CN2659531Y - Gas washing tower - Google Patents
Gas washing tower Download PDFInfo
- Publication number
- CN2659531Y CN2659531Y CN 200320109792 CN200320109792U CN2659531Y CN 2659531 Y CN2659531 Y CN 2659531Y CN 200320109792 CN200320109792 CN 200320109792 CN 200320109792 U CN200320109792 U CN 200320109792U CN 2659531 Y CN2659531 Y CN 2659531Y
- Authority
- CN
- China
- Prior art keywords
- gas
- cylinder
- liquid
- traverse baffle
- storage tank
- 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 - Lifetime
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Abstract
The utility model discloses a gas washer which includes a cylinder. A vent port of gas is arranged at the bottom of the cylinder, an inlet of scrub solution is arranged on one side of the upper part of the cylinder, a traverse baffle is arranged in the upper part of the cylinder, a mixture inlet of gas, liquid and solid is arranged on one side which is a little upward on the lower part of the cylinder, a liquid eliminating and foam destroying element is arranged above the traverse baffle in the upper part of the cylinder, a cyclone gas board is arranged below the traverse baffle in the lower part of the cylinder, a tapering storage tank is arranged below the cyclone gas board in the bottom of the cylinder, and a liquor outlet and a solid outlet are arranged at the bottom of the tapering storage tank. The utility model has the advantages of reasonable structure, simple operation and low investment, and can avoid the problem of gas containing water or dust efficiently.
Description
Technical field
The utility model relates to a kind of separating device of gas, liquid, solid three-phase mixture, particularly relates to a kind of gas scrubber of air flow bed reactor made valuable gases that is.
Background technology
The various vapourizing furnaces of commercialized running are used to produce synthetic raw gas, reducing gas and fuel gas.The gas of preparation is discharged by vapourizing furnace, because gasified raw material (as coal, oil or other carbon containing thing) contains the incomplete conversion of various impurity (as the ash of raw material) and carbon wherein, causes the various impurity of gas-entrained that generate.Usually adopt Quench+washing process cooling and Purge gas, because still keeping 150～280 ℃, pressure, temperature remains on 0.6～9.0MPa through the gas of Quench, the flow velocity of gas in system is higher, often cause carrying secretly in the gas a large amount of liquid and solid, the necessary Ex-all of liquid wherein and solid, otherwise the gas of vapourizing furnace preparation is difficult to use.The treatment unit and the technology of the gas of Chinese patent 98807310.2 reports, system configuration have washing tower, water cooler, gas-liquid separator and a various necessary transferpump of traverse baffle, complex process, equipment is many, the device of this technology is used in domestic introduction, the gas that enters the postorder system also often have band water band ash phenomenon take place, influence the normal operation of total system device.
The utility model content
The purpose of this utility model is at above-mentioned the deficiencies in the prior art, and a kind of rational in infrastructure, simple to operate, gas scrubbing water cooler that washing effect is good is provided.
For achieving the above object, the technical scheme that the utility model adopted is: this gas scrubber comprises cylindrical shell 10, its top is provided with pneumatic outlet 1, its top one side is provided with washings import 2,3,4, be provided with traverse baffle 8 in its top, its underpart side on the upper side is provided with gas, liquid, solid mixture import 7, the top that is positioned at traverse baffle 8 in described cylindrical shell 10 tops is provided with except that liquid foam removal member 9, the below that is positioned at traverse baffle 8 in its underpart is provided with gas cyclone plate 5, the below that is positioned at gas cyclone plate 5 in its bottom is provided with taper storage tank 11, and the bottom of taper storage tank 11 is provided with liquid and solid outlet 6.
Described cylindrical shell 10 is cylindrical.
The described liquid foam removal member 9 that removes is made up of two-layer at least Stainless Steel Cloth.
The grid specification of described Stainless Steel Cloth is 2mm * 2mm～10mm * 10mm.
The utility model compared with prior art has the following advantages: the utility model is rational in infrastructure, simple to operate, less investment, can prevent the band water band ash problem of gas effectively.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Embodiment
Below in conjunction with accompanying drawing the utility model is described further.
Gas scrubber as shown in Figure 1, profile is a cylindrical tube 10, the top of described cylindrical tube 10 is provided with pneumatic outlet 1, its top one side is provided with washings import 2,3,4, washings import 2 is the import of final ablution, the optional comparatively hot water of cleaning of final ablution with design library part editor and reuse system by-product, the buck that the hot water that the washing water of import 3 can adopt the grey water treatment system circulation, the washing water of import 4 can adopt the gasification washing system to produce; Be provided with traverse baffle 8 in the top of described cylindrical tube 10, the top that is positioned at traverse baffle 8 in its top is provided with except that liquid foam removal member 9, the below that is positioned at traverse baffle 8 in its underpart is provided with gas cyclone plate 5, gas cyclone plate 5 and traverse baffle 8 can change air flow line, increase the duration of contact of gas and washing water, improve washing effect; Described cylindrical tube 10 a bottoms side on the upper side is provided with gas, liquid, solid mixture intake 7, and the below that is positioned at gas cyclone plate 5 in its bottom is provided with taper storage tank 11, and the bottom of taper storage tank 11 is provided with liquid and solid outlet 6.
