Method for producing coarse-grain special mirabilite

A manufacturing method and coarse particle technology, applied in chemical instruments and methods, alkali metal sulfite/sulfite, alkali metal compounds, etc., can solve the problems of particle unevenness, agglomeration, inconvenient use, etc., and achieve particle flow good sex effect

Inactive Publication Date: 2009-05-13
四川省川眉芒硝有限责任公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The traditional nitrate production process is to evaporate and concentrate the nitrate water to form a supersaturated solution of thenardite, then use centrifugation to separate the thenardite crystals, and then dry the thenardite crystals to obtain the thenardite. The particles are very uneven, and the resulting Glauber's salt will form agglomerates after being stored for a certain period of time, which will cause a lot of inconvenience in use
[0007] In Chinese Patent No. CN: 00112995.3, the method of producing anhydrous Glauber's salt by cooling, hot-melting method and its hot-melting tower is introduced. The removal of crystallization water in the crystal, although the technological process of this method is short, but the power consumption is large, the most important thing is to use a refrigerator to circulate and cool the nitric water. Since this method is an open technological process, at the same time, this method also It can only be produced in batches; if it is obtained like this, then it will eventually agglomerate

Method used

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  • Method for producing coarse-grain special mirabilite
  • Method for producing coarse-grain special mirabilite

Examples

Experimental program
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Effect test

Embodiment 1

[0028] Use a pump to pump hot water at 40-70°C to dissolve the Glauber's salt (sodium sulfate) in the ore to form a Glauber's salt (sodium sulfate) solution (abbreviation: salt water) containing various impurities and a sodium sulfate concentration of 28.4%. After refining to remove impurities, five-effect vacuum evaporation and concentration, crystallization, the nitric acid slurry is kept at 80°C for 0.5 hours in the thermal insulation crystallization tank, and after centrifugation, wet nitric acid with a water content of 3% is obtained, and the wet nitric acid is transported to the drying The device is dried, and the product is sent to the LLC-I special fluidized bed for treatment, to separate tiny particles of mirabilite, raw nitric water and various data of the purity of mirabilite obtained from production. figure 2 manifested in.

Embodiment 2

[0030] Use a pump to pump hot water at 40-70°C to dissolve sodium sulfate in the ore to form nitric water containing various impurities and a concentration of sodium sulfate of 28.1%. After refining to remove impurities, five-effect vacuum evaporation concentrates and crystallizes. Nitrate slurry is kept at 120°C for 0.5 hours in an insulated crystallization tank. After centrifugation, wet nitric acid with a water content of 6% is obtained. The wet nitric acid is transported to a drying device for drying, and the product is sent to LLC-I special fluidization Bed treatment, separation of tiny particles of thenardite, raw nitrate water and production of various data on the purity of thenardite figure 2 manifested in.

Embodiment 3

[0032] Use a pump to pump hot water at 40-70°C to dissolve sodium sulfate in the ore to form nitric water containing various impurities and a sodium sulfate concentration of 25.6%. After refining to remove impurities, five-effect vacuum evaporation concentrates and crystallizes. The nitric acid slurry is kept at 80°C for 3.0 hours in an insulated crystallization tank. After centrifugation, wet nitric acid with a water content of 6% is obtained. The wet nitric acid is transported to a drying device for drying, and the product is sent to LLC-I special fluidization Bed treatment, separation of tiny particles of thenardite, raw nitrate water and production of various data on the purity of thenardite figure 2 manifested in.

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Abstract

The invention discloses a method for preparing coarse granule special type saltcake, which includes the following technical steps: pumping hot water at 40-70 DEG C by a pump, and forming a saltcake solution containing a plurality of impurities; concentrating for crystallization by vacuum evaporation after refining impurities; obtaining a supersaturated solution containing saltcake crystals, keeping the temperature at 10-120 DEG C, and aging for 0.5-3.0 hours; drying after centrifugal separation, processing by a fluidized bed, separating fine granule saltcake and obtaining coarse granule special type saltcake. The anhydrous coarse granule special type saltcake product obtained by the process method of the invention has the advantages of good granule fluidness and low possibility of agglomeration. The product can be widely used for preparing sodium sulfide, sodium silicate and the like, and is also used in industries of paper making, glass, printing and dyeing, synthetic fiber, hide manufacture, food, medicine and the like.

Description

Technical field: [0001] The invention belongs to the field of fine processing of inorganic chemicals, or the field of fine chemicals. Background technique: [0002] Sodium sulfate decahydrate is Glauber's salt, Glauber's salt (Na 2 SO 4 10H 2 O), English name: Sodiumsulfate, Sodium sulfate, anhydrous Thenardite, containing 55.9% of crystal water and 44.1% of sodium sulfate. Pure mineral contains Na 2 O 19.3%, SO 3 24.8%. Monoclinic crystal system, usually in the form of granular and massive, and also in the form of shell or film. Colorless and transparent, impurities will dye it into gray, gray green, light yellow, milky white, black and so on. Vitreous luster. Streaks white. Hardness 1.5~2.0. The specific gravity is 1.48. It has a slightly bitter and salty taste. It loses water of crystallization at 100°C. It gradually loses water in dry air and turns into white powder anhydrous Glauber's salt. When burning, the flame is dark yellow. Soluble in water and glyc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01D5/00C01D5/16
Inventor 苟兴无刘泽民张大明刘文良余大海
Owner 四川省川眉芒硝有限责任公司
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