CN202036918U - Novel and integrated smoke purification device for desulfurization, denitrification and removal of heavy metals - Google Patents
Novel and integrated smoke purification device for desulfurization, denitrification and removal of heavy metals Download PDFInfo
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- CN202036918U CN202036918U CN2011201059644U CN201120105964U CN202036918U CN 202036918 U CN202036918 U CN 202036918U CN 2011201059644 U CN2011201059644 U CN 2011201059644U CN 201120105964 U CN201120105964 U CN 201120105964U CN 202036918 U CN202036918 U CN 202036918U
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- absorption tower
- trapping agent
- heavy metal
- heavy
- ammonia
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Abstract
The utility model provides a novel and integrated smoke purification device for desulfurization, denitrification and removal of heavy metals, comprising an absorbing tower, an ammonia feeding device, a heavy metal trapping agent feeding device and an ozone feeding device, wherein the ammonia feeding device and the heavy metal trapping agent feeding device are communicated with the lower part of the absorbing tower; and the ozone feeding device is respectively connected with a smoke inlet pipeline and an aerator pipe arranged in the absorbing tower. The novel and integrated smoke purification device for desulfurization, denitrification and removal of the heavy metals is used for purifying smoke, the occupied area is small, the purification efficiency is high, and the utilization value of by-products is high, so that the economic benefit and the social benefit can be obviously improved.
Description
Technical field
The utility model relates to a kind of desulphurization denitration removing heavy-metal integrated fume purifier.The smoke pollution or the industrial tail gas that are applicable to industries such as fire coal, fuel oil, combustion gas thermal power plant, metallurgy, chemical industry, solid useless (rubbish) processing pollute concentrated improvement.
Background technology
At present, domestic flue gas or industrial tail gas pollution control technology are more, and wherein comparative maturity, representative technology have: administer sulfur dioxide (SO
2) limestone-gypsum method, the ammonia process that pollutes, the desulfur technology of two alkaline process; Administer SCR, the SNCR of nitrogen oxide (NOx) pollutant, the denitration technology of low nitrogen burning method.
Which kind of technology no matter just present actual conditions adopt, to sulfur in smoke (SO
2) all be in the different device of two functions, to realize there is not the technology of same set of device high-efficiency desulfurization denitration removing heavy-metal with removing of nitrogen oxide (NOx) and heavy metal.National requirements for environmental protection is to sulfur dioxide (SO
2) and the control of the disposal of pollutants concentration of nitrogen oxide (NOx) and heavy metal more and more stricter.
The utility model content
The purpose of this utility model provides a kind of desulphurization denitration removing heavy-metal integrated fume purifier, to realize sulfur dioxide in flue gas (SO
2), nitrogen oxide (NOx) and heavy metal contaminants integrated efficient remove.
The desulphurization denitration removing heavy-metal integrated fume purifier that the utility model provides comprises the absorption tower, supplies ammonia device, ozone supply device and heavy metal trapping agent feedway, be provided with spraying layer in the described absorption tower, described absorption tower is connected with smoke intake pipeline under described spraying layer, described spraying layer and bottom, described absorption tower are communicated with by the circulation pump line, described ammonia device and the described heavy metal trapping agent feedway of supplying is communicated with bottom, described absorption tower, and described ozone supply device connects described smoke intake pipeline and the aeration tube that is arranged in the described absorption tower respectively.
Preferably, described desulphurization denitration removing heavy-metal integrated fume purifier also comprises: slurries excavationg pump, the clean flue that is used to discharge clean flue gas that links to each other with top, described absorption tower that links to each other by discharge line with bottom, described absorption tower, the flushing water pipeline that is used to provide the demist water that is arranged at the demister that is positioned at described spraying layer top in the absorption tower and flushing water layer and links to each other with described flushing water layer.
Preferably, described ozone supply device comprises the air separation unit and the ozone generator of connection.
Preferably,, described confession ammonia device comprises tank used for storing ammonia and supplies ammonia pump.
