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Catalytic wet oxidation method of flue gas desulfurization waste liquor

A technology for catalyzing wet oxidation and desulfurization waste liquid, which is applied in the direction of oxidized water/sewage treatment, gaseous effluent wastewater treatment, etc. It can solve the problems of inability to overcome catalyst loss, inability to solve Cu loss, and failure to solve it well, so as to speed up Oxidation reaction speed, high oxidation treatment performance, effect of equipment scale reduction

Active Publication Date: 2013-04-17
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

CN101185887 provides a catalyst for wet oxidation process, with γ-Al 2 o 3 As the carrier, transition metal Mn, rare earth oxide CeO 2 and La 2 o 3 As an active component, the catalyst can reduce the amount of expensive noble metal materials, and to a certain extent reduce the loss of transition metal elements such as copper and iron, but the carrier is prone to crystal transformation during the reaction, resulting in catalyst deactivation
U.S. Patent US5360552 adopts CuO / Al 2 o 3 , CuS / activated carbon, Cu / X molecular sieve as wet oxidation catalyst, COD removal rate is high, but still can not solve the problem of Cu loss
[0005] The above studies mainly focus on Cu 2+ , Fe 2+ , Mn 2+ Such metal ions are used as homogeneous catalysts to increase the oxidation rate of sulfite, and the catalytic activity is high, but it cannot overcome the problem of catalyst loss with wastewater discharge, resulting in secondary pollution, and the wastewater needs to be further treated before it can be discharged
For heterogeneous catalysts, the problem of loss of active components is not well resolved, so it will cause problems such as reduced catalyst activity and secondary pollution.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] Embodiment 1 (preparation of catalyst carrier)

[0024] Preparation of catalyst carrier TOS-1: knead 40g of nano-titanium dioxide (average particle size 30nm) and 15g of pseudoboehmite, 2g of 65% nitric acid, 25g of distilled water, 3g of scallop powder, and extrude on a twin-screw extruder Molding treatment, drying the shaped carrier in the air for 24 hours, drying at 120°C for 12 hours, and then roasting at 500°C for 12 hours to obtain cylindrical TiO 2 Vector TOS-1.

[0025] Preparation of catalyst carrier TOS-2: Knead 40g of non-nanometer titanium dioxide (conventional titanium dioxide material, average particle size of about 450nm) and pseudo-boehmite, 2g of 65% nitric acid, 25g of distilled water, and 3g of scallop powder in a double Carry out extrusion molding on the screw extruder, dry the molding carrier in the air for 24 hours, dry at 120°C for 12 hours, and then bake at 500°C for 12 hours to obtain cylindrical TiO 2 Vector TOS-2.

Embodiment 2

[0026] Embodiment 2 (the inventive method uses the preparation of catalyst)

[0027] The TOS-1 carrier was impregnated in the mixed aqueous solution of cerium nitrate and chloroplatinic acid by the impregnation method, the loading amount was 4% Ce, 0.2% Pt, the impregnation time was 0.1h, and then dried in the shade for 20 hours, and then in the air atmosphere Dry it in an oven at 120°C for 12 hours, and finally place it in a muffle furnace and bake it at 550°C for 5 hours in an air atmosphere to obtain catalytic wet oxidation catalyst A.

Embodiment 3

[0028] Embodiment 3 (the inventive method uses the preparation of catalyst)

[0029] The TOS-1 carrier was impregnated in the mixed aqueous solution of lanthanum nitrate and ruthenium chloride by impregnation method, the loading amount was 5% La, 0.2% Ru, the immersion time was 0.2h, and then dried in the air at a certain humidity for 20 hours, then dried in an air oven at 80°C for 12 hours, and finally placed in a muffle furnace and baked at 600°C for 3 hours in an air atmosphere to obtain Catalytic Wet Oxidation Catalyst B.

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PUM

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Abstract

The invention relates to a catalytic wet oxidation method of flue gas desulfurization waste liquor. In the presence of a catalyst, flue gas desulfurization waste liquor contacts air to oxidate sulfite into sulfate, wherein the catalyst uses nano TiO2 as a supporter, the active component of the catalyst is one or more of noble metal elements Pt, Pd, Ru and Rh, and the assistant is one or more of rare earth metal elements La, Ce, Pr and Nd. The catalyst comprises the following components in percentage by weight: 0.05-0.5% of noble metal element and 1-10% of rare earth metal element. The mass ratio of the rare earth metal element to the noble metal element is 10-200. By adopting the proper catalyst, the method provided by the invention lowers the cost of the catalyst on the premise of enhancing the reactivity; and the catalyst has the advantages of high stability and no secondary pollution.

Description

technical field [0001] The invention relates to a treatment method for flue gas desulfurization waste liquid, in particular to a method for treating flue gas desulfurization waste liquid by using a catalytic wet oxidation method. Background technique [0002] In the treatment process of flue gas desulfurization, wet flue gas desulfurization technology is mostly used at home and abroad. The principle is to use alkaline materials as absorbents to absorb SO in the absorption tower. 2 The flue gas is spray scrubbed to make SO 2 React with absorbent to generate sulfite and sulfate. In this process, the oxidation of sulfite is an important process in the treatment of desulfurization waste liquid. Due to the slow process of sulfite oxidation, after the waste liquid is directly oxidized by air Still containing too much sulfite ion makes it difficult for wastewater COD to meet the discharge standard. Improving the oxidation efficiency of sulfite through appropriate methods is of gr...

Claims

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Application Information

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IPC IPC(8): C02F1/74C02F103/18
Inventor 程明珠王学海刘忠生杨英
Owner CHINA PETROLEUM & CHEM CORP
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