Process for producing nickel-cobalt salt and ammonium salt through continuous crystallization

A technology of crystallization and nickel-cobalt, which is applied in the field of continuous crystallization production process of salt, can solve the problems of intermittent operation of the system, low degree of automation, and large footprint, and achieve continuous and stable operation, high degree of automation, and small footprint Effect

Inactive Publication Date: 2020-11-10
CHINA CEC ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The existing technical process has the disadvantages of large volume and quantity of crystallizers, large investment in equipment, large floor space, intermittent operation of the system, and low degree of automation.
In addition, there are also nickel sulfate and cobalt sulfate that adopt continuous crystallization process, adopt cooling type internal circulation continuous crystallizer, and obtain magma after heat exchange and cooling with the external cooler of the crystallizer and circulating cooling water. This production method also has a crystallizer structure Complex, external cooler and crystallizer are prone to material blockage, difficult operation and maintenance, etc.

Method used

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  • Process for producing nickel-cobalt salt and ammonium salt through continuous crystallization

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] Continuous crystallization process for the production of cobalt sulfate. The cobalt sulfate saline solution is 25°C, and the saline solution with a cobalt sulfate concentration of 23% is concentrated through a multi-effect evaporator or MVR evaporation device. The concentrated cobalt sulfate concentration is 41%, and the temperature is 72°C; the concentrated solution enters the vacuum crystallization Flash cooling after the tank, control the temperature of the solution in the vacuum crystallization tank to 48°C, the temperature of the secondary steam generated by the flash is 42°C, and the concentration of cobalt sulfate is 33%. The feed liquid precipitates salt crystals in the vacuum crystallization tank to obtain a slurry. The secondary steam generated by the vacuum crystallization tank is cooled by exchanging heat with the circulating cooling water through the surface cooler to obtain condensed water and a small amount of non-condensable steam. The non-condensable ste...

Embodiment 2

[0019] A continuous crystallization process for the production of nickel sulfate. Nickel sulfate salt-containing solution at 40°C, the salt-containing solution with a nickel sulfate concentration of 21% is concentrated through a multi-effect evaporator or MVR evaporation device, the concentrated nickel sulfate concentration is 41%, and the temperature is 95°C; the concentrated solution enters the vacuum crystallization Flash cooling after the tank, control the temperature of the solution in the vacuum crystallization tank to 45°C, the temperature of the secondary steam generated by the flash is 40°C, and the concentration of nickel sulfate is 33%. The feed liquid precipitates salt crystals in the vacuum crystallization tank to obtain a slurry. The secondary steam generated by the vacuum crystallization tank is cooled by exchanging heat with the circulating cooling water through the surface cooler to obtain condensed water and a small amount of non-condensable steam. The non-con...

Embodiment 3

[0021] Continuous crystallization process for the production of ammonium chloride. A saline solution with an ammonium chloride concentration of 5.9% at a temperature of 30°C is concentrated through a multi-effect evaporator or MVR evaporator. The concentrated ammonium chloride concentration is 40% and the temperature is 75°C; the concentrated solution enters a vacuum crystallization tank After flashing, the temperature of the solution in the vacuum crystallization tank is controlled to be 54°C, the temperature of the secondary steam generated by the flashing is 42°C, and the concentration of ammonium chloride is 34%. The feed liquid precipitates salt crystals in the vacuum crystallization tank to obtain a slurry. The secondary steam generated by the vacuum crystallization tank is cooled by exchanging heat with the circulating cooling water through the surface cooler to obtain condensed water and a small amount of non-condensable steam. The non-condensable steam is pumped out by...

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Abstract

A process for producing nickel-cobalt salt and ammonium salt through continuous crystallization comprises the following steps: a salt-containing solution is concentrated to be close to a saturated state through a multi-effect evaporation device or an MVR evaporation device, the concentrated salt-containing solution enters a vacuum crystallization tank and then is subjected to flash evaporation cooling, salt crystals are separated out while feed liquid circulates in the vacuum crystallization tank, and slurry is obtained; then the secondary steam generated by the vacuum crystallizing tank exchanges heat with circulating cooling water or chilled water through a surface air cooler to be cooled to obtain condensate water and a small amount of non-condensable steam, and the non-condensable steam is pumped out through a vacuum pump or a steam jet pump; finally, the slurry obtained by the vacuum crystallization tank is pumped to the crystallization buffer tank and then sent to the centrifugalmachine by the crystallization buffer tank, and crystals obtained by centrifugal dehydration are dried by the drying bed to obtain crystal products with uniform granularity.

Description

technical field [0001] The invention belongs to the technical field of inorganic salt crystal production, in particular to a continuous crystallization production process for nickel sulfate, cobalt sulfate, cobalt chloride, ammonium chloride and other salts. Background technique [0002] In industrial production, it is often necessary to obtain crystal products of various inorganic salts, such as nickel sulfate hexahydrate, cobalt sulfate heptahydrate, cobalt chloride hexahydrate, ammonium chloride, etc. For example, the high-purity cobalt sulfate solution extracted by the metallurgical industry needs to go through the crystallization process to obtain the cobalt sulfate heptahydrate crystal product. In the existing production, the batch method is mainly used to obtain cobalt sulfate heptahydrate crystals. The method is mainly that the solution is intermittently cooled and crystallized in a jacketed kettle crystallizer, and then the slurry is intermittently discharged to the...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D9/00B01D1/22B01D1/26B01D1/30C01G51/10C01G53/10C01C1/16C01G51/08
CPCB01D9/0018B01D9/0059B01D1/26B01D1/22B01D1/30C01G51/10C01G53/10C01C1/164C01G51/085B01D2009/0086
Inventor 彭征宇万华朱利民黄小红李冰
Owner CHINA CEC ENG
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