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A method for recovering and utilizing secondary steam from ammonia distillation

A technology for secondary steam and ammonia distillation, which is applied in the field of recovery and utilization of secondary steam from ammonia distillation, which can solve the problems of resource waste, environmental pollution, and large investment in equipment, and achieve the effects of saving production costs, simple operation, and reducing pollution

Active Publication Date: 2016-08-24
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

The acid addition method has the advantages of simple method, less investment in equipment, and low energy consumption, but it has disadvantages such as high cost, inaccurate addition, incomplete removal, affecting subsequent evaporation efficiency, increased energy consumption, and equipment corrosion.
Ammonia distillation is a method commonly used in the industry. It has the advantages of low cost and high removal rate. However, this method has the disadvantages of high energy consumption and large investment in equipment, and it has the disadvantages of secondary steam generated in the process of ammonia distillation. Contains a certain amount of ammonia and carbon dioxide, if the above-mentioned secondary steam is directly discharged, it will not only cause waste of resources but also pollute the environment
[0003] At present, the soda ash plant uses ammonia brine to absorb the secondary steam of ammonia distillation, but for factories producing baking soda by double decomposition method, because ammonia brine is not used in the production process and no ammonia brine is produced, if ammonia brine is specially purchased for treatment The cost of the above-mentioned secondary steam is too high, so the use of ammonia brine absorption method to process the secondary steam of ammonia is not suitable for factories producing baking soda by double decomposition

Method used

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  • A method for recovering and utilizing secondary steam from ammonia distillation
  • A method for recovering and utilizing secondary steam from ammonia distillation
  • A method for recovering and utilizing secondary steam from ammonia distillation

Examples

Experimental program
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Effect test

Embodiment 1

[0019] Such as figure 1 As shown, the mother liquor produced in the process of metathesis production of sodium bicarbonate enters the ammonia distillation tower for deammonization treatment. The secondary steam is sent to the condenser for condensation. During the condensation process, the condensation temperature is controlled in the range of 60 to 80 degrees Celsius. The condensate generated in the condenser flows back to the ammonia distillation tower through the return pipe at the bottom of the condenser for deamination again. Treatment, the noncondensable gas containing ammonia and carbon dioxide in the secondary steam of ammonia distillation is drawn out by a vacuum pump and sent to the absorption tower; then, water that can absorb ammonia and carbon dioxide in the noncondensable gas is sent into the absorption tower, and the Ammonia is dissolved in water to obtain ammonia water, which reacts with carbon dioxide to obtain ammonium bicarbonate, so far the absorption liqui...

Embodiment 2

[0023] Such as figure 2 As shown, the difference between this embodiment and Embodiment 1 mainly lies in that a circulation pool is provided, and the water that can absorb ammonia and carbon dioxide in the noncondensable gas is first injected into the circulation pool, and then sent to the absorption tower by the circulation pool, and the water in the absorption tower The discharged absorption liquid also flows into the circulation pool first, and then sent to metathesis production of baking soda by the circulation pool.

[0024] Other process steps of this embodiment are the same as those of Embodiment 1, and will not be repeated here.

Embodiment 3

[0026] Such as image 3 As shown, the difference between this embodiment and embodiment 2 mainly lies in: adding sodium chloride to the water before the water that can absorb ammonia and carbon dioxide in the non-condensable gas is injected into the circulating pool, and the specific way of adding sodium chloride is: set a Dissolving tank, and then put sodium chloride in the dissolving tank, then pour water that can absorb ammonia and carbon dioxide in the non-condensable gas into the dissolving tank and stir, after the sodium chloride in the dissolving tank is dissolved by water, add chlorine The sodium water is injected into the circulation pool, and then the water is sent to the absorption tower from the circulation pool.

[0027] It should be noted that in this embodiment, it is also possible to choose not to add sodium chloride before the water that can absorb ammonia and carbon dioxide in the non-condensable gas is injected into the circulation pool, but after the absorp...

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Abstract

The invention provides a recycling method for steamed ammonia secondary steam and relates to the technical field of industrial waste steam recycling. The method comprises the following steps of: 1) condensing steamed ammonia secondary steam containing ammonia and carbon dioxide in a condenser at a temperature of 60-80 DEG C, returning the condensate back to a ammonia still, and pumping out non-condensable gas containing ammonia and carbon dioxide by a vacuum pump and feeding into an adsorption tower; 2) feeding water which can absorb ammonia and carbon dioxide from the non-condensable gas into the adsorption tower, wherein absorption liquid containing ammonium bicarbonate is obtained after ammonia and carbon dioxide in the non-condensable gas are absorbed by water; and 3) producing baking soda by using the absorption liquid obtained in the step 2) in a double decomposition mode. The recycling method is easy to carry out without ammoniacal brine, and is suitable for workshops which produce baking soda in a double decomposition mode; by adopting the method, ammonia and carbon dioxide in the steamed ammonia secondary steam are recycled, so that environment pollution can be reduced and the production cost of enterprises is reduced.

Description

technical field [0001] The invention relates to the technical field of recovery and utilization of industrial waste steam, in particular to a method for recovery and utilization of secondary steam from ammonia distillation. Background technique [0002] Na + , NH 4 + , Cl - 、HCO 3 - and other ingredients. The recovery of ammonium chloride and sodium chloride by thermal method must first remove free ammonia and bicarbonate in the mother liquor. At present, there are two main methods for dealing with free ammonia and bicarbonate in China: one is to add hydrochloric acid, and the other is to distill ammonia. The acid addition method has the advantages of simple method, less investment in equipment, and low energy consumption, but it has disadvantages such as high cost, inaccurate addition, incomplete removal, affecting subsequent evaporation efficiency, increased energy consumption, and equipment corrosion. Ammonia distillation is a method commonly used in the industry....

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F1/04C01C1/26B01D5/00B01D53/78B01D53/62B01D53/58
CPCY02A50/20Y02P20/151Y02P70/10
Inventor 刘常松刘建军徐柏年腾隆晏清平
Owner 衡阳爱洁科技股份有限公司
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