CN201669049U - Deodorizing device - Google Patents
Deodorizing device Download PDFInfo
- Publication number
- CN201669049U CN201669049U CN2010201837260U CN201020183726U CN201669049U CN 201669049 U CN201669049 U CN 201669049U CN 2010201837260 U CN2010201837260 U CN 2010201837260U CN 201020183726 U CN201020183726 U CN 201020183726U CN 201669049 U CN201669049 U CN 201669049U
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- CN
- China
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- tower body
- spray equipment
- circulation fluid
- fluid case
- inner core
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- Expired - Lifetime
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Abstract
The utility model relates to the technical field of an odor treatment device, in particular to a deodorizing device which carries out purifying treatment on odor of an early-stage piling bin for household refuse burning treatment and odorous gases containing organic sulfur and organic amine in chemical plants. A tower body of the deodorizing device is positioned above a circulating liquid box; the lower part of the tower body is provided with an inner barrel; the bottom of the inner barrel is communicated with the circulating liquid box; a cavity between the inner barrel and the tower body is internally provided with a first spraying device; the circulating liquid box is internally provided with a bubbling pipe; the upper end of the bubbling pipe is introduced into the cavity between the inner barrel and the tower body; the position on the tower body, where the inner barrel is arranged, is provided with an odor inlet, the top end of the tower body is provided with an odor outlet and the tower body is internally provided with a second spraying device; and the odor chemically reacts with atomized potassium permanganate sprayed by the first spraying device and the second spraying device and potassium permanganate solution in the circulating liquid box. The deodorizing device solves the technical problems that the existing deodorizing method has low treatment efficiency, large equipment, difficult after treatment and high equipment operating cost.
Description
Technical field
The utility model relates to foul smell treating apparatus technical field, particularly a kind of consumer waste incineration is handled the odor removal that carries out purified treatment that foul smell, the chemical plant of stacking the storehouse early stage contain organic sulfur and organic amine foul gas.
Background technology
Domestic rubbish disposal both at home and abroad at present has three kinds of methods; A kind of is to bury in the wasteland, gully in no value, allows it rot naturally to decompose, and is utilized by plant absorbing; The 2nd, utilize biofermentation that rubbish is converted into organic fertilizer; The 3rd, direct high temperature incineration, the waste heat of generation are used for generating electricity or are used for industry, life heat supply.The above two degradation speeds are too slow, can't satisfy the needs of Modern Urban Development at all.And the latter has become the main means of treatment of urban garbage.The velocity-stabilization of burning facility disposal of refuse, but the generation velocity perturbation of rubbish is very big, must build the interim storage warehouse of rubbish.Concentrate in transhipment and the storage process at rubbish, rubbish rotten degraded under bacterial action discharges very unpleasant foul gas and causes serious air pollution.The composition of this gas is very complicated, and its main component is: ammonia (NH
3), hydrogen sulfide (H
2S), methyl mercaptan (CH
3SH), methyl sulfide ((CH
3)
2S), formic acid (HCOOH), ethanol (CH
3CH
2OH), sulfur dioxide (SO
2), propionic aldehyde (CH
3CH
2CHO), propionic acid (CH
3CH
2COOH), acetone (CH
3COCH
3), butyric acid (CH
3CH
2CH
2COOH), dimethylamine ((CH
3)
2NH), methyl disulfide (C
2H
6S
2), methyl alcohol (CH
3OH), nitrous oxide (N
2O), methane (CH
4), trimethylamine ((CH
3)
3N), monomethyl amine (CH
3NH :), acetaldehyde (CH
3CHO), indoles (C
8H
7N), styrene (C
6H
5CHCH
2) etc.Gas with obvious stink is: ammonia (NH
3), hydrogen sulfide (H
2S), methyl mercaptan (CH
3SH), methyl sulfide ((CH
3)
2S), formic acid (HCOOH), sulfur dioxide (SO
2), propionic aldehyde (CH
3CH
2CHO), dimethylamine ((CH
3)
2NH), methyl disulfide (C
2H
6S
2), nitrous oxide (N
2O), trimethylamine ((CH
3)
3N), monomethyl amine (CH
3NH
2) etc.Though these materials only account for ten thousand of gas gross/several a few millionths that arrive, stench is unpleasant.
