CN102284231B - Scrubber tower - Google Patents
Scrubber tower Download PDFInfo
- Publication number
- CN102284231B CN102284231B CN 201110158906 CN201110158906A CN102284231B CN 102284231 B CN102284231 B CN 102284231B CN 201110158906 CN201110158906 CN 201110158906 CN 201110158906 A CN201110158906 A CN 201110158906A CN 102284231 B CN102284231 B CN 102284231B
- Authority
- CN
- China
- Prior art keywords
- chamber
- tower
- oil
- spray
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000007921 spray Substances 0.000 claims abstract description 35
- 238000000926 separation method Methods 0.000 claims abstract description 21
- 239000007788 liquid Substances 0.000 claims abstract description 5
- 238000005406 washing Methods 0.000 claims description 19
- 238000005273 aeration Methods 0.000 claims description 9
- 238000005201 scrubbing Methods 0.000 abstract description 5
- 239000000428 dust Substances 0.000 description 8
- 239000010865 sewage Substances 0.000 description 8
- 238000001816 cooling Methods 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 239000011505 plaster Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000013517 stratification Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The invention relates to a scrubber tower. The scrubber tower is characterized by comprising a vertical tower, a transverse tower, a scrubbing chamber and an oil-gas separation chamber, wherein the vertical tower is longitudinally separated into a gas inlet chamber and a spray chamber, the gas inlet chamber is communicated with the middle part of the spray chamber, and a spray head is arranged on the top of the spray chamber; the transverse tower is communicated with the bottom of the spray chamber, and spray heads are distributed on the top of the transverse tower; a pipeline communicated with the end part of the transverse tower is inserted to a position below the liquid level of the scrubbing chamber, the top of the scrubbing chamber is connected with a draught fan through a pipeline, and output of the draught fan is communicated with an air inlet on the upper part of the oil-gas separation chamber through a pipeline; an air outlet is also formed on the upper part of the oil gas separation chamber; and an oil separation baffle is arranged between the air inlet and the air outlet, and close to the side of the air inlet. According to the scrubber tower, a structure of the vertical and the transverse towers is adopted and is matched with the scrubbing chamber and the oil-gas separation chamber, so that the aim of purifying a gas source is achieved.
Description
Technical field:
The present invention relates to a kind of aeration tower that uses on the gas generator that is matched in, especially be suitable as in the exhaust harmless treatment of gas producer, waste cracking furnace and incinerator.
Background technology:
No matter aeration tower as the term suggests use in order to washing gas, is dedusting, cooling or harmless treatment, and except the cleaning solution difference, its structure is roughly the same.Main body is a perpendicular tower, and air inlet and exhaust outlet are located at the bottom and the top of perpendicular tower respectively, and perpendicular tower top is provided with spray head, and tower bottom is provided with necessary sewage draining exit.There is the dead angle in aeration tower when handling the gas of high dust now, causes the dust alluvial, especially influences the unobstructed of air inlet, and also easy accumulated slag at the bottom of the tower, is difficult for discharging from sewage draining exit, after certain work period, promptly needs scarfing cinder to handle, and makes troubles to linking operation.
Summary of the invention:
The objective of the invention is to design a kind of, and merge the aeration tower that Oil-gas Separation is arranged by the combination of perpendicular tower and horizontal tower.
Technical solution of the present invention is achieved in that a kind of aeration tower, it is characterized in that including perpendicular tower, Heng Ta, gas washing chamber and Oil-gas Separation chamber; Perpendicular tower vertically is divided into inlet plenum and spray chamber, and inlet plenum and spray chamber middle part are connected, and spray head is equipped with at the spray chamber top; Horizontal tower is connected with the spray chamber bottom, and horizontal top of tower is distributed with spray head; The pipeline that is communicated with the Heng Ta end inserts under gas washing chamber's liquid level, the gas washing chamber top connects air-introduced machine through pipeline, the output of air-introduced machine is communicated with through the air intake vent of pipeline with top, Oil-gas Separation chamber, this top, Oil-gas Separation chamber also is provided with air outlet, be provided with one fen oil baffle between air intake vent and air outlet, this minute, oil baffle was near air intake vent one side.Inlet plenum that perpendicular tower is partitioned into and spray chamber, no laying dust dead angle, and gas to enter spray chamber be to go out under enterprising, guarantee that gas in spray chamber, has the long time of staying, fully obtain washing and cooling, horizontal tower is once more to after the gas scrubbing, and the sewage that compiles can enter in the gas washing chamber along Heng Ta; Gas under the air-introduced machine effect, after gas washing chamber, send into the Oil-gas Separation chamber do last separate together after, can obtain clean source of the gas.