Preferably,, described heavy metal trapping agent feedway comprises heavy metal trapping agent storage tank and heavy metal trapping agent pump.
The desulphurization denitration removing heavy-metal integrated fume purifier that the utility model provides, owing in a cover absorption plant, realize desulfurization, denitration, removing heavy-metal function, therefore the flue gas system resistance of package unit is only suitable with existing limestone-gypsum method, adds SCR denitration layout with wet desulphurization and has reduced about 30% area.Utilize the utility model to carry out gas cleaning, area occupied is little, and accessory substance value height makes economic benefit, and social benefit can access remarkable increase.
Description of drawings
Fig. 1 is the user mode structural representation of desulphurization denitration removing heavy-metal integrated fume purifier of the present utility model.
Among the figure: the former flue of 1-, 2-booster fan, 3-absorption tower, the 4-demister, the clean flue of 5-, 6-chimney, 7-bypass flue, 8-flushing water pipeline, 9-circulating pump, the 10-excavationg pump, 11-slurries discharge line, 12-air duct, the 13-air separation unit, 14-ozone generator, 15-ozone pipeline, the 16-tank used for storing ammonia, 17-is for ammonia pump, 18-heavy metal trapping agent pump, 19-heavy metal trapping agent storage tank, 20-dust separator, 21-economic benefits and social benefits separator, the 22-multi-effect evaporation system, 23-chemical fertilizer drying system, 24-ammonium sulfate, ammonium nitrate fertilizer output end, 25-heavy metal trapping agent pipeline, the 26-spraying layer, 27-washes water layer.
The specific embodiment
Describe below in conjunction with the user mode of accompanying drawing a kind of desulphurization denitration removing heavy-metal integrated fume purifier of the present utility model.
As shown in Figure 1, this desulphurization denitration removing heavy-metal integrated fume purifier mainly comprises absorption tower 3, air separation unit 13, ozone generator 14, tank used for storing ammonia 16, supplies ammonia pump 17, heavy metal trapping agent pump 18 and heavy metal trapping agent storage tank 19.Absorption tower 3 is the hollow-spraying-tower tower.Air separation unit 13 and ozone generator 14 constitute the ozone supply device, and air separation unit 13 is connected with air duct 12, is used for bubbling air, isolates oxygen; Ozone generator 14 is connected with ozone pipeline 15, and ozone pipeline 15 one road inserts former flue, and another road is inserted in the absorption tower 3.Smoke intake pipeline is communicated with former flue 1 by booster fan 2, and former flue 1 also connects clean flue 5 by bypass flue 7, and the two ends of clean flue 5 are communicated with absorption tower 3 and chimney 6 respectively.Tank used for storing ammonia 16 and confession ammonia pump 17 constitute for ammonia device, insert 3 bottoms, absorption tower (being the slurries ponds), heavy metal trapping agent storage tank 19 and heavy metal trapping agent pump 18 constitute heavy metal trapping agent feedway, insert 3 bottoms, absorption tower by heavy metal trapping agent pipeline 25, realize the circulation absorption of slurries by circulating pump 9 is set between the spraying layer 26 on absorption tower 3 and the bottom on absorption tower 3.The bottom on absorption tower 3 also is connected with excavationg pump 10 and slurries discharge line 11, is used for slurries are discharged.The top on absorption tower 3 also is connected with flushing water layer 27, and the flushing water layer can be sprayed water and be absorbed the ammonia of escaping.The top on absorption tower 3 can also be provided with demister 4.This device also comprises dust separator 20, economic benefits and social benefits separator 21, multi-effect evaporation system 22, chemical fertilizer drying system 23 and ammonium sulfate, ammonium nitrate fertilizer output end 24.
