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Process for recycling products from mother liquid containing ammonium chloride, sodium chloride, ammonium hydrogen carbonate and sodium hydrogen carbonate through thermal method

A technology of ammonium bicarbonate and sodium bicarbonate, applied in the direction of ammonium carbonate/acid carbonate, products, ammonium halide, etc., can solve the problems of increasing mother liquor blockage, large equivalent, low ammonia concentration, etc., and achieve heating Effects of temperature optimization, reduction of equipment corrosion, and reduction of power consumption

Active Publication Date: 2019-06-14
衡阳爱洁科技股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are many disadvantages in this patent: 1. The ammonia water obtained by condensing the tail gas after deamination has low concentration and large equivalent, and the ammonia water contains a large amount of carbon dioxide, which has little practical value; 3. After the high-temperature mother liquor enters the final effect, the temperature drops rapidly, and the secondary steam generated cannot be reused, and the heat utilization rate is not high; 4. Multi-stage pre-heating is adopted in the process. The heat exchange of the heat exchanger, especially the condensate water preheater, has a limited effect, but it will increase the frequency of mother liquor clogging, which is not feasible in the actual industrial production process

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Original mother liquor: the mother liquor after the double decomposition reaction produces baking soda, wherein, Cl - The content is 167.5g / L, NH 4 + The content is 62.96 g / L, HCO 3 - The content is 35.86 g / L, and the original mother liquor volume is 119000kg / h.

[0033] The technology of thermal recovery product from above-mentioned sodium bicarbonate production mother liquor, comprises the following steps:

[0034] Pump the mother liquor into the first-stage condensate heat exchanger of the original mother liquor, heat the mother liquor to 38°C by evaporating condensate water in the V-effect, and then enter the second-stage condensate heat exchanger of the original mother liquor, and evaporate the condensate water with the I-effect Heat the mother liquor to 58°C, and then enter the third-stage heat exchanger of the original mother liquor. After the mother liquor is heated to 66°C, it enters the ammonia distillation tower. The temperature of the lower part of the a...

Embodiment 2

[0045] Original mother liquor: soda ash production mother liquor, wherein, Cl - The content is 161.5g / L, NH 4 + The content is 63.7g / L, HCO 3 - with CO 3 2- The content is 67.5 g / L, and the original mother liquor volume is 119000kg / h.

[0046] Compared with Example 1, the difference is that first: the types of the original mother liquor used are different. The original mother liquor in Example 1 is the mother liquor after the bicarbonate production by the metathesis reaction (ie, the mother liquor for baking soda production), while the original mother liquor in this example It is the heavy alkali filtered mother liquor obtained in the production process of soda ash (that is, the mother liquor of soda ash production). Although the two also contain ammonium chloride, sodium chloride, ammonium bicarbonate, and sodium bicarbonate, there are certain differences in their content; second, this In the embodiment, the tail gas that comes out from the ammonia distillation tower is...

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PUM

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Abstract

The invention provides a process for recycling products from mother liquid containing ammonium chloride, sodium chloride, ammonium hydrogen carbonate and sodium hydrogen carbonate through a thermal method. The process comprises a method for recycling gas generated after deaminizing the mother liquid. The method for recycling the gas generated after deaminizing the mother liquid comnprises the following steps: preheating the mother liquid, then feeding the mother liquid into an ammonia still for deaminizing, feeding carbon dioxide and ammonia gas generated after deaminizing into an ammonia absorption tower for generating carbon-containing ammonia water, adding carbon dioxide into the carbon-containing ammonia water, enabling carbon dioxide in the carbon-containing ammonia water to be excessive and generate ammonium hydrogen carbonate. The process also comprises a method for recycling the deaminized mother liquid and obtaining ammonium chloride and sodium chloride. The method for recycling the deaminized mother liquid and obtaining ammonium chloride and sodium chloride comprises the following steps: carrying out five-effect cross-flow evaporation to obtain sodium chloride, carrying out four-effect flash evaporation and crystallization to obtain ammonium chloride, feeding salt thickener overflowing liquid and salt centrifugal machine post-throwing liquid into a V-effect evaporation tank and enabling the salt thickener overflowing liquid and the salt centrifugal machine post-throwing liquid to participate in circulation again; feeding ammonium thickener overflowing liquid and ammonium centrifugal machine post-throwing liquid into an IV-effect flash evaporation and crystallization tank by using a pump, and enabling the ammonium thickener overflowing liquid and the ammonium centrifugal machine post-throwing liquid to participate in production circulation again. The process is capable of simultaneously recycling to obtain ammonium chloride and sodium chloride; meanwhile, the recycling rate is extremely high; the process is also capable of effectively increasing the heat utilization rate.

Description

technical field [0001] The invention relates to the technical field of recovery of mixed mother liquor, in particular to a process for thermally recovering products from mother liquor containing ammonium chloride, sodium chloride, ammonium bicarbonate and sodium bicarbonate. Background technique [0002] Using brine and ammonium bicarbonate as raw materials to produce baking soda by metathesis reaction, in the production process, a large amount of mother liquor containing ammonium chloride, sodium chloride, ammonium bicarbonate, and sodium bicarbonate will be produced. In addition, the soda ash production process is obtained Heavy alkali filtration mother liquor (usually called soda ash production mother liquor) also contains the above four components, and its component content is slightly different from the mother liquor obtained after the above-mentioned metathesis production of baking soda (usually called baking soda production mother liquor) . [0003] At present, the a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01C1/16C01C1/26C01D3/14C01D7/22
CPCY02P20/141
Inventor 李月明徐柏年郜长水滕隆
Owner 衡阳爱洁科技股份有限公司
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