Method for producing monoammonium phosphate and coproducing N-P binary compound fertilizer by using wet-process phosphoric acid

A technology of monoammonium phosphate and wet-process phosphoric acid, which is applied in the application, fertilization device, fertilizer mixture and other directions, can solve the problems of limited slurry source, long process flow and low level, and achieve reliable control of process indicators, improve economic benefits, The effect of simple process flow

Active Publication Date: 2013-01-09
HUBEI SANNING CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The traditional method of producing industrial monoammonium phosphate in my country uses thermal acid as raw material, and the production cost is high. In recent years, the slurry purification method represented by Sichuan University (wet acid of high-grade phosphate rock) Some progress has been made, but the production scale is relatively small, the source of slurry (raw acid) is limited, and its production rate (the ratio of industrial grade to fertilizer grade is 1:6-10, that is, every ton of industrial grade monoammonium phosphate is produced at the same time Fertilizer-grade monoammonium phosphate (6-10 tons) is not high, and it is difficult to promote industrialization
[0004] According to this situation, many related enterprises in the phosphorus chemical industry and some colleges and universities and research institutions are actively carrying out technical research on industrial monoammonium phosphate, and have achieved some results, which can be summarized into the following categories: First, use wet-process phosphoric acid The main fertilizer cascade produces industrial-grade monoammonium phosphate, and about 1 ton of fertilizer-grade monoammonium phosphate produces 50-100 kg of industrial-grade monoammonium phosphate as a by-product. Obviously, co-production of industrial-grade ind

Method used

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  • Method for producing monoammonium phosphate and coproducing N-P binary compound fertilizer by using wet-process phosphoric acid

Examples

Experimental program
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Effect test

Embodiment 1

[0025] A method for producing monoammonium phosphate and co-producing N-P binary compound fertilizer with wet-process phosphoric acid,

[0026] (1) Set the weight concentration to 20-25%P 2 o 5 Concentrate the dilute phosphoric acid to remove impurities, concentrate to 46-48%, then add a sedimentation agent to settle and remove impurities, and then dilute the phosphoric acid after removal to 20-25% with process water; or directly use phosphoric acid above 46-48% After adding a settling agent to settle and remove impurities, dilute the process water to 20-25%, and send the slag acid to the slag-slurry mixing tank;

[0027] (2) Pump the diluted phosphoric acid obtained in step (1) to the ammoniation reactor, control the degree of neutralization to 1.01-1.04, and conduct a neutralization reaction with ammonia gas at a temperature of 105-115°C, and the slurry after neutralization Naturally clarified in the slurry clarification tank, the supernatant overflows to the secondary neu...

Embodiment 2

[0037] Concentrate 20-25% of dilute phosphoric acid by using waste heat steam produced by the sulfonic acid plant and self-generated electricity through the concentration device, remove part of the fluorine-containing compounds and most impurities during concentration, and pump it in after the acid concentration reaches 46-48% by weight In the clarification tank, after adding a settling agent to settle and remove impurities, the settling agent is polyacrylamide or similar additives with the same function, and the amount added is 1 / 1000 to 5 / 1000 in terms of volume ratio; after the settlement is completed, use The process water is diluted to 20-25%. The process water refers to the secondary steam condensed water of the concentration system. The slag acid is sent to the slurry mixing tank, and the adjusted dilute acid is pumped into the ammoniation reactor to complete the primary neutralization with ammonia gas. Control the degree of neutralization of the slurry to be 1.01 to 1.0...

Embodiment 3

[0039]Use more than 48% phosphoric acid to settle and remove impurities with a sedimentation agent, then dilute to 20-25% with process water, send the slag acid to the slurry mixing tank, and pump the adjusted dilute acid into the ammoniation reactor to complete one-time neutralization with ammonia gas And, the degree of neutralization of the slurry is controlled to be 1.01-1.04, and the temperature is 105-115°C. After the primary neutralization slurry is filtered by the plate and frame filter, the filtrate enters the secondary neutralization tank, and dilute acid is added to the tank to control its pH value from 4.4 to 4.6, and the secondary neutralization slurry is clarified and filtered, and the filtrate is concentrated After the system is concentrated, it is cooled and crystallized, and the crystallization slurry is centrifuged, and the crystals obtained by the centrifugation are dried in a vibrating fluidized bed, which is the finished product of industrial grade monoammon...

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Abstract

The invention discloses a method for producing monoammonium phosphate and coproducing an N-P binary compound fertilizer by using wet-process phosphoric acid. According to the method, wet-process phosphoric acid prepared from low-grade phosphate ores is used as a raw material. The method comprises the following steps: concentrating and setting the wet-process phosphoric acid to remove impurities; diluting with process water; neutralizing with ammonia twice; filtering twice; concentrating; cooling for crystallization; centrifugally separating; drying to obtain the industrial grade monoammonium phosphate finished product; and mixing acid sludge, the centrifugalized mother liquor, residue and the flushing fluid in a slurry mixing tank, performing spray drying to obtain the N-P binary compound fertilizer. According to the method, wet-process phosphoric acid and gaseous ammonia are directly used as raw materials and the existing related devices in the phosphoric acid industry and resources such as waste heat steam and self power can be utilized, thus the yield of industrial grade monoammonium phosphate can be increased, the output of the byproduct N-P binary compound fertilizer can be reduced, the production cost of industrial grade monoammonium phosphate can be greatly reduced, the industry scale can be enlarged, the adaptability of the equipment can be enhanced, the market demands can be met, the stepped comprehensive utilization of the phosphorus resource can be realized and the economic benefit is higher.

Description

technical field [0001] The invention belongs to the technical field of preparation of phosphorus chemical products, and relates to the production of monoammonium phosphate, in particular to a method for producing industrial-grade monoammonium phosphate with wet-process phosphoric acid and co-producing N-P binary compound fertilizer. Background technique [0002] Industrial monoammonium phosphate is mainly used as drip irrigation fertilizer, and can also be used as flame retardant for paper, plastic, rubber, paint, dry powder fire extinguishing agent, analytical reagent, feed, wastewater, metal treatment, etc. The market prospect is extremely broad. The annual industrial monoammonium phosphate consumption in the world is more than 10 million tons, and it is growing at a rate of more than 4%. [0003] The traditional method of producing industrial monoammonium phosphate in my country uses thermal acid as raw material, and the production cost is high. In recent years, the slurr...

Claims

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Application Information

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IPC IPC(8): C05G1/00
CPCY02P20/129
Inventor 李万清肖林波蒋鑫华
Owner HUBEI SANNING CHEM
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