The scheme that refuse odor is handled has biological degradation method, plasma decomposition, ozone oxidation, charcoal absorption etc. at present.Wherein people's utility model such as Zhang She plasma deodorization technology (patent CN101279101A), utilize plasma that the high frequency highfield produces with the foul smell molecular breakdown.This method energy consumption is big, and the super-pressure electric field easily causes electromagnetic radiation, and treatment effeciency is not high, and produces a large amount of nitric oxides and nitrogen dioxide gas, causes secondary pollution.People such as He Pinjing utilize biotechnology to remove materials (patent CN1351897A) such as sulfur dioxide in the foul smell, mercaptan.This method processing speed is very slow, and equipment is huge, and the post processing difficulty is difficult to satisfy garbage disposal requirement in enormous quantities.Ni Ping adopts ozonation technology with foul smell molecular breakdown (CN201006041Y).The ozonation technology that people such as Zhang She adopt on the basis of patent CN101279101A.Rush down but strong oxidizing property gas---ozone is outer easily, environment is caused secondary pollution.Active carbon adsorption efficient is not high, and active carbon is saturated easily, needs continually the active carbon processing of regenerating, the recovery time of active carbon is grown and relatively bothers and difficulty, active carbon is shorter service life, needs often to change active carbon, so equipment operating cost height.
The utility model content
The technical problems to be solved in the utility model is: it is slow to solve existing deodorizing method processing speed, treatment effeciency is not high, equipment is huge, the post processing difficulty, be difficult to satisfy garbage disposal requirement in enormous quantities, the technical problem that equipment operating cost is high, the utility model provides a kind of odor removal, utilize this odor removal that foul smell is carried out purified treatment, little molecule and potassium permanganate reaction nearly all in the gas are all oxidized, and product is nonpoisonous and tasteless carbon dioxide or water miscible organic acid and sulfuric acid; Energy is the pollution abatement problem thoroughly, and equipment investment is little, and operating cost is low.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of odor removal, have tower body, circulation fluid case and circulating pump, tower body is positioned at circulation fluid case top, in the circulation fluid case liquor potassic permanganate is housed, inner core is arranged at the tower body bottom, fixedly connected with the tower body inner wall sealing in the inner core upper end, inner core lower end and circulation fluid case upper wall are sealedly and fixedly connected, interior tube bottom communicates with casing, first spray equipment and bubbling pipe are housed in the cavity between inner core and tower body, and insert in the liquor potassic permanganate of circulation fluid case the bubbling pipe lower end; Be equipped with on the tower body at inner core position and offer air inlet, there is the gas outlet on the tower body top, second spray equipment is equipped with on tower body top, and the liquid sucting port of circulating pump submerges in the liquor potassic permanganate in the circulation fluid case, and the liquid outlet of circulating pump connects first spray equipment and second spray equipment respectively by pipeline.
The utility model is handled foul smell with the strong oxidizer liquor potassic permanganate, thoroughly the pollution abatement problem.Reaction principle:
5H
2S+6KMnO
4+H
2SO
4→3K
2SO
4+3MnSO
4+6H
2O
CH
3SH+KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+CO
2+H
2O
CH
3)
2S++KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+CO
2+H
2O
HCOOH++KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+CO
2+H
2O
CH
3CH
2OH+KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+CO
2+H
2O
SO
2+KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+H
2O
CH
3CH
2CHO++KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+CO
2+H
2O
(CH
3)
2NH+KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+CO
2+N
2+H
2O
(C
2H
6S
2)+KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+CO
2+H
2O
CH
3OH+KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+CO
2+H
2O
N
2O+KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+HNO
3+H
2O
CH
3)
3N+KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+N
2+CO
2+H
2O
CH
3NH
2++KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+N
2+CO
2+H
2O
CH
3CHO+KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+CO
2+H
2O
C
8H
7N+KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+N
2+CO
2+C
6H
5CO
2H+H
2O
C
6H
5CHCH
2+KMnO
4+H
2SO
4→K
2SO
4+MnSO
4+C
6H
5CO
2H+CO
2+H
2O
NH
3+H
2SO
4→(NH
4)
2SO
4
Little molecule and potassium permanganate reaction nearly all in the gas are all oxidized, and product is nonpoisonous and tasteless carbon dioxide or water miscible organic acid and sulfuric acid.
Be to improve the utilization rate of liquor potassic permanganate, prevent that vaporific potassium permanganate from discharging tower body with gas, in the tower body of described second spray equipment top demist is housed and catches drip apparatus.
