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A simultaneous flue gas desulfurization and denitrification process combined with chemical absorption and biotransformation and sulfur and nitrogen resources

A technology of desulfurization, denitrification, and biological transformation, which is applied in chemical instruments and methods, waste fuel, gas treatment, etc., can solve the problem of denitrification and desulfurization technology operating efficiency decline, difficulty in ensuring high load and high efficiency of denitrification and desulfurization process, water pollution, etc. problems, to achieve the effect of no secondary pollution, low investment and operating costs, and reasonable technology

Active Publication Date: 2022-04-08
ZHENGZHOU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, in an anaerobic environment, denitrifying bacteria and sulfate reducing bacteria compete for a common electron donor. At the same time, the hydrogen sulfide produced by Cui needs to be further absorbed and transformed, which leads to the decline of the overall operating efficiency of denitrification and desulfurization technology; High-load and high-efficiency operation of nitrification desulfurization process
[0006] In the process of oxidant wet flue gas denitrification, nitrogen oxides are absorbed by the absorption liquid containing oxidant and oxidized to nitrate, and the direct discharge of denitrification wastewater containing nitrate may cause water pollution.

Method used

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  • A simultaneous flue gas desulfurization and denitrification process combined with chemical absorption and biotransformation and sulfur and nitrogen resources

Examples

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Embodiment 1

[0029] An 80 t / h coal-fired thermoelectric boiler with a flue gas flow rate of 100,000 Nm 3 / h, SO 2 The content is 1000 mg / Nm 3 , NO content is 500 mg / Nm 3 , the flue gas temperature is 130 o C, according to technique of the present invention, when leaving absorption tower, SO 2 The content is 35 mg / Nm 3 , NO content is 50 mg / Nm 3 ; The desulfurization efficiency is above 95%, the denitrification efficiency is above 90%, the recovery of elemental sulfur is 1158 kg / d, and the recovery of ammonia is 505 kg / d.

[0030] SO 2 The absorption tower is a spray tower with a diameter of 3.5 m, a height of 22 m, and a liquid-gas ratio of 15 L / Nm 3 , the absorption process denitrification absorption liquid is NaOH, NaHCO 3 、Na 2 CO 3 One or more of the two and H 2 o 2 Or a combination of NaClO mixed composition.

[0031] The microaerobic bioreactor adopts the activated sludge method, the pH value is controlled at 7.5±0.2, and the temperature is controlled at 25-45 o C, the ...

Embodiment 2

[0035] A 200 t / h coal-fired thermoelectric boiler with a flue gas flow rate of 250,000 Nm 3 / h,SO 2 The content is 900 mg / Nm 3 , NO content is 400 mg / Nm 3 , the flue gas temperature is 150 o C, according to technique of the present invention, when leaving absorption tower, SO 2 The content is 35 mg / Nm 3 , NO content is 50 mg / Nm 3 ; The desulfurization efficiency is above 95%, the denitrification efficiency is above 85%, the recovery of elemental sulfur is 2595 kg / d, and the recovery of ammonia is 1190 kg / d.

[0036] SO 2 The absorption tower is a spray tower with a diameter of 6 m, a height of 25 m, and a liquid-gas ratio of 15 L / Nm 3 , the absorption process denitrification absorption liquid is NaOH, NaHCO 3 、Na 2 CO 3 One or more of the two and H 2 o 2 Or a combination of NaClO mixed composition.

[0037] The microaerobic bioreactor adopts the activated sludge method, the pH value is controlled at 7.5±0.2, and the temperature is controlled at 25-45 o C, the res...

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Abstract

The invention discloses a chemical absorption combined with biological conversion synchronous flue gas desulfurization and denitrification and sulfur and nitrogen co-resource process, which uses an alkaline absorption liquid containing an oxidant to absorb SO in the flue gas in a desulfurization and denitrification absorption tower 2 and NO x Converted to sulfates, sulfites, nitrates, nitrites. Then pump the absorption liquid into the microaerobic bioreactor, and use microorganisms (sulfate-reducing bacteria) to reduce sulfate and sulfite to sulfide (S 2‑ ), which is further converted into elemental sulfur, which will absorb NO x The solution producing nitrate and nitrite is converted to ammonia. The mixed solution containing elemental sulfur and ammonia produced by the microaerobic bioreactor is processed by the ammonia and sulfur recovery system to obtain sulfur and ammonia with high content for recycling, and the alkaline solution obtained by the ammonia and sulfur recovery system is returned to the desulfurization and denitrification absorption tower Recycling. The method has reasonable process, low energy consumption, less investment and operation costs, and less secondary pollution. It can achieve the purpose of simultaneous desulfurization and denitrification of flue gas and recovery of elemental sulfur and ammonia. Resource technology.

Description

technical field [0001] The invention belongs to the technical field of waste gas purification of environmental protection engineering, and relates to a process of synchronous flue gas desulfurization and denitrification combined with sulfur and nitrogen resource utilization combined with chemical absorption and biological conversion. Background technique [0002] Sulfur dioxide (SO 2 ) and nitrogen oxides (NO x ), mainly from natural sources such as volcanic eruptions, lightning, microbial activities, and man-made sources from man-made activities such as industry, transportation, agriculture, forestry, soil destruction, and fossil fuel combustion. x It can form photochemical smog with hydrocarbons, produce acid rain and acid fog, damage vegetation, endanger human health, and also destroy the ozone layer. At the same time, SO 2 It is also the main substance for the formation of acid rain. SO emissions from industrial sources 2 and nitrogen NO x Therefore, it is very impo...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/78B01D53/56B01D53/50B01D53/14C01B17/04C01C1/02
CPCB01D53/78B01D53/502B01D53/56B01D53/1481B01D53/1456C01B17/04C01C1/02B01D2251/106B01D2251/108B01D2252/10B01D2258/0283Y02E50/30
Inventor 王晓伟张婷婷
Owner ZHENGZHOU UNIV