静かに注いだ(粒剤中の全てのチオシクラムシュウ酸塩が水中に溶出した場合500ppmとなる)。これを25℃恒温槽に所定時間静置後、1日後、3日後、7日後における水中に溶出したチオシクラムシュウ酸塩の量をHPLCにより測定した。試験例3の結果を表2にまとめた。
Test Example 3 Underwater dissolution test 1
Put 0.5 g of agricultural chemical granules of Examples 1 to 9 and 13 and Comparative Examples 1 to 7 using thiocyclam oxalate as an agrochemical active ingredient into a 100 mL Erlenmeyer flask, and gently add 100 mL of distilled water. Poured (when all thiocyclam oxalate in the granules is eluted in water, it becomes 500 ppm). The amount of thiocyclam oxalate eluted in water after 1 day, 3 days, and 7 days after standing in a 25 ° C. constant temperature bath was measured by HPLC. The results of Test Example 3 are summarized in Table 2.

表2 粒剤の水中沈降性とチオシクラムシュウ酸塩の溶出量(ppm)
供試試料 1日後 3日後 7日後
実施例1 69 104 136
実施例2 70 104 131
実施例3 128 209 282
実施例4 39 55 67
実施例5 75 123 165
実施例6 36 57 75
実施例7 65 108 145
実施例8 164 249 321
実施例9 107 190 270
実施例13 99 195 293
比較例1 10 16 24
比較例2 307 367 375
比較例3 405 497 484
比較例4 472 498 474
比較例5 470 491 367
比較例6 233 389 428
比較例7 220 328 369
Table 2 Precipitation of granules in water and elution amount of thiocyclam oxalate (ppm)
Test sample 1 day later 3 days later 7 days later Example 1 69 104 136
Example 2 70 104 131
Example 3 128 209 282
Example 4 39 55 67
Example 5 75 123 165
Example 6 36 57 75
Example 7 65 108 145
Example 8 164 249 321
Example 9 107 190 270
Example 13 99 195 293
Comparative Example 1 10 16 24
Comparative Example 2 307 367 375
Comparative Example 3 405 497 484
Comparative Example 4 472 498 474
Comparative Example 5 470 491 367
Comparative Example 6 233 389 428
Comparative Example 7 220 328 369

試験例4 水中溶出試験2
実施例15〜17の農薬粒剤を、農薬活性成分含量が50mgになるよう量り取り、100mL共栓付き三角フラスコに入れ、100mLの蒸留水を静かに注いだ(粒剤中の全ての有効成分が溶出した場合500ppmとなる)。これを25℃恒温槽に所定時間静置後、2時間、24時間、96時間後における水中に溶出した農薬活性成分量をHPLCにより測定した。試験例4の結果を表3にまとめた。
Test Example 4 Water dissolution test 2
The agricultural chemical granules of Examples 15 to 17 were weighed so that the content of the agricultural chemical active ingredient was 50 mg, put into a 100 mL stoppered Erlenmeyer flask, and 100 mL of distilled water was gently poured (all active ingredients in the granules). Is 500 ppm in the case of elution). This was allowed to stand in a constant temperature bath at 25 ° C. for a predetermined time, and then the amount of the pesticidal active ingredient eluted in water after 2 hours, 24 hours and 96 hours was measured by HPLC. The results of Test Example 4 are summarized in Table 3.

表3 粒剤の水中沈降性と有効成分の溶出量(ppm)
供試試料 2時間後 24時間後 96時間後
実施例15 15 52 96
実施例16 8.3 54 105
実施例17 39 117 233
Table 3 Sedimentability of granules in water and elution amount of active ingredients (ppm)
Test sample 2 hours later 24 hours later 96 hours later Example 15 15 52 96
Example 16 8.3 54 105
Example 17 39 117 233

試験例5 殺虫効力試験
30cm×40cm×15cmのコンテナバットに水稲苗5本×6株定植し、加温温室に置いた。定植16日後に本発明のチアメトキサムを農薬活性成分とする実施例17の農薬粒剤を33g散布した。また比較例8として市販のチアメトキサム2%粒剤(デジタルコラトップアクタラ粒剤(商品名)/シンジェンタ社製)を33g散布した。散布後4日、13日、63日後にウンカ類(トビイロウンカ、セジロウンカ)を放虫した。放虫処理3日後にウンカ類の生死を観察して死虫率を算出した。その結果を表4に示した。
Test Example 5 Insecticidal Efficacy Test 5 rice seedlings × 6 strains were planted in a 30 cm × 40 cm × 15 cm container bat and placed in a warming greenhouse. Sixteen days after planting, 33 g of the pesticidal granule of Example 17 containing thiamethoxam of the present invention as an pesticidal active ingredient was sprayed. In addition, as Comparative Example 8, 33 g of a commercially available thiamethoxam 2% granule (Digital Kola Top Actara Granule (trade name) / manufactured by Syngenta) was sprayed. After 4 days, 13 days, and 63 days after spraying, the planthoppers (Tobiro planta, white planthopper) were released. Three days after the insect release treatment, the life and death of the planthoppers were observed, and the death rate was calculated. The results are shown in Table 4.

