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A pre-sco enhanced flue gas denitrification and mercury removal system for coal-fired power plants

A coal-fired power plant, flue gas technology, applied in the direction of gas treatment, chemical instruments and methods, separation methods, etc., can solve the problems of uneconomical, unsatisfactory Hg0 oxidation efficiency, reduced oxidation efficiency, etc., to reduce the amount of use, The technical process is easy to implement and improves the effect of oxygen storage performance

Active Publication Date: 2018-07-27
WUHAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, various types of SCR catalysts are sensitive to Hg 0 Oxidation efficiency is not satisfactory in pilot test conditions and field experiments
There are two essential factors that limit its mercury removal efficiency: first, NH 3 to Hg 0 There is a competitive relationship, and a large amount of NH in the SCR process 3 Injection of Hg will be severely suppressed 0 Reacts with the solid-gas interface of the SCR catalyst, resulting in a reduction in oxidation efficiency; 0 The oxidation efficiency of mercury depends heavily on the HCl in the flue gas. However, the Cl content of coal-fired coal in my country is much lower than that of other countries. It is obviously uneconomical to artificially add HCl to the SCR process to improve the mercury oxidation efficiency.
[0004] On the other hand, the denitrification efficiency of the SCR process has no upper limit in theory, but the main consideration in the actual application process is the cost issue

Method used

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  • A pre-sco enhanced flue gas denitrification and mercury removal system for coal-fired power plants
  • A pre-sco enhanced flue gas denitrification and mercury removal system for coal-fired power plants
  • A pre-sco enhanced flue gas denitrification and mercury removal system for coal-fired power plants

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] A pre-SCO enhanced denitrification and mercury removal technology test experiment was carried out in a coal-fired power plant with a pulverized coal furnace. The SCR unit is a commercial V-W-Ti catalyst, and the original denitrification efficiency is 85%. The measured mercury concentration at the inlet of the SCO unit is 25.6ug / m 3 , NO content is 0.1%, C (NO) / C (NOX) =0.95, the oxygen content was 4.6%. The SCO catalyst used is 5% by mass of cobalt oxide, 3% by mass of tungsten oxide and 10% by mass of cerium oxide as the catalyst carrier, and the arrangement temperature is 300°C. The pre-installation test was carried out, the SCO catalyst was arranged in double layers, and the actual space velocity was 3500h -1 , the flue gas direct passage rate δ is 0%, and the Hg of the SCO unit is measured by the test 0 The oxidation rate is 96%, and the NO oxidation rate is 47%, meeting the established requirements. After the SCR unit and dust removal unit, the Hg removal eff...

Embodiment 2

[0039] A pre-SCO enhanced denitrification and mercury removal technology test experiment was carried out in a coal-fired power plant with a pulverized coal furnace. The SCR unit is a commercial V-W-Ti catalyst, and the original denitrification efficiency is 83%. The measured mercury concentration at the inlet of the SCO unit is 19.6ug / m 3 , NO content is 0.15%, C (NO) / C (NOX) =0.98, the oxygen content is 5%. The SCO catalyst used is 5% by mass of manganese oxide, 5% by mass of tungsten oxide and 20% by mass of cerium oxide as the catalyst carrier, and the arrangement temperature is 350°C. The pre-installation test is carried out, the SCO catalyst adopts a double-layer arrangement, the direct flue gas passing rate δ is 0%, and the actual space velocity is 3900h -1 , measured in SCO unit Hg 0 The oxidation rate was 97%, and the NO oxidation rate was 36%. Change the SCO catalyst unit to a three-layer arrangement, the SCO unit Hg 0 The oxidation rate is 98%, and the NO oxid...

Embodiment 3

[0041] A pre-SCO enhanced denitrification and mercury removal technology test experiment was carried out in a coal-fired power plant with a pulverized coal furnace. The SCR unit is a commercial V-W-Ti catalyst, and the original denitrification efficiency is 87%. The measured mercury concentration at the inlet of the SCO unit is 22.6ug / m 3 , NO content is 0.15%, C (NO) / C (NOX) =0.92, the oxygen content is 5.5%. The SCO catalyst used is that manganese oxide accounts for 2.5% by mass of the catalyst, cobalt oxide accounts for 2.5% by mass of the catalyst, tungsten oxide accounts for 4% by mass of the catalyst, and cerium oxide accounts for 15% by mass of the catalyst carrier. The arrangement temperature is 325°C. The pre-installation test is carried out, the SCO catalyst adopts a double-layer arrangement, the direct flue gas passing rate δ is 0%, and the actual space velocity is 3100h -1 . Measured SCO unit Hg 0 The oxidation rate was 96%, and the NO oxidation rate was 58%...

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Abstract

The invention relates to a prepositioned SCO intensified flue gas denitration and demercuration technology of a coal-fired power plant. NO and Hg<0> in flue gas are oxidized into NO2 and Hg<2+> in advance and then the NO2 and the Hg<2+> are subjected to an SCR (Selective Catalytic Reduction), so that the aim of efficient denitration and demercuration is realized. A catalyst used by an SCO unit is a Co-Mn-Ti-Ce series catalyst, an active component is one or two of cobalt oxide or manganese oxide, an auxiliary agent component is W and a catalyst carrier is Ce doped TiO2. The Hg<0> can be efficiently oxidized and removed under the condition that previous facilities of the coal-fired power plant do not need to be excessively modified; the oxidization efficiency of the Hg<0> is not influenced in an ammonification process. Meanwhile, dependence on HCl is avoided when O2 and NO are used as an oxidant of the Hg<0>; the given mercury oxidization removing efficiency can be realized without adding additional components in the flue gas; a prepositioned SCO process is used for converting 50 percent of NO at an inlet of an SCR unit into the NO2, so that the reaction efficiency of the SCR process can be remarkably improved. The technology provided by the invention has the advantages that raw materials of the catalyst are easy to obtain, the technological process is easy to implement and industrial application is facilitated.

Description

technical field [0001] The invention belongs to the field of air pollution control, and in particular relates to a pre-SCO enhanced flue gas denitrification and mercury removal technology of a coal-fired power plant. Background technique [0002] With the continuous development of our country's social economy and the gradual improvement of people's living standards, the accompanying environmental pollution problems have become increasingly prominent. my country's coal-based energy structure will not change in the short term, and the environmental pollution problems of flue gas such as nitrogen oxides and sulfur oxides will become increasingly serious. At the same time, in order to meet the construction needs of ecological civilization and scientific development, the country's governance standards for atmospheric environmental pollutants are becoming more and more stringent. The latest revision of the "Emission Standards for Air Pollutants from Thermal Power Plants" was offic...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/86B01D53/60B01D53/64
CPCB01D53/8637B01D53/8665B01D2255/2073B01D2255/20746B01D2258/0283
Inventor 胡将军李鸿鹄
Owner WUHAN UNIV
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