Process and device for recycling coked ammonium sulfate acid tar

A technology of acid tar and tar, which is applied in the recovery and treatment process of coking ammonium sulfuric acid tar and its device field, can solve the problems of sewage treatment system paralysis, failure to meet discharge standards, large-scale industrial clear water, etc., and solve the problem of difficult treatment of acid tar, Realize the effect of recycling and increasing tar production

Active Publication Date: 2013-08-28
NANJING IRON & STEEL CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
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Problems solved by technology

The sour tar treatment method described in this article uses steam for steam blowing, which requires a large amount of steam consumption. At the same time, the treated wastewater contains a large number of fine tar particles. Relying on the dilution treatment in the adjustment tank, it cannot meet the national discharge standards. Consuming a large amount of industrial clean water, entering the sewage system will even paralyze the sewage treatment system

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  • Process and device for recycling coked ammonium sulfate acid tar

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Embodiment 1

[0021] A kind of coking ammonium sulfate acid tar recycling process and its device provided by the present embodiment, the device is connected as figure 1 As shown, it includes ammonia water heat exchanger 4 for distilling ammonia, ammonium sulfate full flow tank 2 and acid tar neutralization tank 9, ammonium sulfate full flow tank 2 is connected with full flow pipe 1, and ammonium sulfate full flow tank 2 tar port passes through the pipeline 14 is connected with the acid tar neutralization tank 9, and the hot ammonia water pipeline of the ammonia water heat exchanger 4 leads a branch pipe 3 to the tar port of the ammonium sulfate full flow tank 2, and is close to the ammonium sulfate full flow tank 2 tar port on the branch pipe 3 A valve is installed to adjust the amount of hot ammonia water. When the tar in the full flow tank 2 is taken out, the hot ammonia water from the ammonia water heat exchanger 4 is opened in a small amount in time (the volume ratio of the amount of amm...

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Abstract

The invention belongs to the technical field of purification of coke-oven gas, in particular to a process and device for recycling coked ammonium sulfate acid tar. The process comprises the following steps of: spraying acid tar extracted from a full launder in an ammonium sulfate procedure with hot ammonia water which is subjected to heat exchange by using an ammonia steaming ammonia water heat exchanger at the temperature of 92-98 DEG C; mixing and introducing a mixture into an acid tar neutralizing tank; performing acid-alkali neutralization in the neutralizing tank; extracting mixed liquorof tar and ammonia water from the bottom of the front end of the neutralizing tank by taking a pump as power; introducing acid tar from the upper part of the back end of the tank into the neutralizing tank through the outlet of the pump to fully neutralize the acid tar; circulating for 30 minutes; pumping the mixed liquor into a coal gas sucking pipeline of a coke oven by using the pump; and introducing the mixed liquor into a mechanical ammonia water settling tank along with an ammonia water system to fulfill the aim of recycling the acid tar. The process and device are easy to operate and have low investment and running costs. By adopting the process and device, a heat source of ammonium steaming waste water is fully used for heating the acid tar, a large amount of steam is saved, and the acid tar can be directly taken as a product.

Description

technical field [0001] The invention belongs to the technical field of coke oven gas purification, in particular to a recovery and treatment process and device for coking ammonium sulfate tar. Background technique [0002] At present, in the gas purification process of the coking plant, sulfuric acid is used to absorb NH in the gas 3 , because the gas also contains a small amount of tar, when the sulfuric acid solution is used to reversely spray the gas in the saturator, the NH 3 At the same time, part of the tar in the gas will also be washed down. Due to the difference in specific gravity, the tar floats on the top of the ammonium sulfate solution, and flows through the full flow tank with the ammonium sulfate solution. Most of the acid tar that comes out is treated as waste or mixed in the tar residue, which is treated as solid waste at a low price. A small number of qualified coking plants (with tar slag into ball coal blending process) go to the coal yard together wit...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10C1/00
Inventor 李少源
Owner NANJING IRON & STEEL CO LTD
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