Method for producing phosphoric acid by decomposing low-grade phosphate rock with wet-process phosphoric acid

A wet-process phosphoric acid, low-grade technology, applied in the direction of phosphoric acid, phosphorus oxyacids, etc., can solve the problems of high impurity content of acid insoluble matter, difficulty in comprehensive utilization, complex reaction, etc., to simplify the process of phosphorus enrichment and improve the utilization value , The effect of simple process

Inactive Publication Date: 2013-07-24
成都川科化工有限公司
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Problems solved by technology

[0004] One of the main characteristics of low-grade phosphate rock is that the content of acid-insoluble impurities is particularly high. When phosphoric acid is produced by traditional phosphoric acid production methods, almost all of it enters phosphogypsum, which greatly reduces the quality of phosphogypsum and makes its comprehensive utilization difficult.
Moreover, due to the high content of impurities in low-grade phosphate rock, phosphate rock often has low decomposition rate and low washing rate. The calcium sulfate package generated by the reaction inactivates the reaction, and the formation of calcium hydrogen phosphate crystals increases the P 2 o 5 The loss of calcium sulfate crystals is difficult to separate, resulting in problems such as poor quality of finished phosphoric acid, resulting in abnormally high production costs and extremely unstable production, so that it is impossible to produce agricultural diammonium phosphate and high-grade agricultural monoammonium phosphate
[0005] Chinese patent CN9110859.7 "Tower Type Wet Process Phosphoric Acid Production Method and Equipment" mentions that medium and low-grade phosphate rock can be used as raw material to produce wet process phosphoric acid, but the grade of phosphate rock used is P 2 o 5 ≧25%, the range of available medium and low-grade phosphate rock is narrow; this method directly enters the mixed slurry of phosphate rock powder and circulating phosphoric acid into the extraction tower to react with sulfuric acid, and does not separate the impurities in phosphate rock from phosphogypsum come; and use concentrated sulfuric acid as the extractant, resulting in local SO 4 2- High concentration makes the reaction incomplete
[0006] Chinese patent 200510022547.2 "Method for producing wet-process phosphoric acid using medium and low-grade phosphate rock" also mentions that its method can use medium- and low-grade phosphate rock as raw material to produce wet-process phosphoric acid, but the grade of the phosphate rock used is P 2 o 5 %: 18~26%, and require MgO≦2.0wt%, Fe 2 o 3 +Al 2 o 3 ≦3.5wt%; it has strict requirements on the impurity content of phosphate rock, and at the same time, the process is complicated, the reaction is complicated, and the two-stage multi-stage reaction makes the cost high and does not have industrial universality; the method adopts multi-stage countercurrent extraction, and the operation The process is long and the requirements for production equipment are high; at the same time, there is no washing of residue and gypsum and the use of washing water, and the industrialization of resource technology has not been realized.

Method used

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  • Method for producing phosphoric acid by decomposing low-grade phosphate rock with wet-process phosphoric acid

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Effect test

Embodiment 1

[0034] A method for producing phosphoric acid by using wet-process phosphoric acid to decompose low-grade phosphate rock comprises the following steps:

[0035] Step 1: Use low-grade phosphate rock (P 2 o 5 =15.12wt%, CaO=39.67wt%, MgO=3.80wt%, Fe 2 o 3 =1.52 wt%, Al 2 o 3 =1.33 wt%) to prepare phosphate rock slurry, and then with phosphoric acid (P 2 o 5=27.63wt%) for a one-step reaction, add additives, react at a temperature of 42°C to 50°C for 3 hours, the liquid-solid ratio in the extraction slurry = 27, add polyacrylamide 20ppm, modified polyacrylamide 10ppm, Polymerized ferrous sulfate 20ppm, the extraction clear liquid and filter residue were obtained through separation I operation, and the extraction rate was 94.8%;

[0036] Step 2: Add 1 part of the extraction clear liquid and 1.20 times the calculated amount of sulfuric acid into a special reactor, sulfuric acid = 96wt%, and carry out a two-step reaction. The temperature is maintained at 80°C to 85°C, and the ...

