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TECHNIQUE FOR PRODUCTION OF LIQUID COMPOSITE FERTILIZERS

机译:液体复合肥料的生产技术

摘要

The invention relates to the production of liquid complex fertilizer (HUS) of HUS To get reextraction of phosphoric acid from its saturated organic solvent solution containing the di- and monoammonium phosphate, the amounts of which are determined by the formulas: M 1 / (1 + K) W - 2 and mg K / (1 + K) W 1, where M, and M - the number, respectively the mono- and diammonium phosphate, mol / mol 0, W - output aqueous reextract as HUS, The invention relates to the production of liquid complex fertilizer (HUS) of phosphate raw material used in agriculture in Qual stve efficient and economic fertilizers The closest in technical essence and attainable result is a method for preparing HCS comprising phosphoric acid, extraction with an organic solvent and its re0, 05-0,17 parts by weight (m0ch.), K - molar ratio of di- and mono - ammonium phosphate in HUS, 1.2-1.9, separating the resulting aqueous reextract on Retur and the product, the amount of which is 0.05 0,17m.ch. reextract by treatment with ammonia retour return it to reekstraktsik 0 When this flow ratio is reextracted solution and the organic solvent is determined by the formula P (0,279 (Mt. + Vi) 4- 0.028). (H3P04) ftf, r, where () org - the concentration of phosphoric acid in an organic solvent mol / kg of solvent, and the amount of aqueous reextract outputted as HUS is determined by the formula, (M040) t W 1/1 + (M , + M). According to the present invention was prepared with the sum HCS nutrients N n-, .ravnoy 34,1-37%, the ammonia flow rate is 0,369-0,395 kg / kg, r 2 z0p. f BACKGROUND tabl0 1, 1-yl. ; extraction at 80-110 & amp; deg; C ammonia at P2Off0pr / NH weight ratio)
机译:本发明涉及HUS的液体复合肥料(HUS)的生产,以从其含有磷酸二铵和一铵的饱和有机溶剂溶液中反萃取磷酸,其量由下式确定:M 1 /(1 + K)W-2和mg K /(1 + K)W 1,其中M和M-分别为磷酸一铵和二铵的数量,mol / mol 0,W-作为HUS再输出水,本发明与高效,经济的优质肥料中用于农业的磷酸盐原料的液态复合肥料的生产有关。技术实质和可达到的结果最接近的是一种制备包含磷酸的HCS的方法,用有机溶剂萃取及其方法。 re0,05-0,17重量份(摩尔),K-磷酸二铵和单铵在HUS中的摩尔比为1.2-1.9,分离所得的Retur水溶液和产物,其量为0.05 0.17m.ch.通过氨水再处理进行再萃取,将其返回到reekstraktsik0。当再萃取该流量比的溶液,并且有机溶剂由公式P(0,279(Mt. + Vi)4- 0.028)确定时。 (H3PO4)ftf,r,其中()org-有机溶剂中磷酸的浓度mol / kg溶剂,以及以HUS形式输出的含水再提取物的量由下式确定:(M040)t W 1/1 +(M,+ M)。根据本发明,用总的HCS养分N n-,nv-34.1-37%制备,氨气流速为0,369-0,395 kg / kg,r 2 z0p。 f背景表10、1-yl。 ;在80-110& amp;提取;度P2Off0pr / NH重量比下的C氨)

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