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High purity technical grade phosphoric acid preparation - from wet process phosphoric acid by formation of urea phosphate, purification and treatment with nitric acid

机译:高纯度工业级磷酸制备-由湿法磷酸通过形成脲磷酸酯,纯化和硝酸处理而制得

摘要

Process for the preparation of high purity technical phosphoric acid by following successive stages effected in continuous or batch mode; -a) crude wet process phosphoric acid, containing 50-54% P205, is diluted with water and/or an aqueous solution of phosphoric acid, optionally containing urea, until it contains 30-50% P205 and 0-8% of urea. Then this product is reacted with 1-4wt% of a composition previously formed from 1 part sodium carbonate and 3-5 parts of reduced phosphorite of particle size less than 150 microns, with a reaction content time of 1-3 hrs. and the product from the reaction is treated with 20-30 ppm of a flocculant in aqueous solution. The liquid phase is decanted from the insolubles and represents 50-95% of the initially introduced P205 and contains 31-50% P205 and 0-7%urea; b) the acid from stage a) is treated with urea and the formed urea phosphate crystallised by cooling or heating under reduced pressure to obtain urea phosphate of particle size 100-2000 microns. The mother liquors may be recycled to the first stage and the crystals are lixwated with an equivalent weight of a saturated solution of urea phosphate of recrystallised; c) in a third stage, the urea phosphate from b) is used to form an aqueous reaction product containing 35-50%phosphoric acid, 6-21% nitric acid and 4-15% of urea and when equilibrium is reached the urea nitrate and phosphoric acid formed in the reaction are seperated. The crystalline mass is washed with nitric acid and the washings and a fraction of the obtained phosphate acid are recycled to the reaction with a new lot of urea phosphate; d) the residual urea and nitric acid content of the phosphoric acid is reduced by concentrating at 90-220deg.C. and 110-760 High quality technical grade phosphoric acid contg. not more than 0.02 wt. parts of impurities per 100 wt. parts P205. This product is suitable for use in galvanic baths (cleaning baths), other industrial processes where ortho- and polyphosphates are used a.
机译:通过以连续或间歇方式进行的连续步骤制备高纯工业磷酸的方法; -a)用水和/或磷酸水溶液(任选地包含尿素)稀释包含50-54%P 2 O 5的粗制湿法磷酸,直到其包含30-50%P 2 O 5和0-8%的尿素。然后使该产物与1-4重量%的先前由1份碳酸钠和3-5份粒度小于150微米的还原性亚磷酸酯形成的组合物反应,反应含量时间为1-3小时。反应产物用20-30ppm的絮凝剂在水溶液中处理。从不溶物中倾析出液相,其占初始引入的P205的50-95%,并且包含31-50%的P205和0-7%的尿素; b)将阶段a)的酸用尿素处理,并将形成的磷酸尿素通过冷却或在减压下加热而结晶,以获得粒度为100-2000微米的磷酸尿素。母液可以循环到第一阶段,并用等重量的重结晶的磷酸脲饱和溶液浸提结晶。 c)在第三阶段中,使用b)中的磷酸尿素形成含有35-50%磷酸,6-21%硝酸和4-15%尿素的含水反应产物,当达到平衡时,硝酸尿素分离反应中形成的磷酸。用硝酸洗涤该结晶物质,并将洗涤液和所得的一部分磷酸与新的磷酸脲磷酸酯循环至反应; d)通过在90-220℃浓缩来降低磷酸中残留的尿素和硝酸含量。和110-760高品质工业级磷酸(续)。不超过0.02 wt。每100 wt。零件P205。该产品适用于电镀浴(清洁浴)以及其他使用正磷酸盐和多磷酸盐的工业过程。

著录项

  • 公开/公告号FR2461680B1

    专利类型

  • 公开/公告日1983-03-11

    原文格式PDF

  • 申请/专利权人 CROS SOCIEDAD ANONIMA;

    申请/专利号FR19800015987

  • 发明设计人

    申请日1980-07-16

  • 分类号C01B25/234;

  • 国家 FR

  • 入库时间 2022-08-22 10:01:33

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