Pyrolysis device for processing desulfurization waste liquid in partial oxidation environment

A technology for desulfurizing waste liquid and oxidizing environment, which is applied in the fields of water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc. problems, to achieve the effect of realizing resource recycling, flexible operation, and reducing production costs

Inactive Publication Date: 2014-07-30
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in this method, the molten solid formed by the sodium-containing auxiliary salt in the desulfurization waste liquid is quenched at the same time as the incineration gas, and secondary reactions are likely to occur, resulting in the loss of sodium salt; in addition, due to the defects of the reaction furnace itself , the residence time of desulfurization waste liquid is short in the reaction process, the decomposition is not complete, and it is easy to block the pipeline
[0009] In the existing publicly reported literature, the treatment methods and equipment for desulfurization waste liquid are mainly to recover secondary salts. Generally, multi-effect evaporation crystallization equipment and a large number of steam heat sources can realize the step-by-step recovery of secondary salts, which increases the treatment cost; and the obtained secondary salts The quality and purity of salt are difficult to guarantee, and there is no price in the market, resulting in a backlog of products and increasing management costs
In addition, if the evaporated wastewater is not treated, its COD, nitrogen content, sulfide and other indicators still cannot meet the requirements of the water inlet of the coking biochemical treatment process, and further in-depth treatment is required, which will increase investment and operating costs, making it difficult to promote in a large area

Method used

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  • Pyrolysis device for processing desulfurization waste liquid in partial oxidation environment
  • Pyrolysis device for processing desulfurization waste liquid in partial oxidation environment
  • Pyrolysis device for processing desulfurization waste liquid in partial oxidation environment

Examples

Experimental program
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Effect test

Embodiment 1

[0087] Sodium-containing desulfurization waste liquid (hereinafter referred to as waste liquid, the same below), the original liquid and the pyrolysis gas from the pyrolysis gas outlet 1 are concentrated by 30%, and then atomized by atomizing nozzles 6a and 6b, and enters along the tangent line of the inner wall. In the atomization pyrolysis section II, at about 600°C, the waste liquid is further evaporated and concentrated, and the aromatic compounds and other non-salt organic compounds in the waste liquid are decomposed. The decomposed gas, water vapor and the pyrolysis gas from the lower stage pass upwards through the mist eliminator 5 into the gas separation section I, and are discharged after the temperature drops to about 350°C. The waste liquid flow rate is adjusted by detecting the temperature of the temperature detection hole 8a to ensure that the temperature of the atomization pyrolysis section II is stable at about 600°C.

[0088] The waste liquid is concentrated and d...

Embodiment 2

[0101] The device and operation mode are the same as in Example 1, except that the air coefficient is 0.6 and the concentration of waste liquid is 50%. At this time, the temperature of atomized pyrolysis section II is about 550℃, and the temperature of mixed flow pyrolysis section III is 850 At about ℃, the temperature of inactive salt pyrolysis section IV is about 1100℃. The condensate produced by the concentration of waste liquid and the condensate obtained from pyrolysis gas-liquid separation pass through the chiller 10 together, but not spray into the pyrolysis salt chill section. V. Cool the pyrolysis salt together with the cooling medium in the jacket 3 to form solid particles, which can be used as a solid alkali source for gas desulfurization after being discharged through the solid outlet.

[0102] The pyrolysis gas and pyrolysis salt produced by the above two embodiments have the same composition, and the pyrolysis gas is mainly H 2 S, N 2 , CO 2 And H 2 ; Pyrolysis salt...

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Abstract

The invention discloses a pyrolysis device for processing desulfurization waste liquid in a partial oxidation environment. The pyrolysis device comprises a pressure-bearing housing, a jacket, an insulating layer and a refractory brick which are arranged from outside to inside and connected together, and a gas separation section I, a spray pyrolysis section II, a mixed flow pyrolysis section III, an inactive salt pyrolysis section IV and a pyrolysis salt chilling section V are communicated from top to bottom to treat the desulfurization waste liquid in the partial oxidation environment. The device adopts a segmental treatment mode, so that decomposition of aromatic compounds and organic matters in the desulfurization waste liquid is ensured in the partial oxidation environment, COD and sulfides in the generated wastewater are reduced, meanwhile, pyrolysis of the inactive salt in the desulfurization waste liquid in the reducing atmosphere is ensured; therefore, the pollution problem of the desulfurization waste liquid is thoroughly solved and effective components in the desulfurization waste liquid can be recycled.

Description

Technical field [0001] The invention relates to a pyrolysis device for treating desulfurization waste liquid, in particular to a pyrolysis device for the harmless treatment of coking wet desulfurization waste liquid. It belongs to the technical field of chemical waste water recovery and treatment. Background technique [0002] With the rapid development of the coking industry, coke oven gas has become a large-tonnage energy and chemical resource. The raw coke oven gas contains harmful substances such as sulfide and cyanide, which can easily cause catalyst poisoning and equipment corrosion in the subsequent deep processing section. Therefore, the coke oven gas must be desulfurized and decyanated. [0003] Most of the existing domestic coking enterprises have adopted wet oxidation desulfurization equipment. For example, the alkaline desulfurization device uses soda ash as the alkali source, and the catalyst is regenerated by air oxidation, and the effect of desulfurization and decy...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/10
Inventor 张永发石玉良李国强陈卫青王亚珍
Owner TAIYUAN UNIV OF TECH
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