For saving the installing space of odor removal, make the odor removal compact conformation, described circulating pump is fixedly mounted on the circulation fluid case.
For improving the automaticity of odor removal, described odor removal also has highly concentrated solution case and solution pump, the liquor potassic permanganate of high concentration is housed in the highly concentrated solution case, and the solution pump liquid sucting port submerges in the liquor potassic permanganate of high concentration, and the liquid outlet of solution pump connects the circulation fluid case.The solution concentration measurement mechanism is housed in the circulation fluid case, when mensuration liquor potassic permanganate concentration is lower than setting value, pumps in the circulation fluid case by the liquor potassic permanganate of solution pump with the high concentration in the highly concentrated solution case.
For further improving gas purifying effect, the 3rd spray equipment is housed in the described inner core, the liquid outlet of circulating pump connects the 3rd spray equipment by pipeline.
For improving the fogging degree of liquor potassic permanganate, form littler droplet, described first spray equipment and second spray equipment are ultrasonic ultrasonic delay line memory.Utilize the ultrasonic atomizatio liquor potassic permanganate to form strong oxidizing property, bigger serface mist attitude strong oxidizer liquid and foul gas (hydrogen sulfide, little molecule thioether, mercaptan, organic amine etc.) redox reaction fully takes place, generate nontoxic carbon dioxide or organic acid, react more abundant, gas purifying effect is better.
For ease of the odor removal manufacturing and be convenient to the transportation, described tower body is a split-type structural, described tower body comprises tower body, middle tower body and following tower body, all there is adpting flange the upper end of the lower end of last tower body, the top and bottom of middle tower body, following tower body, offer bolt hole on the adpting flange, last tower body, middle tower body and following tower body are bolted to connection and are integral.
Utilize aforesaid odor removal to carry out the method for deodorizing, has following processing step: foul smell is blasted cavity between inner core and tower body by air inlet by air blast, behind the liquor potassic permanganate generation chemical reaction of the atomizing that sprays with first spray equipment in the cavity of foul smell between inner core and tower body, enter the circulation fluid case by bubbling pipe, liquor potassic permanganate generation chemical reaction in foul smell and the circulation fluid case, then, emerge the liquor potassic permanganate of gas in the circulation fluid case, carry out chemical reaction with the liquor potassic permanganate of the atomizing of second spray equipment in tower body ejection, purified gas is discharged tower body by exhaust outlet.
The beneficial effects of the utility model are, odor removal of the present utility model, compact conformation, first spray equipment and second spray equipment all adopt ultrasonic ultrasonic delay line memory, the liquor potassic permanganate of strong oxidizing property forms the specific area of super large behind ultrasonic atomizatio, enlarged the gas-liquid contact area, helped absorption and the reaction of solution gas.Because atomizing has reduced the volume of drop, has improved the gas-liquid contact area, the suspension time of drop in air-flow prolongs, and reaction is thorough, so the circular flow of the liquid of demand is little.The utility model utilizes the liquor potassic permanganate of strong oxidizing property to handle foul smell, the potassium permanganate of the atomizing in the cavity of foul smell elder generation between inner core and tower body carries out chemical reaction, again with the circulation fluid case in liquor potassic permanganate carry out chemical reaction, at last, the potassium permanganate of the atomizing that sprays with second spray equipment in tower body carries out chemical reaction, foul smell is through four chemical reactions, good purification, since in the gas total amount of odorant itself seldom, also few to the demand of the liquor potassic permanganate that recycles.Therefore, equipment operating cost is lower.
Description of drawings
Fig. 1 is the structural representation of the specific embodiment of odor removal of the present utility model.
Fig. 2 is the A-A cutaway view of Fig. 1.
Among the figure: 1. tower body, 1-1. air inlet, 1-2. gas outlet, the last tower body of 1-3,1-4. middle tower body, tower body under the 1-5., 2. circulation fluid case, 3. in tube stent, 4. liquor potassic permanganate, 5. inner core, 6. first spray equipment, 7. bubbling pipe, 8. second spray equipment, 9. drip apparatus is caught in demist, 10. highly concentrated solution case, 10-1. dog-house, 11. bolts, 12. the circulation pump seat, 13. the 3rd spray equipments, 14. highly concentrated solution pump seats.
