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Method for efficient catalytic reduction regeneration of denitration complexing liquid

A denitrification and complexation technology, applied in the field of environmental pollution control, can solve the problems of high operating cost, influence on industrial promotion, and limit industrial application, etc., and achieve the effect of obvious regeneration effect, low process cost and fast reaction rate

Active Publication Date: 2019-08-30
WUHAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The Fe(II)EDTA complexation absorption method has the advantages of fast absorption rate, large complexation capacity, and low temperature requirements, and has attracted widespread attention. Fe(II)EDTA is easily absorbed by O in flue gas 2 Oxidation to Fe(III)EDTA, resulting in the gradual reduction of the ability of the complexing liquid to absorb NO, which limits its industrial application
Therefore, simply using Fe(II) EDTA complex solution to absorb NO is difficult to maintain a high removal rate of NO for a long time. In order to maintain a higher and longer NO removal rate and process continuity, it is oxidized to become Fe(III)EDTA and Fe(II)EDTA-NO should be reduced in time, and the regeneration of Fe(II)EDTA has become a hot research topic at home an

Method used

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  • Method for efficient catalytic reduction regeneration of denitration complexing liquid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038] The Pd-Cu / C catalyst in Example 1 uses activated carbon as a carrier, the mass fraction of palladium is 5%, and the mass fraction of copper is 0%.

[0039] (1) Preparation of Pd-Cu / C catalyst:

[0040] 0.8339g of PdCl 2 Add it to 100ml of dilute hydrochloric acid solution with a concentration of 0.01mol / L, heat to dissolve, and make the volume of the solution slightly larger than the volume of the activated carbon carrier. 10g of activated carbon support impregnated in the precursor PdCl2 In the solution, after stirring and dehydrating, dry in a vacuum drying oven at 100°C for 12h, place in a vacuum tube muffle furnace, burn at 400°C for 2h, add excess hydrazine hydrate after natural cooling, stir fully, and the stirring time is 12h , dehydrated and dried with a rotary evaporator, and dried in a vacuum oven at 80°C for 12 hours before use.

[0041] (2) Regeneration of invalid denitrification complex solution:

[0042] Take 500ml of expired denitrification complex sol...

Embodiment 2

[0046] Pd-Cu / Al in this embodiment 2 2 o 3 The catalyst is based on γ-Al 2 o 3 As the carrier of the catalyst, the mass fraction of palladium is 5%, and the mass fraction of copper is 0%.

[0047] (1) Pd-Cu / Al 2 o 3 Catalyst preparation:

[0048] 0.8339g of PdCl 2 Add it to 100ml of dilute hydrochloric acid solution with a concentration of 0.01mol / L, heat to dissolve, and make the volume of the solution slightly larger than γ-Al 2 o 3 The volume of the carrier. 10g of γ-Al calcined at 500°C for 4h 2 o 3 The support is impregnated with the precursor PdCl 2 In the solution, after stirring and dehydrating, dry in a vacuum drying oven at 100°C for 12h, place in a vacuum tube muffle furnace, burn at 400°C for 2h, add excess hydrazine hydrate after natural cooling, stir fully, and the stirring time is 12h , dehydrated and dried with a rotary evaporator, and dried in a vacuum oven at 80°C for 12 hours before use.

[0049] (2) Regeneration of invalid denitrification compl...

Embodiment 3

[0054] The Pd-Cu / C catalyst in Example 3 uses activated carbon as a carrier, the mass fraction of palladium is 5%, and the mass fraction of copper is 1.5%.

[0055] (1) Preparation of Pd-Cu / C catalyst:

[0056] 0.8339g of PdCl2 was added to 100ml of dilute hydrochloric acid solution with a concentration of 0.01mol / L, heated to dissolve, and 0.5663g of Cu(NO 3 ) 2 ·3H 2 O is dissolved in the above solution, so that the volume of the solution is slightly larger than the volume of the activated carbon carrier. Immerse 10g of activated carbon carrier in the above solution, stir and dehydrate and dry, then dry in a vacuum oven at 100°C for 12h, place in a vacuum tube muffle furnace, burn at 400°C for 2h, add excess hydrazine hydrate after natural cooling, Fully stir, stir for 12 hours, dehydrate and dry with a rotary evaporator, and dry in a vacuum oven at 80°C for 12 hours before use.

[0057] (2) Regeneration of invalid denitrification complex solution

[0058] Take 500ml of...

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Abstract

The invention discloses a method for efficient catalytic reduction regeneration of a denitration complexing liquid, wherein the method comprises: preparation of Pd-Cu/C and Pd-Cu/Al2O3 catalyst and catalytic reduction regeneration of denitration complexing liquid. According to the method, formic acid and sodium formate are added to a spent denitration complexing liquid, and under the action of magnetic stirring, through Pd-Cu/C or a Pd-Cu/Al2O3 catalyst, Fe(III) EDTA is reduced into Fe(II)EDTA and Fe(II)EDTA-NO is reduced into Fe(II)EDTA, and N2. According to the present invention, with the method, the complexing liquid can be rapidly and efficiently regenerated so as to improve the denitration performance of the Fe(II)EDTA complexing liquid, reduce the application cost of the process andachieve good application prospect.

Description

technical field [0001] The invention relates to the field of environmental pollution control, in particular to an efficient method for catalytic reduction and regeneration of denitrification complex liquid. Background technique [0002] Nitrogen oxide is a major pollutant that causes air pollution. It can form photochemical smog, destroy the ozone layer, cause acid rain and cause the greenhouse effect, causing great harm to human health and the natural environment. At present, the technologies for controlling NOx emissions are mainly divided into two categories: low NOx combustion technology and post-combustion NOx control technology. The Fe(II)EDTA complexation absorption method has the advantages of fast absorption rate, large complexation capacity, and low temperature requirements, and has attracted widespread attention. Fe(II)EDTA is easily absorbed by O in flue gas 2 Oxidation to Fe(III)EDTA causes the ability of the complexing liquid to complex and absorb NO to gradu...

Claims

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Application Information

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IPC IPC(8): B01D53/96B01D53/56
CPCB01D53/56B01D53/96B01D2251/902
Inventor 张光旭许超许文晋刘会轩
Owner WUHAN UNIV OF TECH