表4 粒剤のウンカ類に対する効力試験結果(死虫率/%)
供試試料 4日 13日 63日
実施例17 63 92 24
比較例8 0 89 24
Table 4 Results of the efficacy test of granule on planthoppers (Death rate /%)
Test sample 4 days 13 days 63 days Example 17 63 92 24
Comparative Example 8 0 89 24

表1に示したように本発明の農薬粒剤は、水中への投入直後だけでなく投入後時間が経過しても水中に沈降した状態を保っていた。これは農薬粒剤に含まれる無機物質が当該農薬粒剤の比重を1以上に調整したことと共に、界面活性剤が粒表面の物理性を変化させ、親水性を付与すると共に、粒表面に付着する泡を粒表面から剥離させる働きにより、粒剤を持続的に水中に沈降させることができた。また硬度試験においてもボールミル破砕量が少ない結果を示し、農薬粒剤として十分な硬度を示した。一方、水難溶性多糖類成分を添加しない比較例1は持続的沈降性を維持できず、また硬度試験においてもボールミル破砕量が多く粒剤硬度としては不十分であった。熱溶融により調製した比較例6、7は、DL−クレーを含有した効果により良好な水沈降性を示したが、粒剤硬度は若干低下した。
また表2及び表3に示したように、本発明の農薬粒剤は水難溶性多糖類、無機物質、界面活性剤を添加し、これらの組成含量を調整することによって、様々な溶出特性を持つ粒剤に仕上げることが可能であり、初期溶出性を抑制すると共に持続的な薬剤溶出制御を達成し、所望の溶出速度の粒剤を得ることができた。また、チオシクラムシュウ酸塩に限らず、農薬活性成分としてイミダクロプリドやチアメトキサムのネオニコチノイド系農薬活性成分、並びにピメトロジンに対して溶出制御能を付与することができ、様々な農薬有効成分に対する応用範囲の広い製剤処方技術であると言える。一方、水難溶性多糖類を含まない比較例1は薬剤溶出速度の著しい低下が見られ、また熱溶融により調製された比較例2〜7は薬剤の初期溶出抑制が達せられず、農薬活性成分の持続的放出に伴う薬効維持効果に課題が見られた。
本発明の実施例17の殺虫効力試験は、散布後〜63日に亘り殺虫効力を発揮できることが示された。本願の初期薬剤放出制御作用と持続的薬剤放出制御作用を有する農薬粒剤は、殺虫効力の初期効力と持続的効力を両立する殺虫効果を発揮した。一方、比較例8である市販のチアメトキサム含有粒剤(デジタルコラトップアクタラ粒剤(商品名)/シンジェンタ社製)は、長期残効性を示したものの初期効力が不十分であった。したがって、本願に係る農薬粒剤は薬剤溶出制御作用を有し、農薬散布の初期から長期に亘り持続的な薬剤溶出を達成し、一度の圃場散布により殺虫効力の初効と残効の両立を図ることができることが示された。
As shown in Table 1, the agrochemical granule of the present invention was kept in the state of being settled in water not only immediately after being put into water but also after the time had been passed. This is because the inorganic substance contained in the pesticide granules adjusts the specific gravity of the pesticide granules to 1 or more, and the surfactant changes the physical properties of the grain surface, imparts hydrophilicity, and adheres to the grain surface. Due to the action of exfoliating foam from the surface of the grains, the granules could be continuously settled in water. Also in the hardness test, the results showed that the ball mill crushed amount was small, and the hardness was sufficient as an agrochemical granule. On the other hand, in Comparative Example 1 in which the poorly water-soluble polysaccharide component was not added, the sustained sedimentation property could not be maintained, and in the hardness test, the ball mill crushed amount was large and the granule hardness was insufficient. Comparative Examples 6 and 7 prepared by hot melting showed good water sedimentation due to the effect of containing DL-clay, but the granule hardness slightly decreased.
Moreover, as shown in Table 2 and Table 3, the agrochemical granule of the present invention has various elution characteristics by adding a poorly water-soluble polysaccharide, an inorganic substance, and a surfactant and adjusting the composition content thereof. It was possible to finish it into a granule, and it was possible to obtain a granule having a desired elution rate by suppressing initial dissolution and achieving continuous drug elution control. In addition to thiocyclam oxalate, it can provide elution control capability to imidacloprid and thiamethoxam neonicotinoid agrochemical active ingredients and pymetrozine as an agrochemical active ingredient, and it can be applied to various agrochemical active ingredients. It can be said that this is a wide range of pharmaceutical formulation technology. On the other hand, in Comparative Example 1 containing no poorly water-soluble polysaccharide, the drug elution rate was remarkably reduced, and Comparative Examples 2 to 7 prepared by hot melting did not achieve the initial elution suppression of the drug. There was a problem in the effect of maintaining the drug effect due to the sustained release.
The insecticidal efficacy test of Example 17 of the present invention showed that insecticidal efficacy can be exerted for up to 63 days after spraying. The agrochemical granule having the initial drug release control action and the sustained drug release control action of the present application exhibited an insecticidal effect that achieves both an initial insecticidal efficacy and a sustained efficacy. On the other hand, the commercially available thiamethoxam-containing granule (Comparative Example 8 Digital Collatop Actara Granule (trade name) / manufactured by Syngenta Co., Ltd.), which was Comparative Example 8, showed long-term residual effect but had insufficient initial efficacy. Therefore, the agrochemical granule according to the present application has a drug elution control action, achieves continuous drug elution over the long term from the beginning of pesticide spraying, and achieves both the initial effect and the residual effect of insecticidal efficacy by spraying once in the field. It was shown that it can be planned.

