Method for producing broad-concentration phosphoric acid and clean plaster by middle-low grade phosphorus ore wet process

A low-grade, phosphoric acid technology, applied in phosphoric acid, phosphorus oxyacid, calcium/strontium/barium sulfate, etc., can solve the problems of difficult beneficiation, large phosphorus loss, large equipment, etc. rate increase effect

Inactive Publication Date: 2011-04-06
SICHUAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the first two processes have passed the pilot test, these processes are based on the improvement of the traditional dihydrate process, and the obtained phosphoric acid is 27%P 2 o 5 The low concentration of phosphoric acid below, the gypsum obtained is of high quality, but it is still dihydrate gypsum. If it is to be used as building gypsum, it needs to be calcined, and the energy consumption is high; at the same time, the device is large and the production capacity is limited.
[0003] China's phosphate rock resources are becoming increasingly depleted. Quite a few low- and medium-grade phosphate rocks have small crystal grains, making mineral processing extremely difficult. It is difficult to use the existing wet process. The content of impurities is high, the reactivity is poor, and the solids are seriously fouled in the filtration. The obtained phosphogypsum not only has a high liquid content, but also has a large loss of phosphorus, and is difficult to use.
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  • Method for producing broad-concentration phosphoric acid and clean plaster by middle-low grade phosphorus ore wet process
  • Method for producing broad-concentration phosphoric acid and clean plaster by middle-low grade phosphorus ore wet process
  • Method for producing broad-concentration phosphoric acid and clean plaster by middle-low grade phosphorus ore wet process

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0034] Example 1:

[0035] The process flow of this embodiment is as attached figure 2 Shown. P of a phosphate rock 2 O 5 The grade is 16-18%, and the phosphate rock is processed into 80% powder with a 0.125mm (120 mesh) screen. Add 1000 parts of phosphate rock powder to semi-water tank R1 for acid hydrolysis. The operating conditions of acid hydrolysis reaction are: temperature 95~105℃, liquid-solid ratio 4-6, phosphoric acid concentration 37~42%P 2 O 5 , The reaction time is 1 to 3 hours. The acid hydrolyzed slurry after the reaction enters the separator S1 for solid-liquid separation, and the obtained clear liquid enters the crystallization tank R2, and sulfuric acid is added for the crystallization reaction. The crystallization operation conditions are: control SO 3 The concentration is 15-65g / L, the temperature is 100-110°C, and the crystallization reaction is 3-6 hours. After full crystallization reaction, the slurry is separated by vacuum filter S2 to separate semi-aque...

Example Embodiment

[0036] Example 2:

[0037] The process flow of this embodiment is shown in FIG. 3. The grade of a certain phosphate rock is 22~28WT%P 2 O 5 . The particle size of the phosphate rock powder is 80% through a 0.075mm (200 mesh) screen. Add 1000 parts of phosphate rock powder and enter the semi-water tank R1 for acid hydrolysis. Add sulfuric acid during the acid hydrolysis process. The acid hydrolysis reaction operating conditions are: temperature 95~105℃, liquid-solid ratio 5-8, phosphoric acid concentration 40~45WT% P 2 O 5 , Control SO 3 The concentration is 10-20g / L, and the reaction time is 1-2 hours. The acid hydrolyzed slurry after the reaction enters the separator S1 for solid-liquid separation. The obtained clear liquid enters the crystallization tank R2, and sulfuric acid is added to carry out the crystallization reaction. The crystallization reaction operating conditions are: control SO 3 The concentration is 10~45g / L, the temperature is 100~110℃, and the crystallizatio...

Example Embodiment

[0038] Example 3:

[0039] The process flow of this embodiment is as attached figure 2 Shown. P of a phosphate rock 2 O 5 The grade is 16-18%, and the phosphate rock is processed into 80% powder with a 0.125mm (120 mesh) screen. Add 1000 parts of phosphate rock powder to semi-water tank R1 for acidolysis. The operating conditions of acidolysis reaction are: temperature 95~105℃, liquid-solid ratio 4-7, phosphoric acid concentration 37~42%P 2 O 5 , The reaction time is 1 to 3 hours. The acid hydrolyzed slurry after the reaction enters the separator S1 to separate the solid phase. The obtained clear liquid enters the crystallization tank R2, and sulfuric acid is added to carry out the crystallization reaction. The crystallization reaction operating conditions are: control SO 3 The concentration is 15-65g / L, the temperature is 70-85°C, and the crystallization reaction is 2-6 hours. After full crystallization reaction, 628~723 parts of dihydrate white gypsum are separated from the ...

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Abstract

The invention discloses a method for producing broad-concentration phosphoric acid and clean plaster by a middle-low grade phosphorus ore wet process. The method comprises the following main procedures: (1) adding powder phosphorus ore and phosphoric acid to a semi-acid hydrolysis reaction tank for acid hydrolysis reaction at 95-105 DEG C, and carrying out solid-liquid separation on the slurry obtained by acid hydrolysis after full acid hydrolysis reaction; (2) transferring phosphoric acid clear liquid separated in procedure (1) into a crystallization tank, adding sulfuric acid and carrying out crystallization at 70-110 DEG C, and carrying out solid-liquid separation after full reaction, wherein, a liquid phase is the phosphoric acid to be prepared and a solid phase is the functional clean plaster to be prepared; and (3) transferring residue slurry separated in procedure (1) into a secondary acid hydrolysis reaction tank, adding water, carrying out secondary acid hydrolysis and recrystallization on the residue slurry at 65-80 DEG C, carrying out solid-liquid separation after full reaction, transferring the obtained separation liquid into procedure (2), and discharging the separated solid residues. The method of the invention has the characteristics of high production efficiency, high phosphorus resource recovery rate, strong production capacity, good economic benefit, strong operability and the like.

Description

technical field [0001] The invention relates to the development and utilization of low- and medium-grade phosphate rocks, and more specifically relates to a method for producing phosphoric acid with a wide concentration range and functional clean gypsum by using a wet method using low- and medium-grade phosphate rocks as raw materials. Background technique: [0002] With the gradual depletion of phosphate rock resources in the world, all countries are very concerned about the development and utilization of low-grade phosphate rock. Many scholars in China have carried out in-depth research on the wet production of medium and low-grade phosphate rock. For example, the research group of Professor Liu Daijun from the Department of Chemical Engineering of Sichuan University has long been committed to the research on the wet production of medium and low-grade phosphate rock, and has achieved various results. Research results, such as the two-stage dihydration process for high-sili...

Claims

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Application Information

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IPC IPC(8): C01B25/22C01F11/46
Inventor 刘代俊陈小林刘芊宏
Owner SICHUAN UNIV
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