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Phosphogypsum processing method

A processing method and phosphogypsum technology are applied in the field of phosphorus chemical industry to achieve the effect of realizing recycling, reducing environmental protection pressure and realizing comprehensive utilization of resources

Active Publication Date: 2014-12-17
YUNNAN PHOSPHATE CHEM GROUP CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Sichuan University Master Thesis, 2004), Potassium Sulfate (Liu Daijun, Li Jun, Zhong Benhe, Zhang Yunxiang. A new process for producing potassium sulfate by phosphogypsum conversion method [J]. Phosphate Fertilizer and Compound Fertilizer, 1996, 3: 17-19), etc. , but it is used to prepare magnesium sulfate, especially the method for preparing magnesium sulfate in combination with carbon dioxide tail gas has not been reported
[0009]In summary, regarding the use of carbon dioxide generated in the production process of calcium feed to carbonize active magnesium oxide to process phosphogypsum to prepare magnesium sulfate and use yellow phosphorus tail gas to reduce magnesium sulfate to prepare high The technical scheme of pure magnesium oxide has not been reported yet

Method used

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  • Phosphogypsum processing method

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Experimental program
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Effect test

Embodiment 1

[0026] Activated magnesia is carbonized with carbon dioxide in a carbonization tower, and then solid-liquid separation is performed to obtain liquid-phase heavy magnesium water, and then phosphogypsum and heavy magnesium water are subjected to metathesis reaction to obtain liquid-phase magnesium sulfate solution after solid-liquid separation, and then magnesium sulfate solution Evaporate and crystallize to obtain magnesium sulfate heptahydrate crystals, and finally reduce and thermally decompose the magnesium sulfate heptahydrate crystals with 1.2 times the molar amount of carbon monoxide to obtain sulfur dioxide and high-purity magnesium oxide.

[0027] Described carbon dioxide, its volume percentage is 50-90%.

[0028] The activated magnesia has an activity of 60%-90% using the hydration method.

[0029] The carbon monoxide is 60-95% by volume.

[0030] Through the above operations, the purity of the obtained high-purity magnesium oxide is 98-99.5%.

Embodiment 2

[0032] Activated magnesia is carbonized with carbon dioxide in a carbonization tower, and then solid-liquid separation is performed to obtain liquid-phase heavy magnesium water, and then phosphogypsum and heavy magnesium water are subjected to metathesis reaction to obtain liquid-phase magnesium sulfate solution after solid-liquid separation, and then magnesium sulfate solution Evaporate and crystallize to obtain magnesium sulfate heptahydrate crystals, and finally reduce and thermally decompose the magnesium sulfate heptahydrate crystals with 2 times the molar amount of carbon monoxide to obtain sulfur dioxide and high-purity magnesium oxide.

[0033] Described carbon dioxide, its volume percentage is 80%.

[0034] The activated magnesium oxide has an activity of 85% using the hydration method.

[0035] The carbon monoxide is 90% by volume.

[0036] Through the above operations, the purity of the obtained high-purity magnesium oxide is 99.2%.

Embodiment 3

[0038] Activated magnesia is carbonized with carbon dioxide in a carbonization tower, and then solid-liquid separation is performed to obtain liquid-phase heavy magnesium water, and then phosphogypsum and heavy magnesium water are subjected to metathesis reaction to obtain liquid-phase magnesium sulfate solution after solid-liquid separation, and then magnesium sulfate solution Evaporate and crystallize to obtain magnesium sulfate heptahydrate crystals, and finally reduce and thermally decompose the magnesium sulfate heptahydrate crystals with 1.5 times the molar amount of carbon monoxide to obtain sulfur dioxide and high-purity magnesium oxide.

[0039] Described carbon dioxide, its volume percentage is 50%.

[0040] The activated magnesium oxide has an activity of 65% using the hydration method.

[0041] The carbon monoxide is 60% by volume.

[0042] Through the above operations, the purity of the obtained high-purity magnesium oxide is 98.1%.

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Abstract

The invention relates to a phosphogypsum processing method. The method is characterized in that: active magnesium oxide is carbonized for 0.5-2h by using carbon dioxide under a temperature of 20-40 DEG C in a carbonization tower; solid-liquid separation is carried out, such that liquid-phase heavy magnesium water is obtained; phosphogypsum and the heavy magnesium water are subjected to a metathesis reaction for 0.5-2h under a temperature of 20-60 DEG C; solid-liquid separation is carried out, such that a liquid-phase magnesium sulfate solution is obtained, wherein the ratio of the amount of sulfate in phosphogypsum to the amount of magnesium ion in the heavy magnesium water is that SO4<2->:Mg<2+>=1-2:1; the magnesium sulfate solution is subjected to evaporation crystallization, such that magnesium sulfate heptahydrate crystals are obtained; the magnesium sulfate heptahydrate crystals are subjected to reduction thermal decomposition under a temperature of 600-900 DEG C by using carbon monoxide with a 1.2-2 time molar amount, such that sulfur dioxide and high-purity magnesium oxide are obtained. Raw materials adopted by the invention are sourced from industrial waste slag or industrial tail gas. The processing process is simple, no pollution is caused, preparation efficiency is high, cost is low, and good economic benefit is provided. The method is an ideal industrial waste recycling method.

Description

technical field [0001] The invention relates to a processing method of phosphogypsum, which belongs to the field of phosphorus chemical industry. This processing method is mainly used for the reuse of phosphogypsum, the production of magnesium sulfate and the production of high-purity magnesium oxide. Background technique [0002] Phosphogypsum is a kind of solid waste produced in the process of wet phosphate fertilizer production. It mainly contains gypsum, phosphorus, fluorine, silicon dioxide and a certain amount of water, and it is easy to cause environmental pollution during the stacking process. There are nearly 20 million tons of phosphogypsum discharged in my country every year, and more than 100 million tons have been stockpiled over the years. At present, there are many plans for the utilization of phosphogypsum, such as building materials and the production of ammonium sulfate. However, due to the relatively concentrated distribution of phosphogypsum and the sma...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01F5/12
Inventor 李耀基陆伟才张晖方世祥张勇李小双阳杨何宾宾沈潜王孟来王建勇李云驹
Owner YUNNAN PHOSPHATE CHEM GROUP CORP
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