Desulfurization, denitration and dust removal integrated process

A desulfurization, denitrification and process technology, applied in gas treatment, chemical instruments and methods, dispersed particle separation, etc., can solve the problems of high water content, high investment, high risk of combustion and explosion, and achieve small footprint, low investment cost, Set up flexible effects

Pending Publication Date: 2021-10-29
淮南市明月环保科技有限责任公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] At present, the most widely used desulfurization technology is the wet lime-gypsum method, which has the following problems: 1) The desulfurization pipeline is easily blocked; 2) The utilization rate of absorbent raw materials is low; 3) Calcium sulfite is difficult to oxidize, and the power consumption of the oxidation fan is large; 4) The by-product calcium sulfate is viscous, difficult to filter, and has a high water content; 5) The quality of the by-product calcium sulfate is low;
[0003] At present, the most widely used denitrification technology at home and abroad is medium-high temperature SCR denitrification. The application characteristic of this method is that it needs a suitable temperature zone. , there is no temperature zone required for medium and high temperature SCR denitration. This method has three major problems in the treatment of flue gas in these industries: 1) heating is required, which consumes huge energy; 2) heat exchange and other facilities need to be installed, which prolongs the process and expands the capacity Investment; 3) Catalyst consumption is large and loss is large
[0004] For the dust removal ultra-low emission transformation, the "wet electricity" process is generally used, and there are three major problems: 1) The effect of wet electricity is greatly affected by the desulfurization system, and the demisting function itself is gradually reduced; 2) The addition of wet electricity dust removal requires high investment and low operation High cost; 3) Wet electricity requires a high-voltage electric field, and the risk of combustion and explosion is high

Method used

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  • Desulfurization, denitration and dust removal integrated process
  • Desulfurization, denitration and dust removal integrated process
  • Desulfurization, denitration and dust removal integrated process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] Example 1 is an example of an integrated process for low-sulfur flue gas desulfurization, denitration and dust removal.

[0043] figure 1 Medium desulfurization, denitrification and dust removal integrated tower 1, swirl plate 2, electrocatalytic layer 3, penetrating liquid film layer 4, demister layer 5, chimney 6, washing spray layer 7, absorption spray layer 8, absorption circulation pump 9 , washing circulation pump 10, filter pump 11, filter 12; flue gas A, purified flue gas B, ammonia water C, washing process water D, solid residue E.

[0044] The desulfurization, denitrification and dust removal integrated tower 1 is equipped with double circulation, with swirl plates 2, 3 electrocatalytic layers 3, penetrating liquid film layers 4 and demisting layers 5 arranged from bottom to top, and 4 absorption spray layers 8 and 1 layer of washing and spraying layer 7; the electrocatalytic reaction layer is composed of supports, electrodes and electroactive fillers, and th...

Embodiment 2

[0049] Example 2 is an example of the integrated desulfurization, denitrification and dust removal process of the tower and pond.

[0050] figure 2 Medium desulfurization, denitrification and dust removal integrated tower 1, chimney 2, slurry tank 3, gypsum whisker preparation tank 4, clear water tank 5, absorption circulation pump 6, washing circulation pump 7, lime automatic dosing device 8, filter pump 9, filter 10; Flue gas A, purified flue gas B, lime C, washing process water D, ammonia water E, gypsum whiskers F.

[0051] The desulfurization, denitrification and dust removal integrated tower 1 is equipped with double circulation, and a conjoined chimney 2 is installed. The conjoined pool is divided into three parts: a slurry pool 3, a gypsum whisker preparation pool 4 and a clear water pool 5;

[0052] Process: The flue gas A enters the bottom of the desulfurization, denitrification and dust removal integrated tower 1, and is in countercurrent contact with the absorption...

Embodiment 3

[0056] Embodiment 3 is an example of the integrated process of desulfurization, denitrification and dust removal of tower pool split.

[0057] image 3 Medium desulfurization, denitrification and dust removal integrated tower 1, slurry tank 2, transition slurry tank 3, gypsum whisker preparation tank 4, clear water tank 5, reflux tank 6, absorption circulation pump 6, lime automatic dosing device 7, vacuum belt filter 8 , a gas-liquid separator 9, a vacuum pump 10, a filter 11, an absorption circulation pump 12, and a washing circulation pump 13; communication gaps a1, a2, a3, a4, a5 between the pools, outlet b1 at the bottom of the tower, and outlet b2 for washing water; Flue gas A, purified flue gas B, lime C, washing process water D, ammonia water E, gypsum whiskers F, suction filter exhaust gas G.

[0058] Desulfurization, denitrification and dust removal integrated tower 1 is equipped with double circulation, and a conjoined chimney is installed. The split pool is divide...

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Abstract

The invention relates to a desulfurization, denitrification and dust removal integrated process. According to the process, flue gas is fed into a desulfurization, denitrification and dust removal integrated tower by an induced draft fan, the flue gas moves from bottom to top, spraying liquid moves from top to bottom, an electroactive substance is selected as a catalytic reaction medium when a gas-liquid phase of the flue gas passes through an electrocatalytic reaction layer, under the effect of an electric field, an electro-catalytic reaction is carried out on the surface area of the electroactive substance, ammonia or urea in the circulating liquid is absorbed as a reducing agent to enable NOx to generate N2, meanwhile, desulfurization is carried out, then the flue gas passes through a liquid film washing layer to achieve the dust removal effect, and the purified flue gas is sent to a chimney for up-to-standard emission. The desulfurization, denitrification and dust removal integrated process has the following beneficial effects: (1) desulfurization, denitrification and dust removal cooperate with each other, and the problem of flue gas treatment is solved with high efficiency and low cost; (2) a high-consumption and high-pollution process is changed into a production process with product value; (3) denitration is not limited by temperature; (4) the problems of entrainment, soluble salt taking-out and ammonia escape in wet desulphurization are solved; and (5) the occupied area is small, and the investment cost is low.

Description

technical field [0001] The invention belongs to the field of boiler tail gas treatment. The invention relates to an integrated process of desulfurization, denitrification and dust removal, which is used to remove SO in flue gas 2 , NOx and dust, more specifically, the desulfurization, denitrification and dust removal are completed in a main absorption tower equipment, which occupies a small area, has a small investment in equipment, and has good effects. net emission standards. Background technique [0002] At present, the most widely used desulfurization technology is the wet lime-gypsum method, which has the following problems: 1) The desulfurization pipeline is easily blocked; 2) The utilization rate of absorbent raw materials is low; 3) Calcium sulfite is difficult to oxidize, and the power consumption of the oxidation fan is large; 4) The by-product calcium sulfate is viscous, difficult to filter, and has a high water content; 5) The quality of the by-product calcium ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/75B01D53/78B01D53/86B01D53/96B01D53/56
CPCB01D53/75B01D53/78B01D53/8631B01D53/96B01D2258/0283
Inventor 徐继红陶俊
Owner 淮南市明月环保科技有限责任公司
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