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Normal-temperature flue gas denitration method

A flue gas and denitrification technology, applied in the field of normal temperature flue gas denitrification process, can solve the problems of low ammonia removal nitrogen oxide treatment efficiency, high operating cost and high investment, and achieves the elimination of hidden dangers of explosion, low operating cost and high denitration efficiency. Effect

Active Publication Date: 2014-04-23
水木清研生态环保(山东)有限公司
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Problems solved by technology

[0003] The shortcomings of the above-mentioned denitrification process are: selective non-catalytic reduction method: the efficiency of nitrogen oxide removal by spraying ammonia in the furnace is low (30%-50%), ammonia escape is serious, and it is difficult to standardize emissions; selective catalytic reduction method uses Catalyst, the efficiency is relatively high and can reach 80% efficiency, but the investment is high, the catalyst layer needs to be replaced every 2-3 years, and the operating cost is high
In the prior art, as far as the applicant knows, there is no process and device that can be practically applied in industry

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Embodiment Construction

[0028] A normal temperature flue gas denitrification process is characterized in that it comprises the following steps:

[0029] 1) Dust removal;

[0030] 2) Desulfurization;

[0031] 3) Plasma oxidation;

[0032] 4) Spray the oxidized flue gas with alkaline aqueous solution to capture the oxidized substances in the flue gas.

[0033] Among them, the dust removal process adopts bag type dust removal, and the desulfurization process adopts desulfurization tower.

[0034] The row-type double dielectric barrier discharge plasma oxidizer includes a casing 9, a frame 2 is arranged in the casing 9, a single air duct 8 is arranged on the frame 2, and the single air duct 8 is arranged sequentially from top to bottom. Tuyere 1, spray device 3, plasma disk 4, single fuel tank 5 and disk gland device 6, the lower end of single air cylinder 8 is connected to air outlet 7. A heat sink 10 and a power supply 11 are also provided in the casing 9 .

[0035] Wherein, the frame 2 is to supp...

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Abstract

The invention relates to a method used for processing nitrogen oxide in boiler flue gas, and specifically relates to a normal-temperature flue gas denitration method. The normal-temperature flue gas denitration method comprises following steps: 1) dedusting; 2) desulphurization; 3) plasma oxidation, wherein processed flue gas is delivered into a row electrode type double-dielectric barrier discharge plasma oxidation device for oxidation treatment; and 4) collection of oxidized substances in the flue gas via spraying the oxidized flue gas with an alkaline aqueous solution. Compared with traditional technology, the normal-temperature flue gas denitration method is capable of realizing large wind amount treatment, is high in denitration efficiency, and can be widely used for boilers of different types; and denitration efficiency can be more than 90% via controlling plasma row electrode control.

Description

technical field [0001] The invention relates to a method for treating nitrogen oxides in boiler flue gas, in particular to a normal temperature flue gas denitrification process. Background technique [0002] At present, the main denitrification processes are SNCR (selective non-catalytic reduction) and SCR (selective catalytic reduction) technologies. By adding ammonia or ammonia water to the flue gas and controlling the reaction conditions, the nitrogen oxides and ammonia undergo a redox reaction to generate nitrogen to achieve the purpose of denitrification. [0003] The shortcomings of the above-mentioned denitrification process are: selective non-catalytic reduction method: the efficiency of nitrogen oxide removal by spraying ammonia in the furnace is low (30%-50%), ammonia escape is serious, and it is difficult to standardize emissions; selective catalytic reduction method uses Catalyst, the efficiency is relatively high and can reach 80% efficiency, but the investment...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/75B01D53/56
Inventor 李瑞莲张建平
Owner 水木清研生态环保(山东)有限公司
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