首页> 外国专利> СПОСІБ ВИГОТОВЛЕННЯ ЕНТОМОЦИДНОГО ПРЕПАРАТУ БАЦИЛОТУРІНГУ-М НА ОСНОВІ BACILLUS THURINGIENSIS VAR. THURINGIENSIS Л-4СПОСОБ ИЗГОТОВЛЕНИЯ ЭНТОМОЦИДНОГО ПРЕПАРАТА БАЦИЛЛОТУРИНГА-М НА ОСНОВЕ BACILLUS THURINGIENSIS VAR. THURINGIENSIS Л-4

СПОСІБ ВИГОТОВЛЕННЯ ЕНТОМОЦИДНОГО ПРЕПАРАТУ БАЦИЛОТУРІНГУ-М НА ОСНОВІ BACILLUS THURINGIENSIS VAR. THURINGIENSIS Л-4СПОСОБ ИЗГОТОВЛЕНИЯ ЭНТОМОЦИДНОГО ПРЕПАРАТА БАЦИЛЛОТУРИНГА-М НА ОСНОВЕ BACILLUS THURINGIENSIS VAR. THURINGIENSIS Л-4

机译:基于苏云金芽孢杆菌的杀虫剂制备Bacyloturing-M的方法。 THURINGIENSIS L-4 [基于拟南芥VAR。的杀虫剂杀菌法-M的制备方法。苏黎世L-4

摘要

A method to make a biopreparation for protecting plants from leaf-eating pests includes inoculating the cells of the strain L-4 of the bacteria Bacillus thuringiensis var. thuringiensis deposited at the Depository of the Institute of Microbiology and Virusology of NAS of Ukraine under the number IMV V-7130; cultivating thereof in a nutrient medium comprising all the micronutrients necessary for the cells, in particular Mg, Mn, Fe, Zn, mineral salts, carbohydrates, amine nitrogen; accumulation biomass thereof; drying on atomizing drier obtaining a dry preparation. Preparing a stock culture, inoculum and cultivating the strain is carried on a balanced medium comprising mass %: maize extract 2.0; molasses 2.0; (NН4)2НРО4 0.24; К2НРO4 0.051; рН prior sterilization is 7.3-7.5. To obtain the end product, the stock culture of the second passage is used for inoculating a production medium in an amount of 0.5-1.0% from the volume of the nutrient medium in a fermenter. While fermenting, air consumption is 14-16 m3/hour, a pressure of 0.4 bars, a temperature (30±2) °С, after fermenting the suspension concentrate is cooled and 7-8% of filler is added.
机译:一种制备用于保护植物免受叶食性害虫侵害的生物制剂的方法包括接种苏云金芽孢杆菌var。L-4菌株的细胞。将苏云金芽孢杆菌以IMV V-7130号保藏在乌克兰NAS微生物学和病毒学研究所保藏处;在包含细胞所需的所有微量营养素,特别是Mg,Mn,Fe,Zn,无机盐,碳水化合物,胺氮的营养培养基中培养;积累生物质;在雾化干燥器上干燥得到干燥制剂。准备储备培养物,接种物和培养菌株在包含质量%的平衡培养基上进行:玉米提取物2.0;和糖蜜2.0; (NН4)2НРО40.24; К2НРO40.051; рН之前的消毒温度是7.3-7.5。为了获得最终产品,第二代的原种培养物用于以发酵罐中营养培养基的0.5-1.0%的量接种生产培养基。发酵时,空气消耗量为14-16立方米/小时,压力为0.4巴,温度(30±2)°C,发酵后将悬浮浓缩物冷却并添加7-8%的填料。

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