Hydrochloric acid process of producing feed level calcium diphosphate and gypsum coproduct

A technology of calcium hydrogen phosphate and hydrochloric acid method, which is applied in the forming or processing of animal feed, animal feed, animal feed, etc. It can solve the problems of uneconomical economy, high product cost, and large ammonia consumption, and achieve the improvement of comprehensive economic benefits , advanced production technology, the effect of reducing environmental pollution

A technology of calcium hydrogen phosphate and hydrochloric acid method, which is applied in the forming or processing of animal feed, animal feed, animal feed, etc. It can solve the problems of uneconomical economy, high product cost, and large ammonia consumption, and achieve the improvement of comprehensive economic benefits , advanced production technology, the effect of reducing environmental pollution

CN100402418CInactive Publication Date: 2008-07-16自贡鸿鹤化工股份有限公司

Examples

Experimental program
Comparison scheme
Effect test

Embodiment

[0016] A. Acid hydrolysis and sedimentation separation: first, the calcium water (or / and clear water) after the secondary neutralization treatment will be used to prepare 60% of the solid content, P in the phosphate rock powder 2 o 5 2m pulp with a content of 33% 3 Put it into the acidolysis tank with a stirrer, under stirring at 14m 3 The flow rate of / h added concentration is 125g / L hydrochloric acid 7.3m 3 (the dilute hydrochloric acid 6.3m that this embodiment reclaims by H 3 and 1m 3 Concentration of 20% of the industrial hydrochloric acid), after 60 minutes of reaction, a section of the sedimentation concentrate obtained by neutralization 1.5m 3 Add 50Kg of sodium sulfide aqueous solution with a concentration of 2%, stir and react for 5 minutes, then add 50Kg of an aqueous solution of polyacrylamide with a concentration of 0.5% and a molecular weight of 60,000, stir and mix evenly, and then set aside to settle and separate the acid solution;

[0017] B. Filtration: ...

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Abstract

The hydrochloric acid process of producing feed level calcium diphosphate and gypsum coproduct includes the steps of: acidolysis and depositing separation, filtering, the first section neutralization, the second section neutralization, preparing feed level calcium diphosphate, purification and concentrating calcium solution, synthesizing gypsum, recovering hydrochloric acid, and preparing gypsum product. The process adopts phosphate rock powder and sulfuric acid as main material, utilizes hydrochloric acid to acidolyze phosphate rock powder, recovers hydrochloric acid for reuse, controls the leaching out of fluorine and promotes it to precipitate for separating out, and has increased calcium solution purification step. The process has the features of high quality of feed level calcium diphosphate, P2O5 yield up to 90 %, production of gypsum with wide use, less environmental pollution and raised comprehensive utility.

Description

technical field [0001] The invention belongs to chemical production, and relates to a method for producing feed calcium hydrogen phosphate and co-producing gypsum by adopting a hydrochloric acid method. Background technique [0002] The production methods of conventional wet feed calcium hydrogen phosphate include sulfuric acid method and hydrochloric acid method, with the former being the main method. Although the sulfuric acid method has the characteristics of low production cost, easy access to the main raw material sulfuric acid, and large-scale industrial production; but there is defluorination and a large amount of phosphogypsum waste generated in the production (each ton of calcium feed product will produce 2.5 tons of phosphogypsum ) processing difficulty is big, and processing cost is high, and the gained calcium hydrogen phosphate causes the product phosphorus content on the low side because of containing a small amount of calcium sulfate, and can not utilize the d...

Claims

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Application Information

Patent Timeline
16 Jul 2008
Publication
CN100402418C
IPC
C01B25/32; C01F11/46; A23K1/00; A23K20/24; A23K20/26; A23K40/00
Inventors
王兆华; 陈欣