The specific embodiment
The specific embodiment of odor removal of the present utility model as depicted in figs. 1 and 2, it has tower body 1, circulation fluid case 2, circulating pump (not shown), highly concentrated solution case 10 and solution pump (not shown), tower body 1 is positioned at circulation fluid case 2 tops, liquor potassic permanganate 4 is housed in the circulation fluid case 2, the liquor potassic permanganate of high concentration is housed in the highly concentrated solution case 10, offer dog-house 10-1 on the highly concentrated solution case 10, the solution pump liquid sucting port submerges in the liquor potassic permanganate of high concentration, and the liquid outlet of solution pump connects circulation fluid case 2.Inner core 5 is arranged at tower body 1 bottom, fixedly connected with tower body 1 inner wall sealing in inner core 5 upper ends, inner core 5 lower ends and circulation fluid case 2 upper walls are sealedly and fixedly connected, inner core 5 bottoms communicate with circulation fluid case 2, be positioned at inner core 5 belows in the circulation fluid case 2 and also have tube stent 3, fixedlying connected with circulation fluid case 2 upper walls in the upper end of interior tube stent 3, fixedlys connected with the diapire of circulation fluid case 2 in the lower end.First spray equipment 6 and bubbling pipe 7 are housed in the cavity that inner core 5 and tower body are 1, and directly insert in the liquor potassic permanganate 4 in the circulation fluid case 2 bubbling pipe 7 lower ends; Be equipped with on the tower body 1 at inner core 5 positions and offer air inlet 1-1, there is gas outlet 1-2 on tower body 1 top, tower body 1 internal upper part is equipped with second spray equipment 8, the 3rd spray equipment 13 is housed in the inner core 5, the liquid sucting port of circulating pump submerges in the liquor potassic permanganate in the circulation fluid case 2, and the liquid outlet of circulating pump connects first spray equipment 6, second spray equipment 8 and the 3rd spray equipment 13 respectively by pipeline.In the tower body 1 of second spray equipment, 8 tops demist is housed and catches drip apparatus 9, circulation pump seat 12 is housed on the circulation fluid case 2, circulating pump is fixedly mounted on the circulation pump seat 12 on the circulation fluid case 2.Highly concentrated solution pump seat 14 is housed on the highly concentrated solution case 10, and solution pump is fixedly mounted on the highly concentrated solution pump seat 14 on the highly concentrated solution case 10.First spray equipment 6, second spray equipment 8 and the 3rd spray equipment 13 are ultrasonic ultrasonic delay line memory.Tower body 1 is a split-type structural, comprise tower body 1-3, middle tower body 1-4 and following tower body 1-5, there is last tower body adpting flange the lower end of last tower body 1-3, there is adpting flange on the middle tower body upper end of middle tower body 1-4, there is adpting flange under the middle tower body lower end of middle tower body 1-4, there is following tower body adpting flange the upper end of following tower body 1-5, last tower body adpting flange, adpting flange on the middle tower body, adpting flange and following tower body adpting flange all offer bolt hole under the middle tower body, adpting flange on last tower body adpting flange and the middle tower body, adpting flange is fixedlyed connected by bolt 11 respectively with following tower body adpting flange under the middle tower body, adpting flange on last tower body adpting flange and the middle tower body, the seam areas of adpting flange and following tower body adpting flange is tamped with resin-bonded mastic and is filled up under the middle tower body, so that go up tower body 1-3 and middle tower body 1-4, all can be tightly connected between middle tower body 1-4 and following tower body 1-5.
Utilize above-mentioned odor removal to carry out the method for deodorizing, has following processing step: foul smell is blasted cavity between inner core and tower body by air inlet by air blast, behind the liquor potassic permanganate generation chemical reaction of the atomizing that sprays with first spray equipment in the cavity of foul smell between inner core and tower body, enter the circulation fluid case by bubbling pipe, liquor potassic permanganate generation chemical reaction in foul smell and the circulation fluid case, then, emerge the liquor potassic permanganate of gas in the circulation fluid case, carry out chemical reaction with the liquor potassic permanganate of the atomizing of second spray equipment in tower body ejection, purified gas is discharged tower body by exhaust outlet.
