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Denitration synergist and SNCR (selective non-catalytic reduction) denitration synergism method

A synergist and denitrification technology, applied in the field of flue gas denitrification, can solve the problems of complicated process, expensive hydrazine, and poor practicability, and achieve the effect of strong industrial applicability and improved denitrification efficiency

Inactive Publication Date: 2014-05-07
HANGZHOU TIANLAN ENVIRONMENTAL PROTECTION EQUIP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The present invention provides a denitrification synergist and a SNCR denitrification synergistic method, which mainly solves the problem in the prior art that the temperature window still needs a medium and high temperature during SNCR denitration, and the temperature window is not wide; The oxygen content does not exceed 9%, and the oxygen content in the middle temperature zone is less than 17%. The process is more complicated and difficult to operate; moreover, the price of hydrazine as a rocket propellant is relatively expensive, the industrial application cost is high, and the practicability is not strong. Technical problems such as

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] Embodiment 1: a kind of denitrification synergist and SNCR denitrification synergist method of this example, its steps are:

[0034] a. Weigh 0.1kg ammonium metavanadate, 0.1kg tungsten trioxide, 0.1kg molybdenum trioxide, 0.1kg ammonium molybdate, 0.1kg copper hydroxide, mix evenly to obtain denitrification synergist;

[0035] b. Dissolve the denitrification synergist in 100kg of ammonia water, stir for 1 hour to mix the denitrification synergist and reducing agent evenly, let it stand for 2 hours, and then spray it into the furnace.

Embodiment 2

[0036] Embodiment 2: a kind of denitration synergist and SNCR denitration synergistic method of this example, its steps are:

[0037] a. Weigh 0.5kg ammonium metavanadate, 0.5kg tungsten trioxide, 0.5kg molybdenum trioxide, 0.5kg ammonium molybdate, 0.2kg copper hydroxide, mix well to obtain denitrification synergist;

[0038] b. Dissolve the denitrification synergist A in 100kg of ammonia water, stir for 1.5 hours to mix the denitrification synergist and reducing agent evenly, and spray it into the furnace after standing for 1.5 hours.

Embodiment 3

[0039] Embodiment 3: a kind of denitrification synergist and SNCR denitration synergist method of this example, its steps are:

[0040] a. Weigh 1.0kg ammonium metavanadate, 1.0kg tungsten trioxide, 0.8kg molybdenum trioxide, 0.8kg ammonium molybdate, 0.4kg copper hydroxide, and mix evenly to obtain denitrification synergist;

[0041] b. Dissolve the denitrification synergist in 100kg of ammonia water, stir for 1 hour to mix the denitrification synergist and reducing agent evenly, let it stand for 2 hours, and then spray it into the furnace.

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Abstract

The invention discloses an SNCR (selective non-catalytic reduction) denitration synergism method and a denitration synergist. Some soluble metal compounds and accessory ingredients are added into an SNCR reducing agent to prepare the denitration synergist; when the reducing agent is sprayed into a hearth, metal oxides with SCR activity are generated in a high-temperature environment and have an effect ofcatalyzing reaction of NH3 and NOx; along with the flowing of smoke, SCR denitration reaction is realized, and the smoke is removed through a subsequent dust removal device. The denitration synergist is prepared from the following raw materials in parts by mass: 0.1-5.5 parts of ammonium metavanadate, 0.1-13.8 parts of tungsten trioxide, 0.1-18 parts of molybdenum trioxide, 0.1-27 parts of ammonium molybdate and 0.1-1.1 parts of copper hydroxide according to 100 parts of ammonia water. According to the SNCR denitration synergism method and the denitration synergist, the denitration reaction can be continued in a subsequent flue instead of being restrained within a temperature window of 850-1,100 DEG C, and can generate in a temperature window at 250-1,100 DEG C, so that the overall denitration efficiency is effectively improved, and extremely high industrial practicality is achieved.

Description

technical field [0001] The invention relates to the technical field of flue gas denitrification, in particular to a denitrification synergist and a SNCR denitrification synergistic method. Background technique [0002] SNCR denitrification technology is a clean denitrification technology that sprays an amino-containing reducing agent into the furnace within a certain temperature range to reduce and remove NOx in the flue gas to generate nitrogen and water without using a catalyst. SNCR denitrification technology generally uses ammonia water as the reducing agent, NH 3 The reduction reaction with NOx is very sensitive to temperature conditions, and it is generally believed that the ideal temperature range is 850-1100°C, which varies with the type of reactor. SNCR technology has the advantages of simple economy, convenient operation, low price, etc., and has been widely used. However, when the temperature is lower than the temperature window, due to the limitation of the res...

Claims

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Application Information

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IPC IPC(8): B01D53/90B01D53/56
Inventor 舒欢忠王岳军王瑞祥刘学炎舒坑忠
Owner HANGZHOU TIANLAN ENVIRONMENTAL PROTECTION EQUIP