水溶解度の高い農薬活性成分の溶出を制御し溶出期間を長期化させ、散布回数を減らし省力化を可能にする。また、当該農薬粒剤中に水中沈降性を付与する材料を添加及び/又は押出造粒して得られた農薬粒剤の表面にコーティングすることで脂肪酸誘導体の比重の軽さと撥水性による粒の水面への浮上の結果起きる、流水や風による粒剤の局在化や水田からの流亡を防いで、均一な効力を発揮する。


Controls the elution of pesticide active ingredients with high water solubility, prolongs the elution period, reduces the number of spraying, and saves labor. In addition, by adding and / or coating the surface of the pesticide granule obtained by adding and / or extrusion granulating a material that imparts sedimentation in water to the agrochemical granule, the specific gravity of the fatty acid derivative and the water repellent Prevents the localization of granules and the runoff from paddy fields caused by flowing water and wind, resulting in uniform effectiveness.


Claims (19)

農薬活性成分(a)、脂肪酸及び/又は脂肪酸誘導体(b)、水難溶性多糖類(c)、及び無機物質(d)を含むことを特徴とする農薬組成物。 A pesticide composition comprising a pesticide active ingredient (a), a fatty acid and / or a fatty acid derivative (b), a poorly water-soluble polysaccharide (c), and an inorganic substance (d). 農薬活性成分(a)として20℃における水溶解度が100ppm以上の農薬活性成分である請求項1記載の農薬組成物。 The agrochemical composition according to claim 1, wherein the agrochemical active ingredient (a) is an agrochemical active ingredient having a water solubility at 20 ° C of 100 ppm or more. 農薬組成物中に農薬活性成分(a)を3〜25質量%含有する請求項1又は2に記載の農薬組成物。 The agrochemical composition according to claim 1 or 2, wherein the agrochemical composition contains 3 to 25% by mass of the agrochemical active ingredient (a). 脂肪酸及び/又は脂肪酸誘導体(b)がC8〜C40アルキル鎖カルボン酸及びその誘導体の中から選ばれる1種、または2種以上の混合物である請求項1〜3のいずれか一項に記載の農薬組成物。 The agrochemical according to any one of claims 1 to 3, wherein the fatty acid and / or fatty acid derivative (b) is one or a mixture of two or more selected from C8-C40 alkyl chain carboxylic acids and derivatives thereof. Composition. 脂肪酸及び/又は脂肪酸誘導体(b)がヒマシ硬化油、ヒマシ油、及びステアリン酸の混合物である請求項1〜4のいずれか一項に記載の農薬組成物。 The agrochemical composition according to any one of claims 1 to 4, wherein the fatty acid and / or the fatty acid derivative (b) is a mixture of castor oil, castor oil, and stearic acid. 水難溶性多糖類(c)が結晶セルロースであってその平均粒子径が1μm〜45μmであることを特徴とする請求項1〜5のいずれか一項に記載の農薬組成物。 The agrochemical composition according to any one of claims 1 to 5, wherein the poorly water-soluble polysaccharide (c) is crystalline cellulose and has an average particle size of 1 µm to 45 µm. 農薬活性成分(a)がネライストキシン系農薬活性成分を含む請求項1〜6のいずれか一項に記載の農薬組成物。 The agrochemical composition according to any one of claims 1 to 6, wherein the agrochemical active ingredient (a) includes a nereistoxin agrochemical active ingredient. ネライストキシン系農薬活性成分が1,3−ジカルバモイルチオ−2−(N,N−ジメチルアミノ)−プロパン塩酸塩(以下、カルタップ塩酸塩)、又は5‐ジメチルアミノ‐1,2,3‐トリチアンシュウ酸塩(以下、チオシクラムシュウ酸塩)である請求項7に記載の農薬組成物。 Nereistoxin pesticide active ingredient is 1,3-dicarbamoylthio-2- (N, N-dimethylamino) -propane hydrochloride (hereinafter referred to as cartap hydrochloride) or 5-dimethylamino-1,2,3- The agrochemical composition according to claim 7, which is trithian oxalate (hereinafter referred to as thiocyclam oxalate). 