Claims (7)
1. odor removal, it is characterized in that: have tower body (1), circulation fluid case (2) and circulating pump, tower body (1) is positioned at circulation fluid case (2) top, liquor potassic permanganate (4) is housed in the circulation fluid case (2), inner core (5) is arranged at tower body (1) bottom, fixedly connected with tower body (1) inner wall sealing in inner core (5) upper end, inner core (5) lower end and circulation fluid case (2) upper wall are sealedly and fixedly connected, inner core (5) bottom communicates with circulation fluid case (2), first spray equipment (6) and bubbling pipe (7) are housed in the cavity between inner core (5) and tower body (1), and insert in the liquor potassic permanganate of circulation fluid case (2) bubbling pipe (7) lower end; Be equipped with on the tower body (1) at inner core (5) position and offer air inlet (1-1), there is gas outlet (1-2) on tower body (1) top, second spray equipment (8) is housed in the tower body (1), the liquid sucting port of circulating pump submerges in the liquor potassic permanganate in the circulation fluid case (2), and the liquid outlet of circulating pump connects first spray equipment (6) and second spray equipment (8) respectively by pipeline.
2. odor removal according to claim 1 is characterized in that: in the tower body (1) of described second spray equipment (8) top demist is housed and catches drip apparatus (9).
3. odor removal according to claim 1 is characterized in that: described circulating pump is fixedly mounted on the circulation fluid case (2).
4. odor removal according to claim 1, it is characterized in that: described odor removal also has highly concentrated solution case (10) and solution pump, the liquor potassic permanganate of high concentration is housed in the highly concentrated solution case (10), the solution pump liquid sucting port submerges in the liquor potassic permanganate of high concentration, and the liquid outlet of solution pump connects circulation fluid case (2).
5. odor removal according to claim 1 is characterized in that: the 3rd spray equipment (13) is housed in the described inner core (5), and the liquid outlet of circulating pump connects the 3rd spray equipment (13) by pipeline.
6. odor removal according to claim 1 is characterized in that: described first spray equipment (6), second spray equipment (8) and the 3rd spray equipment (13) are ultrasonic ultrasonic delay line memory.
7. odor removal according to claim 1, it is characterized in that: described tower body (1) is a split-type structural, comprise tower body (1-3), middle tower body (1-4) and following tower body (1-5), all there is adpting flange the upper end of the top and bottom of the lower end of last tower body (1-3), middle tower body (1-4), following tower body (1-5), offer bolt hole on the adpting flange, last tower body (1-3), middle tower body (1-4) and following tower body (1-5) are fixedlyed connected by bolt (11) and are integral.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201837260U CN201669049U (en) | 2010-04-30 | 2010-04-30 | Deodorizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201837260U CN201669049U (en) | 2010-04-30 | 2010-04-30 | Deodorizing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201669049U true CN201669049U (en) | 2010-12-15 |
Family
ID=43326462
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201837260U Expired - Lifetime CN201669049U (en) | 2010-04-30 | 2010-04-30 | Deodorizing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201669049U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101804296A (en) * | 2010-04-30 | 2010-08-18 | 蒋超 | Deodorization device and method thereof |
| CN105344219A (en) * | 2014-08-20 | 2016-02-24 | 江苏创云环保科技有限公司 | Air purification equipment |
| CN105435606A (en) * | 2014-08-20 | 2016-03-30 | 江苏创云环保科技有限公司 | Air cleaning equipment |
| CN105617836A (en) * | 2014-11-07 | 2016-06-01 | 江苏创云环保科技有限公司 | Air purification equipment |
| CN107420927A (en) * | 2017-08-04 | 2017-12-01 | 中节能工业节能有限公司 | A kind of fire coal boiler fume high-efficient purification and UTILIZATION OF VESIDUAL HEAT IN technique |
-
2010
- 2010-04-30 CN CN2010201837260U patent/CN201669049U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101804296A (en) * | 2010-04-30 | 2010-08-18 | 蒋超 | Deodorization device and method thereof |
| CN101804296B (en) * | 2010-04-30 | 2011-11-23 | 蒋超 | Deodorization device and method thereof |
| CN105344219A (en) * | 2014-08-20 | 2016-02-24 | 江苏创云环保科技有限公司 | Air purification equipment |
| CN105435606A (en) * | 2014-08-20 | 2016-03-30 | 江苏创云环保科技有限公司 | Air cleaning equipment |
| CN105617836A (en) * | 2014-11-07 | 2016-06-01 | 江苏创云环保科技有限公司 | Air purification equipment |
| CN107420927A (en) * | 2017-08-04 | 2017-12-01 | 中节能工业节能有限公司 | A kind of fire coal boiler fume high-efficient purification and UTILIZATION OF VESIDUAL HEAT IN technique |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20101215 Effective date of abandoning: 20111123 |