Described horizontal tower bottom at least is an incline structure, an end height that is communicated with spray chamber, and an end that is communicated with pipeline is low.Make the easier discharge of sewage, and have descending acceleration, can wash away the dirts such as dust of deposition.
Described spray chamber bottom is an incline structure, tilts toward horizontal tower direction.Long working also can keep clean in the tower.
The top of described gas washing chamber is provided with discharge outlet, and the bottom is provided with mud mouth.Can discharge the plaster of the precipitation of the liquid of collection and bottom in good time.
Bottom, described Oil-gas Separation chamber is provided with oil drain out for tilting at the end at the bottom lowest part, and operations such as in good time oil extraction are provided.
The present invention adopts a perpendicular horizontal Double-Tower Structure; not only overcome the interior laying dust problem of tower in the conventional art; and gas maintains the long time of staying in tower; reach abundant washing and cool effect, sewage also can be discharged at a high speed along the inclined plane, does not stay laying dust and ponding dead angle; cooperate gas washing chamber and Oil-gas Separation chamber; both but Purge gas also can not shut down and carry out necessary operations such as desilting, to the characteristics such as reutilization of the sewage that precipitate and isolate.
Description of drawings:
The present invention will be further described below in conjunction with concrete legend:
Fig. 1 waste cracking furnace structural representation
Wherein
1-erects tower 11-inlet plenum 12-spray chamber
The horizontal tower 3-of the 2-31-of gas washing chamber discharge outlet
32-mud mouth 4-Oil-gas Separation chamber 41-air intake vent
42-air outlet 43-divides oil baffle 44-oil drain out
5-spray head 6-pipeline 7-air-introduced machine
The specific embodiment:
With reference to Fig. 1, aeration tower includes perpendicular tower 1, horizontal tower 2, gas washing chamber 3 and Oil-gas Separation chamber 4; Perpendicular tower 1 vertically is divided into inlet plenum 11 and spray chamber 12, and inlet plenum 11 and spray chamber 12 middle parts are connected, so that the gas that enters can comprehensively be sprayed, and does not have pipeline dead angle, no dust stratification, and spray head 5 is equipped with at spray chamber 12 tops; Horizontal tower 2 is connected with spray chamber 12 bottoms, discharge fast in order to make ponding etc., spray chamber 12 bottoms are incline structure, tilt toward horizontal tower 2 directions, and horizontal tower 2 itself at least the bottom be incline structure, an end height that is communicated with spray chamber 12, an end that is communicated with pipeline 6 is low, high speed flowing water also can be taken away various dust stratifications rapidly, reaches non-maintaining in the tower;
Described gas washing chamber 3 is an obturator, and the pipeline of introducing from horizontal tower 26 directly inserts wherein, and keeps the mouth of pipe under liquid level; Gas washing chamber 3 tops are provided with discharge outlet 31, and the bottom is provided with mud mouth 32, so that at sewage and precipitation plaster for a long time, make the need of cleaning.The sewage that discharge outlet 31 is discharged can flow to the miscellaneous equipment of biomass garbage incinerator or pyrolysis furnace, and such as the slag cooling, perhaps slag absorption etc. reaches recycling, avoids producing secondary pollution.
The top of gas washing chamber 3 connects air-introduced machine 7 through pipeline 6, the output of air-introduced machine 7 is communicated with through the air intake vent 41 of pipeline 6 with 4 tops, Oil-gas Separation chamber, these 4 tops, Oil-gas Separation chamber also are provided with air outlet 42, between air intake vent 41 and air outlet 42, be provided with one fen oil baffle 43, this minute, oil baffle 43 was near air intake vent 41 1 sides, the high-speed gas that is entrained with oil gas impacts when dividing oil baffle 43, fine particle such as oil gas and aqueous vapor can be divided oil baffle 43 to adsorb, drip after constantly gathering, and 4 bottoms, Oil-gas Separation chamber are for tilting the end, be provided with oil drain out 44 at the bottom lowest part, utilize it can discharge the surplus oil of collection in good time.