無機物質(d)がクレー、タルク、白土、珪藻土、ゼオライト、硫酸バリウム、二酸化チタン、及び非晶質二酸化珪素(ホワイトカーボン)からなる群から選ばれる1種以上である請求項1〜8のいずれか一項に記載の農薬組成物。 The inorganic substance (d) is at least one selected from the group consisting of clay, talc, white clay, diatomaceous earth, zeolite, barium sulfate, titanium dioxide, and amorphous silicon dioxide (white carbon). The agricultural chemical composition according to claim 1. 農薬組成物中に、農薬活性成分(a)を3〜25質量%、脂肪酸及び/又は脂肪酸誘導体(b)を10〜80質量%、水難溶解性多糖類(c)を0.5〜20質量%、及び無機物質(d)を10〜60質量%を含有する請求項1〜9のいずれか一項の農薬組成物。 In the agrochemical composition, the agrochemical active ingredient (a) is 3 to 25% by mass, the fatty acid and / or the fatty acid derivative (b) is 10 to 80% by mass, and the poorly soluble polysaccharide (c) is 0.5 to 20% by mass. %, And the agrochemical composition as described in any one of Claims 1-9 containing 10-60 mass% of inorganic substances (d). 更に界面活性剤(e)を0.1〜10質量%含有する請求項1〜10のいずれか一項に記載の農薬組成物。 Furthermore, the agrochemical composition as described in any one of Claims 1-10 which contains 0.1-10 mass% of surfactant (e). 界面活性剤(e)がノニオン性界面活性剤及びアニオン性界面活性剤の中から選ばれる1種、または2種以上の混合物である請求項11に記載の農薬組成物。 The agrochemical composition according to claim 11, wherein the surfactant (e) is one or a mixture of two or more selected from nonionic surfactants and anionic surfactants. 請求項1〜12のいずれか一項に記載の農薬組成物を混合した後、造粒してなる農薬粒剤。 The agrochemical granule formed by granulating, after mixing the agrochemical composition as described in any one of Claims 1-12. 請求項1〜12のいずれか一項に記載の農薬組成物を混合し、縦型押出造粒機にて造粒して得られる農薬粒剤。 The agrochemical granule obtained by mixing the agrochemical composition as described in any one of Claims 1-12, and granulating with a vertical extrusion granulator. 請求項1〜12のいずれか一項に記載の農薬組成物を混合し、縦型押出造粒機にて造粒したものに、請求項11又は12に記載の界面活性剤(e)をコーティングして得られる農薬粒剤。 The surfactant (e) according to claim 11 or 12 is coated on the mixture obtained by mixing the agrochemical composition according to any one of claims 1 to 12 and granulating with a vertical extrusion granulator. Pesticide granules. 粒径が2mm〜10mmであることを特徴とする請求項13〜15に記載の農薬粒剤。 The agrochemical granule according to claim 13, wherein the particle size is 2 mm to 10 mm. 請求項1〜12のいずれか一項に記載の農薬組成物を混合した後、縦型押出造粒機にて造粒する農薬粒剤の製造方法。 The manufacturing method of the agrochemical granule granulated with a vertical extrusion granulator after mixing the agrochemical composition as described in any one of Claims 1-12. 請求項1〜12のいずれか一項に記載の農薬組成物を混合した後、縦型押出造粒機にて造粒した後、請求項11又は12に記載の界面活性剤(e)をコーティングする農薬粒剤の製造方法。 After mixing the agrochemical composition according to any one of claims 1 to 12, and then granulating with a vertical extrusion granulator, the surfactant (e) according to claim 11 or 12 is coated. To produce agrochemical granules. 縦型押出造粒機に使用するダイスの厚さが10mm以上であることを特徴とする請求項17又は18に記載の農薬粒剤の製造方法。 The method for producing an agrochemical granule according to claim 17 or 18, wherein the die used in the vertical extrusion granulator has a thickness of 10 mm or more.
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