Method for producing fertilizer monopotassium phosphate by phosphoric acid by semi-hydrated process and wet process

A technology of potassium dihydrogen phosphate and wet-process phosphoric acid, which is applied in the field of phosphorus chemical industry, can solve the problems of serious equipment corrosion, high production cost, short supply of potassium dihydrogen phosphate, etc., and achieves the effect of reducing water consumption and improving yield

Active Publication Date: 2016-07-27
KUNMING CHUAN JINNUO CHEM IND
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Potassium dihydrogen phosphate is a high-quality high-quality phosphorus-potassium compound fertilizer. The traditional process generally uses neutralization and double decomposition. The neutralization process is simple, but the cost of raw materials used is expensive, and it is difficult to produce potassium dihydrogen phosphate for agriculture. Promoted in China; the metathesis method mainly uses potassium chloride and phosphoric acid to carry out the metathesis reaction, and the reaction can be carried out by removing the hydrogen chloride gas generated by the reaction. This method has pr

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  • Method for producing fertilizer monopotassium phosphate by phosphoric acid by semi-hydrated process and wet process
  • Method for producing fertilizer monopotassium phosphate by phosphoric acid by semi-hydrated process and wet process
  • Method for producing fertilizer monopotassium phosphate by phosphoric acid by semi-hydrated process and wet process

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Example Embodiment

[0021] Example 1:

[0022] Add semi-aqueous wet-process phosphoric acid to phosphate rock powder for desulfurization, the addition ratio is 1:2 according to the molar ratio of sulfur and calcium oxide, and the reaction time is 1.5 hours. The reaction temperature is 50°C. The slurry after desulfurization is filtered, and the filter residue is sent to the phosphoric acid system. Therefore, the filtrate enters the primary neutralization tank, and the concentration is 15% potassium hydroxide is added for neutralization, and the pH value of the primary neutralization slurry is adjusted to 2.2. The reaction time 1.5 hours, the reaction temperature is 60°C, the primary neutralization slurry is filtered, the filter residue is added to the nitrogen, phosphorus and potassium compound fertilizer, the filtrate enters the secondary neutralization tank, and the concentration is 15% potassium hydroxide is added for secondary neutralization, and the secondary neutralization is adjusted. The p...

Example Embodiment

[0025] Example 2:

[0026] Add semi-aqueous wet-process phosphoric acid to phosphate rock powder for desulfurization, the addition ratio is 1:3 according to the molar ratio of sulfur to calcium oxide, and the reaction time is 1.5 hours. The reaction temperature is 50°C. The slurry after desulfurization is filtered, and the filter residue is sent to the phosphoric acid system. Therefore, the filtrate enters the primary neutralization tank, and the concentration is 15% potassium hydroxide is added for neutralization, and the pH value of the primary neutralization slurry is adjusted to 2.2. The reaction time 1.5 hours, the reaction temperature is 30°C, the primary neutralization slurry is filtered, the filter residue is added to the nitrogen, phosphorus and potassium compound fertilizer, the filtrate enters the secondary neutralization tank, and the concentration is 15% potassium hydroxide is added for secondary neutralization, and the secondary neutralization is adjusted. The pH...

Example Embodiment

[0028] Example 3:

[0029]

[0030] Add semi-aqueous wet-process phosphoric acid to phosphate rock powder for desulfurization, the addition ratio is 1:2.5 according to the molar ratio of sulfur to calcium oxide, and the reaction time is 1.5 hours. The reaction temperature is 50°C. The slurry after desulfurization is filtered, and the filter residue is sent to the phosphoric acid system. Therefore, the filtrate enters the primary neutralization tank, and the concentration is 15% potassium hydroxide is added for neutralization, and the pH value of the primary neutralization slurry is adjusted to 2.2. The reaction time 1.5 hours, the reaction temperature is 30°C, the primary neutralization slurry is filtered, the filter residue is added to the nitrogen, phosphorus and potassium compound fertilizer, the filtrate enters the secondary neutralization tank, and the concentration is 15% potassium hydroxide is added for secondary neutralization, and the secondary neutralization is adj...

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Abstract

The invention discloses a method for producing a fertilizer monopotassium phosphate by phosphoric acid by a semi-hydrated process and a wet process. The method is characterized by comprising the following process steps of: adding phosphoric acid by the semi-hydrated process and the wet process into powdered rock phosphate to carry out desulfurization, filtering desulfurized slurry, feeding filter residues into a phosphoric acid system, introducing filtrate into a primary neutralizing tank, adding potassium hydroxide into the primary neutralizing tank to neutralize the filtrate, and regulating the pH value of the primary neutralized slurry to be 2.0-2.5. The method has the beneficial effects that the phosphoric acid by the semi-hydrated process and the wet process and dry ground phosphorite react for desulfurization, so that SO4<2-> of the phosphoric acid by the semi-hydrated process and the wet process is reduced while 2-5% of CaO is dissolved. Dosage of potassium hydroxide for primary and secondary neutralization and impurity removal can be reduced. Phosphor and potassium are sufficiently utilized, so that the yield of P2O5 is increased; mother liquor subjected to tertiary neutralization and filtration is returned to preparation water of potassium hydroxide subjected to primary and secondary neutralization, so that water consumption in a production process is reduced; and meanwhile, residual phosphor and potassium in the mother liquor are recycled, so that the phosphor and the potassium are sufficiently utilized, and therefore, the yields of the phosphor and the potassium are increased.

Description

technical field [0001] The invention belongs to the field of phosphorus chemical industry, in particular to potassium dihydrogen phosphate (KH 2 PO 4 )Methods. Background technique [0002] Potassium dihydrogen phosphate (KH 2 PO 4 ) is a large branch of phosphate, potassium dihydrogen phosphate is an important product of phosphate, pure potassium dihydrogen phosphate is potassium oxide (K 2 O) 34.60%, phosphorus pentoxide (P 2 o 5 )52.20%. Potassium dihydrogen phosphate is a colorless or white lustrous orthorhombic crystal, soluble in water, showing acidic reaction, insoluble in alcohol. Potassium dihydrogen phosphate is a high-quality high-quality phosphorus-potassium compound fertilizer. The traditional process generally uses neutralization and double decomposition. The neutralization process is simple, but the cost of raw materials used is expensive, and it is difficult to produce potassium dihydrogen phosphate for agriculture. Promoted in China; the metathesis m...

Claims

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Application Information

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IPC IPC(8): C01B25/30C05B7/00
CPCC01B25/301C05B7/00
Inventor 曾润国韦文相
Owner KUNMING CHUAN JINNUO CHEM IND
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