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Technology for removing carbon dioxide in combined process for manufacturing soda ash and ammonium chloride

A technology of carbon dioxide and combined alkali production, which is applied in separation methods, chemical instruments and methods, and separation of dispersed particles, can solve problems such as deterioration of mother liquor conditions, reduced salt dissolution rate, and increased washing water equivalent, so as to ensure normal mother liquor conditions and salt Increased dissolution rate and reduced production cost

Active Publication Date: 2012-02-15
张志广 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the method of removing calcium and magnesium ion impurities in the clarification tank is used, but due to the high viscosity of the mother liquid and the high density of the mother liquid, the sedimentation velocity of the impurities in the clarification tank is inversely proportional to the viscosity of the mother liquid and proportional to the density difference between the impurities and the mother liquid. The settling speed is small, it is difficult to effectively remove the calcium and magnesium ion impurities in the mother liquor system, resulting in the accumulation of calcium and magnesium ion impurities in the mother liquor system, resulting in the deterioration of the mother liquor conditions, and bringing many adverse effects to the production of combined alkali, such as: the removal of carbon dioxide Low rate, low salt dissolution rate, small sodium bicarbonate crystals, high salt content in sodium bicarbonate entering the sodium carbonate production process, increased washing water equivalent, mother liquor expansion, etc.

Method used

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  • Technology for removing carbon dioxide in combined process for manufacturing soda ash and ammonium chloride
  • Technology for removing carbon dioxide in combined process for manufacturing soda ash and ammonium chloride
  • Technology for removing carbon dioxide in combined process for manufacturing soda ash and ammonium chloride

Examples

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Effect test

Embodiment 1

[0025] The carbon dioxide removal method in the combined soda production process, the process is as follows figure 1 As shown, the mother liquor B after ammonium chloride separation in the ammonium chloride production process is heated (temperature is 26-32°C) and enters ammonia absorber 1 to absorb ammonia, and the mother liquor after ammonia absorption (temperature is 36-54°C) enters clarification The barrel 2 separates the calcium and magnesium ion impurities carried in it, and after separating the impurities, it exchanges heat with the cooling device 3 and is cooled. The temperature after cooling is 26-36°C. After cooling, it enters the mixer 4; the alkali filter 5 separates the decarburization tower 8 out The mother liquor after the solid sodium bicarbonate in the tower liquid (temperature is 34-44°C) is divided into two parts, the first part mother liquor A1 is cooled by heat exchange with the cooling device 6, and the temperature after cooling is 26-42°C, after cooling, ...

Embodiment 2

[0031] The removal method of carbon dioxide in the combined soda production process, the process is as follows figure 2 As shown, the mother liquor B after ammonium chloride separation in the ammonium chloride production process is heated (temperature is 26-32°C) and enters ammonia absorber 1 to absorb ammonia, and the mother liquor after ammonia absorption (temperature is 36-54°C) enters clarification Barrel 2 separates the calcium and magnesium ion impurities carried in it, and enters the mixer 4 after separating the impurities; the mother liquor (temperature is 34-44°C) after separating the solid sodium bicarbonate in the tower liquid from the decarbonization tower 8 by the alkali filter 5 is divided into two Part, the first part of mother liquid A1 enters the mixer 4; A1 and B are mixed according to the volume ratio = 0.6 ~ 1.6:1, the temperature of the mixed liquid is 35 ~ 49 ° C, the temperature of the mixed liquid at 35 ~ 49 ° C is exchanged with the cooling device 10 ...

Embodiment 3

[0037] The removal method of carbon dioxide in the combined soda production process, the process is as follows image 3As shown, the mother liquor B after ammonium chloride separation in the ammonium chloride production process is heated (temperature is 26-32°C) and enters ammonia absorber 1 to absorb ammonia, and the mother liquor after ammonia absorption (temperature is 36-54°C) enters clarification Barrel 2 separates the calcium and magnesium ion impurities carried in it, and enters the mixer 4 after separating the impurities; the alkali filter 5 separates the mother liquor after the solid sodium bicarbonate in the decarburization tower 8 exits the tower liquid (temperature is 34 ~ 44 ℃) is divided into two Part, the first part of mother liquid A1 enters the mixer 4; A1 and B are mixed according to the volume ratio = 0.6 ~ 1.6: 1, the temperature of the mixed liquid is 35 ~ 49 ° C, the mixed liquid is cooled by heat exchange with the cooling device 7, and the temperature is ...

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Abstract

The invention belongs to the technical field of a combined process for manufacturing soda ash and ammonium chloride, and especially relates to a technology for removing carbon dioxide in the combined process for manufacturing soda ash and ammonium chloride. According to the invention, solid sodium bicarbonate is separated from a liquid discharged from a decarburization tower, such that a mother liquid is obtained; the mother liquid is divided into two parts which are A1 and A2; ammonium chloride is separated from a liquid discharged from an ammonium chloride producing process, such that a mother liquid B is obtained; the mother liquid B is processed through ammonia adsorption, and calcium and magnesium ionic impurities are removed from the mother liquid B; the mother liquid B is mixed with A1; the temperature of the mixed liquid is regulated to 18 to 24 DEG C, and carbon dioxide is removed from the mixed liquid in the decarburization tower. With the technology provided by the invention, a carbon dioxide removal reaction can be normally carried out with no internal or external cooling device arranged in the decarburization tower. That is to say, during the process since the decarburization solution is delivered into the decarburization tower to the decarburization solution is discharged from the tower, no heat exchanging by cooling is required. The decarburization tower can smoothly operate in a long period, wherein a task cycle is more than 60 days. With the technology, the carbon dioxide absorption effect is good, and a utilization rate is higher than 99.6%.

Description

technical field [0001] The invention belongs to the technical field of combined soda production, and in particular relates to a carbon dioxide removal process in the combined soda production. Background technique [0002] The conventional combined soda production method uses the mother liquor of separated ammonium chloride for the removal of carbon dioxide, and the ammonia mother liquor after absorbing ammonia is used as the decarburization liquid. The temperature of the decarburization liquid is 28-48°C. A cooler needs to be installed inside or outside the decarburization tower. The decarburization liquid in the decarburization tower is cooled by heat exchange with the cooler installed inside or outside. The reaction product sodium bicarbonate is easily affected by the large temperature difference during heat exchange. Accelerated precipitation and deposition on the surface of the decarburization tower and cooler, resulting in scarring and blockage of the decarbonization to...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/78B01D53/62
CPCY02A50/20Y02C20/40
Inventor 张志广丁丽芳
Owner 张志广
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