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Neutralizing and concentrating device used for monoammonium phosphate production and using method thereof

A technology of monoammonium phosphate and raffinate acid, applied in the direction of phosphate, phosphorus oxyacid, etc.

Active Publication Date: 2018-11-02
YIDU XINGFA CHEM COMPANY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The present invention aims to provide an integrated device for neutralizing and concentrating monoammonium phosphate products using raffinate acid to solve the problem of too high concentration of raffinate acid when using raffinate method to produce monoammonium phosphate products. , it is necessary to reduce the technical difficulties of subsequent production after acid concentration, which can save the steam consumption of slurry concentration in the production of monoammonium phosphate products by slurry method, and save a large amount of steam required for slurry concentration every year, and play a role in energy saving and emission reduction purpose, and at the same time realize the efficient recovery and reuse of raffinate

Method used

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  • Neutralizing and concentrating device used for monoammonium phosphate production and using method thereof

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Embodiment 1

[0025] like figure 1 In, the present invention will be further described in conjunction with accompanying drawing:

[0026] A neutralization and concentration device for the production of monoammonium phosphate, the bottom of the reactor 1 is connected to the steam heat exchanger 9 through the circulation pump 6, the steam heat exchanger 9 is connected to the tubular reactor 12, and the tubular reactor 12 is reacted The slurry circulation pipe 14 is connected to the top of the reactor 1; the upper part of the reactor 1 is provided with a feeding pipe 25 for raffinate; the middle part of the reactor 1 passes through the slurry to the high-pressure pump delivery pipe 24 and is connected with the high-pressure pump 23 and then sent to the powder spraying tower .

[0027] The upper part of the reactor 1 is provided with an overflow pipe 21. The overflow pipe 21 is arranged at the 80-90% liquid level of the reactor 1 tower body. ; Insert the raffinate delivery pipe into the lower...

Embodiment 2

[0032] The process carried out using the device described in Example 1 is as follows:

[0033] Transport the raffinate with 40-44% acid concentration to the reactor tower body 1 through the raffinate delivery pipeline 25, and start the circulation pump 6 when the liquid level gauge 17 shows that the liquid level reaches 30%;

[0034] Intake ammonia through the intake ammonia delivery pipeline 13 to the tubular reactor 12, strengthen sampling analysis, and wait for the degree of neutralization to reach 0.92mol / mol, compare the intake ammonia delivery pipeline 13 inlet ammonia flow rate with the raffinate acid delivery pipeline inlet flow rate Put into automatic interlocking, set the neutralization degree of amino acid ratio to 0.95--1.02mol / mol;

[0035] Sampling and analyzing the specific gravity of the slurry, when the specific gravity is 1.5-1.55, it is not necessary to use its own concentrated steam heat exchanger 9; directly start the high-pressure pump 23 to transport the...

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Abstract

The invention discloses a neutralizing and concentrating device used for monoammonium phosphate production and a using method thereof. Specifically, the bottom of a reactor is connected with a steam heat exchanger through a circulating pump; the steam heat exchanger is connected with a tubular reactor; the tubular reactor is connected with the top of the reactor through a reaction slurry circulating tube; the upper part of the reactor is equipped with an extracted residual acid conveying tube; the middle part of the reactor is connected with a high-pressure pump through a high-pressure pump conveying tube, and the slurry is fed to a powder spraying tower. Extracted residual acid or concentrated phosphoric acid performs neutral reaction with gas ammonium, so that monoammonium phosphate which meets powder-spraying indexes is conveyed to the powder spraying tower through the high-pressure pump to obtain a monoammonium phosphate finished product. When a slurry method is used for producingmonoammonium phosphate from extracted residual acid, concentration of acid needs to be reduced for follow-up production as concentration of the extracted residual acid is too high, so that steam consumption amount of slurry concentration can be reduced while the monoammonium phosphate product is produced through the slurry method; and 43200 tons of steam is saved per year according to the extracted residual acid consumption amount, so that the annular saved steam amount reaches economic benefits of 7.78 millions of yuan.

Description

technical field [0001] The present invention relates to the recycling and utilization of phosphorus resources. Specifically, the raffinate acid produced in the wet-process phosphoric acid refining process is simply mixed with acid (after ensuring that the acid concentration is 40-44%, and the specific gravity is 1.4-1.5). The device reacts with gaseous ammonia to generate monoammonium phosphate slurry, and adjusts its own concentration system according to the actual situation of the slurry to obtain the required monoammonium phosphate slurry and send it to the powder spraying tower to produce monoammonium phosphate products. Background technique [0002] In the production process of wet-process phosphoric acid refining, a large amount of raffinate will be produced, which has high solid content and high sesquioxide. The general treatment method is to use the by-product raffinate to produce monoammonium phosphate by slurry method , because the acid concentration of the raffina...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B25/28
CPCC01B25/28
Inventor 郑光明邹学勇沈维云刘明高杜万保王宗孝陈春雷黄翔翔汪耀兴
Owner YIDU XINGFA CHEM COMPANY
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