Below in conjunction with Fig. 1 the technological process that utilizes described desulphurization denitration removing heavy-metal integrated fume purifier is described further.The flue gas that enters from former flue 1 mixes ozone (O through booster fan 2 with the ozone that comes through 15 supplies of ozone pipeline
3) nitric oxide in the flue gas (NO) can be oxidized to nitrogen dioxide (NO substantially
2), entering absorption tower 3 afterwards, the flue gas that enters absorption tower 3 upwards flows through spraying layer, sulfur in smoke (SO
2), the absorption liquid reaction absorbing and removing that contains ammoniacal liquor and heavy metal trapping agent that sprayed by spraying layer of nitrogen oxide (NOx), heavy metal, washing absorbing and removing sulfur dioxide (SO
2), the clean flue gas behind the nitrogen oxide (NOx), heavy metal, remove droplet through demister 4 again after, through clean flue 5 by chimney 6 dischargings.The absorption liquid of 3 bottoms, absorption tower keeps certain liquid level, to guarantee the reaction time.After absorption liquid was transported to the spraying layer nozzle atomization by circulating pump 9, washing absorbed sulfur in smoke (SO
2), nitrogen oxide (NOx), heavy metal.The ammoniacal liquor utilization of tank used for storing ammonia 16 adds the bottom, absorption tower for ammonia pump 17.Ozone is to make purity oxygen through air separation unit 13, forms through ozone generator 14 ionization again, establishes ozone (O in the absorption tower
3) aeration tube.Ozone (O
3) be uniformly distributed in the absorption tower by aeration tube, being used for sulfite oxidation is ammonium sulfate, nitrous acid is oxidized to nitric acid.
As removing the mixed liquor that absorbent is ammoniacal liquor and heavy metal trapping agent.Ammoniacal liquor can be prepared with liquefied ammonia, also available ammonia or urea production.As long as can satisfy the system held water balance, the concentration of ammoniacal liquor does not have specific (special) requirements.Absorbent adds below liquid level.When adding the implantation site difference, the escapement ratio of ammonia is slightly different.The heavy metal trapping agent is the general designation to reagent that can the adsorbing separation heavy metal ion, and the principle of absorption can also chemical reaction can take place for physical absorption.In the commercially available prod, heavy metal trapping agent weigh again metal agent for capturing or heavy metal chelating agent, kind has the mixture of xanthate class, dithiocarbamate salt derivative, synthetic high polymer class, multiple organic compound etc.Can choose suitable heavy metal trapping agent according to the composition and the reaction condition in the reaction tower of heavy metal in the flue gas.
Ozone (O
3) nitric oxide in the flue gas (NO) is oxidized to nitrogen dioxide (NO
2) or nitrogen trioxide (N
2O
3), dinitrogen pentoxide (N
2O
5) etc.; Nitric oxide (NO) is oxidized to higher nitrogen oxides (NOx) substantially in the former flue gas (being untreated flue gas).The ozone supply device is after the pipeline incoming end of ozone supply can be arranged on air-introduced machine in former flue gas or behind the booster fan.Stock tank at utmost is oxidized to ammonium sulfate, ammonium nitrate with the ammonium sulfite in the slurries in the tower, ammonium nilrite in another road ozone injection tower.Ozone (O
3) can make purity oxygen through air separation unit, again through ozone (O
3) generator ionization forms; Also available air is directly passed through ozone (O
3) generator ionization makes.
Absorption liquid is transported to the spraying layer at absorption tower middle part by circulating pump, and former flue gas enters behind the described absorption plant upwards through described spraying layer, the SO in the former flue gas
2, NOx and heavy metal be absorbed by liquid absorption and remove.
Reach certain density slurries, get rid of through the slurries excavationg pump, the slurries of eliminating can at first come out dust separation by centrifugal separator, afterwards, deliver to evaporation and crystallization system and handle.Nitrogen element in the final nitrogen oxide (NOx) is transformed in the ammonium nitrate.Final sulfur dioxide (SO
2) be removed and react generation ammonium sulfate.
Heavy metal is rich to be amassed behind finite concentration, carries out desorption, and the heavy metal that desorption goes out is concentrated and carried out harmless treatment.
