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METHOD FOR PRODUCING SPHERICAL pyroxylin gunpowder for sporting cartridges of 7.62 mm

机译:用于制造7.62毫米运动弹药的球形吡咯啉火药的方法

摘要

A method for producing spherical powder pyroxylin to 7.62 mm sporting cartridge comprising preparing a powder lacquer with agitation in an aqueous medium with a mixture of nitrocellulose reciprocating together with technological wastes diphenylamine and solvent-ethyl acetate, dispersing the powder lacquer to the spherical particles and the removal of ethyl acetate, wherein that is poured into the reactor 4.5 ... 5.6 wt. parts of water in relation to the nitrocellulose charged with 1 wt. part of nitrocellulose with a nitrogen oxide content of 212.7 ... 214.0 mL NO / g and up to 30 wt% reciprocating process waste from previous operations, is poured under stirring, 3.8 ... 5.2 parts by weight of solvent -. of ethyl acetate was charged to . weight nitrocellulose 0.5 ... 0.8 wt% diphenylamine, are preparation of a powder lacquer at a temperature of 55 ... 68 ° C for 60 ... 80 min, then after entering the protective colloid - mezdrovogo adhesive in an amount of 0.8 ... 1.2 wt.% and 0.4 ... 0.8 wt.% of dextrin relative to the water, leading to crushing of the powder lacquer spherical particles for 70 ... 90 min n and a reactor temperature of 55 ... 68 ° C, is introduced in relation to water of 2.2 ... 2.5 wt.% sodium sulfate and lead stirring for 30 ... 40 min at a reactor temperature of 60 ... 68 ° C, distilling off the solvent from the powder elements are the temperature of coolant supplied to the reactor jacket, while for 10 ... 15 min coolant temperature is raised to 82 ... 86 ° C, and lead exposure, distilling off 70 ... 75 wt.% solvent, and then for 10 ... 15 minutes, the temperature the coolant is raised to 94 ... 98 ° C, and lead exposure until the temperature of the mixture in the reactor is 94 ... 96 ° C .
机译:一种将球状粉末木粉生产到7.62 mm运动药筒的方法,该方法包括在水性介质中搅拌混合硝化纤维素与技术废品二苯胺和溶剂-乙酸乙酯的混合物,制备粉末状漆料,将粉末状漆料分散到球形颗粒和除去乙酸乙酯,其中将其倒入反应器中4.5 ... 5.6 wt。相对于硝化纤维素中加入1 wt。在搅拌下将一部分氮氧化物含量为212.7 ... 214.0 mL NO / g的硝化纤维素和高达30 wt%的先前操作的往复工艺废料倒入3.8 ... 5.2重量份的溶剂-中。将一半的乙酸乙酯装入水中。重量的硝化纤维素0.5 ... 0.8 wt%二苯胺是在55 ... 68°C的温度下制备粉末漆60 ... 80 min,然后以0.8的量进入保护性胶体-mezdrovogo粘合剂相对于水... ... 1.2重量%和0.4 ... 0.8重量%的糊精,导致粉末漆球形颗粒的压碎持续70到90分钟,反应器温度为55到68相对于2.2 ... 2.5 wt。%的硫酸钠加入30°C,并在60 ... 68°C的反应器温度下铅搅拌30 ... 40 min,从粉末中蒸馏出溶剂元素是供应到反应器夹套的冷却剂温度,同时在10到15分钟内将冷却剂温度升至82到86°C,并暴露在铅中,蒸馏出70到75 wt%的溶剂,以及然后持续10到15分钟,冷却剂的温度升至94到98℃,并暴露在铅中,直到反应器中混合物的温度达到94到96℃为止。

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