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Method and device for preparing ammonia through active molecule oxidation flue gas double-circulation denitration

An active molecule and double-cycle technology, which is applied in separation methods, chemical instruments and methods, and dispersed particle separation, can solve the problems of low income, high denitrification operation cost, difficult treatment of active molecule oxidation and denitrification wastewater, and reduce wastewater discharge. Quantity, large environmental and economic benefits, and the effect of increasing alkalinity

Active Publication Date: 2022-08-02
浙江百能科技有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] In order to solve the problems of difficult treatment of active molecular oxidation and denitrification wastewater and high denitrification operation costs and low returns, the present invention provides a method and device for electrolytic ammonia production by active molecular oxidation of flue gas denitrification wastewater, which can convert nitrogen oxides in flue gas for high value NH 3 , while reducing waste water discharge, reducing absorbent and oxygen consumption, and reducing system energy consumption

Method used

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  • Method and device for preparing ammonia through active molecule oxidation flue gas double-circulation denitration
  • Method and device for preparing ammonia through active molecule oxidation flue gas double-circulation denitration
  • Method and device for preparing ammonia through active molecule oxidation flue gas double-circulation denitration

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Embodiment 1

[0057] like figure 1 and 2 As shown in the figure, the flue gas with a temperature of 60-160 °C after the previous treatment enters the flue reactor 1, and the active molecules O produced by the active molecule generator 2 3 Mixed to convert nitrogen oxides in flue gas into high-valence nitrogen oxides through oxidation reaction. After oxidation, the flue gas enters the wet scrubbing absorption tower 3, and the lye is sprayed uniformly through the top of the tower to absorb the high-valence nitrogen oxides in the flue gas into a nitrate-containing solution, and the flue gas enters the mist eliminator 9 after removing droplets. The rear flue gas treatment device. The absorbed nitrate-containing solution enters the ammonia-producing electrolytic cell 4, and is converted into ammonia molecules through catalytic electrolysis of nitrate ions, and the ammonia-containing solution enters the ammonia outlet tower 5, and the ammonia is evaporated under heating, and the water vapor is ...

Embodiment 2

[0060] like image 3 and 4As shown, the flue gas with a temperature of 60~160°C after the previous treatment (SOx vol% / NOx vol% in the flue gas is 2) enters the flue reactor 1, and the active molecule O produced by the active molecule generator 2 3 Mixed to convert nitrogen oxides in flue gas into high-valence nitrogen oxides through oxidation reaction. After oxidation, the flue gas enters the wet scrubbing absorption tower 3, and the slaked lime lye is evenly sprayed through the top of the tower to absorb the high-valent nitrogen oxides in the flue gas into a nitrate-containing solution, and the flue gas is removed by the mist eliminator 9. Enter the rear flue gas treatment device. The absorbed nitrate-containing solution enters the crystallization separation device 14 to separate the calcium sulfate crystals enriched in the solution, and generate gypsum products after subsequent treatment. The solution after desulfurization enters the ammonia production electrolytic cell...

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Abstract

The invention provides a method and device for preparing ammonia through active molecule oxidation flue gas double-circulation denitration, and relates to the field of flue gas treatment denitration wastewater treatment and flue gas denitration. The method comprises the following steps: flue gas containing nitrogen oxides sequentially enters a flue reactor and a wet washing absorption tower, O3 molecules from an active molecule generator oxidize the flue gas, and the nitrogen oxides are absorbed into a nitrate solution through wet alkali washing; the absorbed nitrate-containing alkali wash liquor generates ammonia through an ammonia production electrolytic bath, the ammonia is removed through an ammonia outlet tower, and the alkali liquor is regenerated after being diluted by make-up water and enters a wet washing absorption tower to be recycled. According to the invention, the emission of the active molecule oxidation flue gas denitration wastewater is reduced, the flue gas pollutant NOx is converted into NH3, the resource recycling of the pollutant is realized, the alkali liquor and oxygen in the system are recycled, the consumption of the alkali liquor and oxygen is reduced, and meanwhile, the energy consumption is reduced. The denitration efficiency is 95% or above, the NH3 conversion rate reaches 80% or above, and the method has great environmental and economic benefits.

Description

technical field [0001] The invention relates to the field of flue gas denitration wastewater treatment and flue gas denitration, in particular to a method and a device for producing ammonia by active molecular oxidation of flue gas double-cycle denitration. Background technique [0002] The combustion of solid waste, waste liquid, and exhaust gas in chemical production produces a large amount of air pollutants, including nitrogen oxides. [0003] At present, the main application technologies for flue gas denitrification are SNCR (selective non-catalytic reduction) and SCR (selective catalytic reduction) technologies. SNCR is suitable for the flue gas temperature of 850~1150 ℃. Directly inject reducing agent into the flue gas to reduce nitrogen oxides to N through thermochemical reaction. 2 It can be carried out without catalyst, and the investment and operation costs are low, but the denitration efficiency is low. With the increasingly strict emission standards, SNCR alone ...

Claims

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Application Information

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IPC IPC(8): B01D53/75B01D53/76B01D53/78B01D53/50B01D53/56C25B1/27C04B11/26
CPCB01D53/75B01D53/76B01D53/56B01D53/78B01D53/502C25B1/27C04B11/264B01D2258/0283B01D2251/104B01D2251/404B01D2251/604Y02A50/20
Inventor 张相戴聪润何春晓凌有基赵琛杰
Owner 浙江百能科技有限公司
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