Utilize this desulphurization denitration removing heavy-metal integrated fume purifier, nitrogen oxide (NOx) content is reduced to below the 50mg in the clean flue gas.The height of denitration efficiency depends on the control of oxidation of nitric oxide rate.Clean sulfur dioxide in flue gas (SO
2) content is reduced to below the 50mg.The efficient of removing heavy-metal is more than 90%.Utilizing described desulphurization denitration removing heavy-metal integrated fume purifier also to overcome other removes technology and easily generates the difficult oxidation of ammonium sulfite, nitrous acid in aerosol and the saline solution, ammonium sulfate, the inferior shortcoming of ammonium nitrate.
After ammonium sulfate, ammonium nitrate solution reached certain concentration, slurries were discharged through excavationg pump 10.The slurries of discharging at first come out dust separation by centrifugal separator, afterwards, through the economic benefits and social benefits separator heavy metal trapping agent are separated with saline solution, and it is recycling that isolated heavy metal trapping agent returns tower; Saline solution is delivered to evaporation and crystallization system and is handled, and obtains byproduct of ammonium sulfate, ammonium nitrate fertilizer, and the quality of ammonium sulfate, ammonium nitrate products reaches Grade A.
Claims (5)
1. desulphurization denitration removing heavy-metal integrated fume purifier, it is characterized in that, comprise the absorption tower, supply ammonia device, ozone supply device and heavy metal trapping agent feedway, be provided with spraying layer in the described absorption tower, described absorption tower is connected with smoke intake pipeline under described spraying layer, described spraying layer and bottom, described absorption tower are communicated with by the circulation pump line, described ammonia device and the described heavy metal trapping agent feedway of supplying is communicated with bottom, described absorption tower, and described ozone supply device connects described smoke intake pipeline and the aeration tube that is arranged in the described absorption tower respectively.
2. desulphurization denitration removing heavy-metal integrated fume purifier according to claim 1, it is characterized in that, also comprise: slurries excavationg pump, the clean flue that is used to discharge clean flue gas that links to each other with top, described absorption tower that links to each other by discharge line with bottom, described absorption tower, the flushing water pipeline that is used to provide the demist water that is arranged at the demister that is positioned at described spraying layer top in the absorption tower and flushing water layer and links to each other with described flushing water layer.
3. desulphurization denitration removing heavy-metal integrated fume purifier according to claim 1 is characterized in that described ozone supply device comprises the air separation unit and the ozone generator of connection.
4. desulphurization denitration removing heavy-metal integrated fume purifier according to claim 1 is characterized in that, described confession ammonia device comprises tank used for storing ammonia and supplies ammonia pump.
5. desulphurization denitration removing heavy-metal integrated fume purifier according to claim 1 is characterized in that described heavy metal trapping agent feedway comprises heavy metal trapping agent storage tank and heavy metal trapping agent pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201059644U CN202036918U (en) | 2011-04-12 | 2011-04-12 | Novel and integrated smoke purification device for desulfurization, denitrification and removal of heavy metals |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201059644U CN202036918U (en) | 2011-04-12 | 2011-04-12 | Novel and integrated smoke purification device for desulfurization, denitrification and removal of heavy metals |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202036918U true CN202036918U (en) | 2011-11-16 |
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ID=44964384
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201059644U Expired - Lifetime CN202036918U (en) | 2011-04-12 | 2011-04-12 | Novel and integrated smoke purification device for desulfurization, denitrification and removal of heavy metals |
Country Status (1)
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|---|---|
| CN (1) | CN202036918U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102188883A (en) * | 2011-04-12 | 2011-09-21 | 王晓晔 | Novel smoke purification process and device capable of integrally desulphurizing, denitrifying and removing heavy metals |
-
2011
- 2011-04-12 CN CN2011201059644U patent/CN202036918U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102188883A (en) * | 2011-04-12 | 2011-09-21 | 王晓晔 | Novel smoke purification process and device capable of integrally desulphurizing, denitrifying and removing heavy metals |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20111116 |