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Method for producing phosphoric acid by-product low-silicon phosphogypsum from high-silicon phosphate rock

A high-silicon phosphate rock and phosphoric acid technology, applied in chemical instruments and methods, phosphorus compounds, calcium/strontium/barium sulfate, etc., can solve the problems of reducing the silicon content of phosphogypsum and high silicon content, so as to reduce investment and improve products Quality, the effect of eliminating environmental problems

Active Publication Date: 2015-11-18
龚家竹
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  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0021] In order to overcome the shortcoming that the silicon content in the by-product phosphogypsum produced by wet-process phosphoric acid from high-silicon phosphate rock is too high, it cannot be used as a resource or has a relatively small range of utilization. A method of producing low-silicon phosphogypsum by-product, the method of producing phosphoric acid by-product low-silicon phosphogypsum from high-silicon phosphate rock, using phosphoric acid to decompose phosphate rock, removing silicon compounds in the phosphate rock, and then using sulfuric acid to precipitate phosphoric acid to decompose phosphate rock to produce Calcium ion compound, which reduces the silicon content in phosphogypsum, does not use the high-cost high-silicon phosphate ore beneficiation method before wet-process phosphoric acid production, nor does it use chemical flotation for phosphogypsum after wet-process phosphoric acid production The method of separating and removing silicon greatly simplifies the silicon removal process, achieves the purpose of saving energy, reducing investment, reducing production costs, increasing production capacity, and increasing the economic benefits of producers, eliminating the fact that high-silicon phosphogypsum cannot be used as a resource and is environmentally friendly. problem

Method used

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  • Method for producing phosphoric acid by-product low-silicon phosphogypsum from high-silicon phosphate rock
  • Method for producing phosphoric acid by-product low-silicon phosphogypsum from high-silicon phosphate rock
  • Method for producing phosphoric acid by-product low-silicon phosphogypsum from high-silicon phosphate rock

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Embodiment 1

[0047] Such as figure 2 As shown, the finely ground high-silicon phosphate rock powder (see Table 1 for the main chemical composition) is put into the decomposition reaction tank D1 at an hourly input rate of 26,717 kg, and is mixed with the thick classifier E3 and the solid-liquid separator. The liquid recycled in F is 247,770 kg per hour for decomposition reaction, the residence time of the reaction material is 20 minutes, and the reaction temperature is 45°C; after the reaction, the material is sent to the continuous sedimentation thick classifier E1 for thick, 3 / 4 thick light phase After entering the decomposition reaction tank D2, 1 / 4 of the thick heavy phase returns to the decomposition reaction tank D1 to continue to react with the circulating liquid. The material entering the decomposition reaction tank D2 continues to undergo decomposition reaction, the residence time is 20 minutes, and the reaction temperature is 40°C; after the reaction, the material is sent to the...

Embodiment 2

[0049] Such as figure 2As shown, the finely ground high-silicon phosphate rock powder (see Table 1 for the main chemical composition) is put into the decomposition reaction tank D1 at an hourly input rate of 53,434 kg, and is mixed with the thick classifier E3 and the solid-liquid separator. The liquid recycled in F is 495,540 kg per hour for decomposition reaction, the residence time of the reaction material is 20 minutes, and the reaction temperature is 45°C; after the reaction, the material is sent to the continuous sedimentation thick classifier E1 for thick classification, 3 / 4 thick classification The light phase enters the decomposition reaction tank D2, and 1 / 4 of the thick and classified heavy phase returns to the decomposition reaction tank D1 to continue to react with the circulating liquid. The material entering the decomposition reaction tank D2 continues to undergo decomposition reaction, the residence time is 20 minutes, and the reaction temperature is 40°C; aft...

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Abstract

The invention discloses a method for producing a byproduct low-silicon ardealite by using high-silicon phosphorite. The method is as follows: high-silicon phosphorite powder enters more than one stage of countercurrent decomposition reaction tank for performing more than one countercurrent decomposition reaction and thickening, wherein the countercurrent decomposition reaction tank is composed of a decomposition reaction tank and a thickening classifier; one part of materials subjected to countercurrent decomposition reaction and thickening enters a sedimentation and crystallization tank and performs sedimentation and crystallization reaction with sulfuric acid to prepare phosphoric acid and low-silicon ardealite, another part of materials enters a solid-liquid separator for performing solid-liquid separation, and another part of materials returns a first-stage decomposition reaction tank and reacts with the high-silicon phosphorite powder. According to the method, the difficulty of too high silicon content in the byproduct ardealite when the phosphoric acid is produced by adopting a wet process is solved, the quality of the byproduct ardealite is improved, the content of the silicon in the ardealite is reduced, the influence factor of developing and applying the ardealite due to silicon content is eliminated, a firm resource foundation is laid for completely utilizing the ardealite, the economic benefit of a producer is increased, and the difficulty of environment protection of piling and treating the ardealite is eliminated.

Description

technical field [0001] The invention relates to a method for producing phosphogypsum by-product of wet-process phosphoric acid, in particular to a method for producing low-silicon phosphogypsum by-product of phosphoric acid from high-silicon phosphate rock. Background technique [0002] In the production of wet-process phosphoric acid, phosphoric acid solution is obtained through metathesis reaction between phosphate rock and sulfuric acid, and the calcium ions and sulfate ions in the phosphate rock crystallize and precipitate gypsum calcium sulfate. Because calcium sulfate comes from phosphorus chemical production, it is customarily called phosphogypsum . Its main production chemical reaction principle is as follows: [0003] Ca 5 F(PO 4 ) 3 +5H 2 SO 4 +10H 2 O→3H 3 PO 4 +5CaSO 4 2H 2 O↓+HF↑ (1) [0004] Some impurities such as iron, aluminum, and magnesium brought from the phosphate rock also participate in the reaction, and most of the generated phosphate rema...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B25/225C01F11/46
Inventor 龚家竹
Owner 龚家竹