Claims (2)
1. an aeration tower is characterized in that including perpendicular tower, Heng Ta, gas washing chamber and Oil-gas Separation chamber; Perpendicular tower vertically is divided into inlet plenum and spray chamber, and inlet plenum and spray chamber middle part are connected, and spray head is equipped with at the spray chamber top; Horizontal tower is connected with the spray chamber bottom, and horizontal top of tower is distributed with spray head; The pipeline that is communicated with the Heng Ta end inserts under gas washing chamber's liquid level, the gas washing chamber top connects air-introduced machine through pipeline, the output of air-introduced machine is communicated with through the air intake vent of pipeline with top, Oil-gas Separation chamber, this top, Oil-gas Separation chamber also is provided with air outlet, be provided with one fen oil baffle between air intake vent and air outlet, this minute, oil baffle was near air intake vent one side; Described horizontal tower bottom at least is an incline structure, an end height that is communicated with spray chamber, and an end that is communicated with pipeline is low; Described spray chamber bottom is an incline structure, tilts toward horizontal tower direction; Bottom, described Oil-gas Separation chamber is the inclination end, and lowest part is provided with oil drain out in the bottom.
2. a kind of aeration tower according to claim 1 is characterized in that the top of gas washing chamber is provided with discharge outlet, and the bottom is provided with mud mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110158906 CN102284231B (en) | 2011-06-14 | 2011-06-14 | Scrubber tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110158906 CN102284231B (en) | 2011-06-14 | 2011-06-14 | Scrubber tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102284231A CN102284231A (en) | 2011-12-21 |
| CN102284231B true CN102284231B (en) | 2013-07-31 |
Family
ID=45331147
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201110158906 Expired - Fee Related CN102284231B (en) | 2011-06-14 | 2011-06-14 | Scrubber tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102284231B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105268299A (en) * | 2015-11-18 | 2016-01-27 | 华文蔚 | Device for treating waste gas of incinerator |
| CN105289259A (en) * | 2015-11-18 | 2016-02-03 | 华文蔚 | Incinerator exhaust-gas treatment device |
| CN108148636A (en) * | 2018-02-05 | 2018-06-12 | 陕西冶金设计研究院有限公司 | A kind of raw coke oven gas pneumatic trough |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE789914A (en) * | 1971-10-12 | 1973-02-01 | Steag Ag | SMOKE GAS PURIFICATION DEVICE |
| CN201676627U (en) * | 2010-04-23 | 2010-12-22 | 河南海星化工科技有限公司 | Oil gas absorption tower |
| CN201695008U (en) * | 2010-05-27 | 2011-01-05 | 山西阳煤丰喜肥业(集团)有限责任公司 | Scrubber tower |
| CN202113745U (en) * | 2011-06-14 | 2012-01-18 | 福州市英袖能源科技有限公司 | Scrubber tower |
-
2011
- 2011-06-14 CN CN 201110158906 patent/CN102284231B/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN102284231A (en) | 2011-12-21 |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: FUJIAN YINGXIU ENERGY TECHNOLOGY CO., LTD. Free format text: FORMER NAME: FUZHOU YINGXIU ENERGY TECHNOLOGY CO., LTD. |
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| CP01 | Change in the name or title of a patent holder |
Address after: Riverside East Road in Fuzhou city of Fujian province 350015 No. 108 Fujian Province students Pioneering Park 518 Patentee after: Fujian Li Li Energy Technology Co.,Ltd. Address before: Riverside East Road in Fuzhou city of Fujian province 350015 No. 108 Fujian Province students Pioneering Park 518 Patentee before: Fuzhou Yingxiu Energy Technology Co.,Ltd. |
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| ASS | Succession or assignment of patent right |
Owner name: FUJIAN BOYI ENVIRONMENTAL PROTECTION TECHNOLOGY CO Free format text: FORMER OWNER: FUJIAN YINGXIU ENERGY TECHNOLOGY CO., LTD. Effective date: 20140918 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 350015 FUZHOU, FUJIAN PROVINCE TO: 350003 FUZHOU, FUJIAN PROVINCE |
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| TR01 | Transfer of patent right |
Effective date of registration: 20140918 Address after: 350003, A, 5 floor, International Building, No. 54, Gulou District, Fujian, Fuzhou Patentee after: Fujian BoYi Environmental Protection Technology Co.,Ltd. Address before: Riverside East Road in Fuzhou city of Fujian province 350015 No. 108 Fujian Province students Pioneering Park 518 Patentee before: Fujian Li Li Energy Technology Co.,Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130731 |