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Method for denitration of complexing ferroporphyrin smoke based on supergravity

A super-gravity and super-gravity machine technology is applied in the field of super-gravity complex ferrous flue gas denitrification, which can solve the problems of complex process route and high operating cost, and achieve the effects of simple process, good regeneration effect and high absorption efficiency.

Inactive Publication Date: 2013-12-11
WUHAN GLT ENERGY & ENVIRONMENTAL TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Domestic scholars have reported iron filings, malic acid, vitamin C, etc. to regenerate Fe(III)EDTA, but the key problems of this technology are high operating costs and complicated process routes, and further research is needed

Method used

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  • Method for denitration of complexing ferroporphyrin smoke based on supergravity

Examples

Experimental program
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Effect test

Embodiment 1

[0021] The method for the denitrification of flue gas by complexing ferrous iron in high gravity, such as figure 1 shown, including the following steps:

[0022] 1) After dedusting and desulfurization, the flue gas is 400Nm 3 The flow rate of / h enters the supergravity machine, the NOx concentration in the flue gas is 500-800ppmv, the flue gas temperature is 120, and the flue gas and the absorbent pumped into the supergravity machine from the storage tank through the pump are in the supergravity machine rotor packing layer Countercurrent contact, reaction denitrification; absorbent composition is HEDTA, sodium sulfide, Fe 2+ and Fe 3+ , the total Fe concentration is 0.01mol / L, the molar ratio of HEDTA to total Fe is 1.02:1, the molar ratio of sodium sulfide to total iron is 5:1, the temperature of absorbent is 20°C, and the volume ratio of flue gas to absorbent is 10:1;

[0023] 2) The purified flue gas after the reaction enters the demister from the gas phase outlet of th...

Embodiment 2

[0027] The method for the denitrification of flue gas by complexing ferrous iron in high gravity, such as figure 1 shown, including the following steps:

[0028] 1) After dedusting and desulfurization, the flue gas is 400Nm 3 The flow rate of / h enters the supergravity machine, the NOx concentration in the flue gas is 500-800ppmv, the flue gas temperature is 40°C, the flue gas and the absorbent pumped into the supergravity machine from the storage tank are in the supergravity machine rotor packing layer Countercurrent contact, reaction denitrification; absorbent composition is EDTA, sodium hydrosulfide, Fe 2+ and Fe 3+ , the total Fe concentration is 0.5mol / L, the molar ratio of EDTA to total Fe is 1.5:1, the molar ratio of sodium hydrosulfide to total iron is 4:1, the temperature of absorbent is 0°C, the volume ratio of flue gas to absorbent is is 500:1;

[0029] 2) The purified flue gas after the reaction enters the demister from the gas phase outlet of the supergravity ...

Embodiment 3

[0033] The method for the denitrification of flue gas by complexing ferrous iron in high gravity, such as figure 1 shown, including the following steps:

[0034] 1) After dedusting and desulfurization, the flue gas is 400Nm 3 The flow rate of / h enters the supergravity machine, the NOx concentration in the flue gas is 500-800ppmv, the flue gas temperature is 50°C, the flue gas and the absorbent pumped into the supergravity machine from the storage tank are in the supergravity machine rotor packing layer Countercurrent contact, reaction denitrification; absorbent composition is NTA, ammonium sulfide, Fe 2+ and Fe3+ , the total Fe concentration is 0.3mol / L, the molar ratio of NTA to total Fe is 2:1, the molar ratio of ammonium sulfide to total iron is 3:1, the absorbent temperature is 55°C, and the volume ratio of flue gas to absorbent is 1000:1;

[0035] 2) The purified flue gas after the reaction enters the demister from the gas phase outlet of the supergravity machine, and...

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Abstract

The invention discloses a method for denitration of complexing ferroporphyrin smoke based on supergravity. The method comprises the following steps of feeding desulfurated smoke which is at the temperature of 40 DEG C-120 DEG C and contains NOx into a supergravity machine to carry out countercurrent contact on the smoke and an absorber which is at the temperature of 0 DEG C-55 DEG C and enters into the supergravity machine in a rotor packing layer of the supergravity machine, and reacting for denitration; feeding cleaned smoke into a demister from the air phase outlet of the supergravity machine and then entering into a discharging system; flowing denitrated rich liquor into a balance tank from the liquid phase outlet of the supergravity machine, and then flowing into a settling tank from the balance tank, so that solid in the denitrated rich liquor is settled to the bottom, filting to recover sulfur, and pumping filtrate into the settling tank; pumping out upper clear liquid to be fed into the supergravity machine to be mixed with supplemented a reducer on line, and then flowing into the supergravity machine for circular absorption and denitration. The method provided by the invention has the advantages that supergravity equipment is utilized as gas-liquid mass transfer strengthen equipment; the method is beneficial to removal of NOx, the complexing ferroporphyrin is utilized as the absorber, the absorption efficiency is high, the regeneration effect is good, an absorption liquid is applied in a circulating manner, and the denitration rate is more than 96%.

Description

technical field [0001] The invention relates to purification of industrial flue gas, in particular to a method for denitrification of flue gas by complexing ferrous iron under high gravity. Background technique [0002] The pollution of acid rain and its harm have become one of the important environmental issues concerned by countries all over the world. my country is a country where coal is the main energy source. According to survey statistics, more than 90% of SO in my country 2 、More than 67% NO X , More than 70% of the soot emissions come from the combustion of coal. The SO produced by coal combustion 2 and NO X It is the main source of industrial waste gas pollution (acid rain hazard). Nitrogen oxides can also form photochemical pollution, produce the greenhouse effect, destroy the ozone layer, and have toxic effects on the human body. Nitrogen oxides and sulfur oxides can also be converted into PM2.5 to cause haze weather. [0003] At present, the selective cat...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/78B01D53/56
Inventor 余国贤黄泽朔潘威李海峰路平吴宏观隋志军万昆
Owner WUHAN GLT ENERGY & ENVIRONMENTAL TECH CO LTD
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