Embodiment 2

[0039] A method for producing phosphoric acid by using wet-process phosphoric acid to decompose low-grade phosphate rock comprises the following steps:

[0040] Step 1: Use low-grade phosphate rock (P 2 o 5 =18.95wt%, CaO=42.31wt%, MgO=1.52wt%, Fe 2 o 3 =1.47 wt%, Al 2 o 3 =1.28wt%) to prepare phosphate rock slurry, and then with phosphoric acid (P 2 o 5 =35.94wt%) for one-step reaction, adding additives, reacting for 8 hours at a temperature of 35 ° C ~ 42 ° C, the liquid-solid ratio in the extraction slurry = 25, after the reaction is completed, add polyacrylamide 10ppm, polyaluminum chloride 20ppm, through Separation I operation to obtain the extract clear liquid and filter residue, the extraction rate is 96.43%;

[0041] Step 2: Add 1 part of the extraction clear liquid and 1.16 times the calculated amount of sulfuric acid into a special reactor, sulfuric acid = 97wt%, and carry out a two-step reaction. The temperature is maintained at 85°C to 90°C, and the reaction...

Embodiment 3

[0044] A method for producing phosphoric acid by using wet-process phosphoric acid to decompose low-grade phosphate rock comprises the following steps:

[0045] Step 1: Use low-grade phosphate rock (P 2 o 5 =17.24wt%, CaO=40.59wt%, MgO=2.25wt%, Fe 2 o 3 =1.96 wt%, Al 2 o 3 =0.93wt%) to prepare phosphate rock slurry, and then with phosphoric acid (P 2 o 5 =26.59wt%) for a one-step reaction, add additives, react for 6 hours at a temperature of 48 ° C ~ 57 ° C, the liquid-solid ratio in the extraction slurry = 22, after the reaction is completed, add polyacrylamide 2ppm, and obtain the extraction liquid by separation Ⅰ operation Liquid and filter residue, the extraction rate is 95.28%;

[0046] Step 2: Add 1 part of the extraction clear liquid and 1.09 times the calculated amount of sulfuric acid into a special reactor, sulfuric acid = 98wt%, and carry out a two-step reaction. The temperature is maintained at 90°C to 95°C, and the reaction is complete for 5 hours. Add 2pp...

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Abstract

The invention discloses a method for producing phosphoric acid by decomposing a low-grade phosphate rock with wet-process phosphoric acid, which is characterized by using a two-step reaction, additive addition and separation. The method comprises the following steps: step one, decomposing the low-grade phosphate rock using phosphoric acid in an extraction tank, and removing residues through solid-liquid separation, so as to obtain a clear solution; and step two, reacting the extracted clear solution with sulfuric acid in a reactor to generate crystals of calcium sulfate dehydrate (phosphogypsum) and the phosphoric acid solution, so as to obtain the phosphoric acid solution and a phosphogypsum after solid-liquid separation, concentrating the phosphoric acid solution, thus finally partial concentrated phosphoric acid solution is returned to continuously decompose the phosphate rock, and partial phosphoric acid solution is output as finished products. By using the method, the relatively high quality phosphoric acid can be obtained and the yield of phosphoric acid is high, thus the method has wide prospect in industrial application; and at the same time, a white plaster as the by-product of method also has wide application value.

Description

technical field [0001] The invention relates to a method for producing phosphoric acid by using wet-process phosphoric acid to decompose low-grade phosphate rock, and belongs to the field of wet-process phosphoric acid production. Background technique [0002] Wet-process phosphoric acid is one of the important methods for preparing phosphoric acid, and it is also the basic product of the phosphorus chemical industry. It is widely used in the phosphate industry and the phosphorus compound fertilizer industry, and has a large demand. The production process of wet-process phosphoric acid is mainly to produce phosphoric acid by decomposing phosphate rock with inorganic acid (mainly sulfuric acid). The total amount of phosphate rock resources in my country is close to 50 billion tons, and P in phosphate rock 2 o 5 The rich ore with a content of more than 30% only accounts for about 8% of the reserves, and most of them are low-grade ores. 2 o 5 The average grade is only 16.85...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B25/22
Inventor 唐建华马刚张海
Owner 成都川科化工有限公司
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