During work, pending gas, liquid, Gu three-phase mixture enters the utility model gas scrubber from import 7, the solid and the liquid of gas entrainment some amount wherein, the said mixture that enters gas scrubber is delivered to through a bend pipe below the liquid level of taper storage tank 11 of gas scrubber bottom, wherein being formed bubbling by the gas of the preliminary washing of the liquid of 11 li of taper storage tanks overflows, flow to the top of gas scrubber, through gas cyclone plate 5, the flow direction of traverse baffle 8 changes, gas prolonged in the residence time of gas scrubber, add the washing of the liquid that flows downward, most of solid of gas entrainment and liquid are washed water at this and take taper storage tank 11 to, the air-flow that rises removes the liquid foam removal through what remove liquid foam removal member 9, the clean gas that does not contain the liquid foam leaves gas scrubber by gas scrubber top exit 1 and enters subsequent processing, liquid wherein and solid come together in taper storage tank 11, and liquid and solid outlet 6 through taper storage tank 11 bottoms leave gas scrubber.
Claims (4)
1, a kind of gas scrubber, it comprises cylindrical shell (10), its top is provided with pneumatic outlet (1), its top one side is provided with washings import (2,3,4), be provided with traverse baffle (8) in its top, its underpart side on the upper side is provided with gas, liquid, solid mixture import (7), it is characterized in that: the top that is positioned at traverse baffle (8) in described cylindrical shell (10) top is provided with except that liquid foam removal member (9), the below that is positioned at traverse baffle (8) in its underpart is provided with gas cyclone plate (5), the below that is positioned at gas cyclone plate (5) in its bottom is provided with taper storage tank (11), and the bottom of taper storage tank (11) is provided with liquid and solid outlet (6).
2, gas scrubber according to claim 1 is characterized in that: described cylindrical shell (10) is for cylindrical.
3, according to claim 1,2 described gas scrubbers, it is characterized in that: the described liquid foam removal member (9) that removes is made up of two-layer at least Stainless Steel Cloth.
4, gas scrubber according to claim 3 is characterized in that: the grid specification of described Stainless Steel Cloth is 2mm * 2mm～10mm * 10mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200320109792 CN2659531Y (en) | 2003-11-20 | 2003-11-20 | Gas washing tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200320109792 CN2659531Y (en) | 2003-11-20 | 2003-11-20 | Gas washing tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2659531Y true CN2659531Y (en) | 2004-12-01 |
Family
ID=34343400
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200320109792 Expired - Lifetime CN2659531Y (en) | 2003-11-20 | 2003-11-20 | Gas washing tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2659531Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102491398A (en) * | 2011-12-20 | 2012-06-13 | 广西华纳新材料科技有限公司 | Gas stripping precipitated calcium carbonate carbonation reactor |
| CN104388703A (en) * | 2014-11-11 | 2015-03-04 | 宁夏嘉翔自控技术有限公司 | Cyclone dust-removal plate of reducing slag collection tank used in integrated metal magnesium smelting, high-pressure slag-skimming and charging machine |
| CN104388706A (en) * | 2014-11-11 | 2015-03-04 | 宁夏嘉翔自控技术有限公司 | Reducing slag collecting box for metallic magnesium smelting and high-pressure slag skimming charging system |
| CN105498518A (en) * | 2015-11-29 | 2016-04-20 | 大连碧蓝节能环保科技有限公司 | Solid-liquid two-phase gas washing tower |
-
2003
- 2003-11-20 CN CN 200320109792 patent/CN2659531Y/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102491398A (en) * | 2011-12-20 | 2012-06-13 | 广西华纳新材料科技有限公司 | Gas stripping precipitated calcium carbonate carbonation reactor |
| CN104388703A (en) * | 2014-11-11 | 2015-03-04 | 宁夏嘉翔自控技术有限公司 | Cyclone dust-removal plate of reducing slag collection tank used in integrated metal magnesium smelting, high-pressure slag-skimming and charging machine |
| CN104388706A (en) * | 2014-11-11 | 2015-03-04 | 宁夏嘉翔自控技术有限公司 | Reducing slag collecting box for metallic magnesium smelting and high-pressure slag skimming charging system |
| CN105498518A (en) * | 2015-11-29 | 2016-04-20 | 大连碧蓝节能环保科技有限公司 | Solid-liquid two-phase gas washing tower |
| CN105498518B (en) * | 2015-11-29 | 2017-08-01 | 大连碧蓝节能环保科技有限公司 | A kind of solid-liquid two-phase gas scrubbing tower |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: XI AN YUANCHUANG CHEMICAL INDUSTRY TECHNOLOGY CO., Free format text: FORMER OWNER: XIBEI RESEARCH INST. OF CHEMICAL ENGINEERING Effective date: 20130729 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 710600 XI AN, SHAANXI PROVINCE TO: 710061 XI AN, SHAANXI PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130729 Address after: 710061, west two floor, Qujiang campus, Xi'an Jiao Tong University, Yanta Road, 99, Yanta District, Shaanxi, Xi'an Patentee after: Xi'an Origin Chemical Technologies Co., Ltd. Address before: 710600 No. 1 Railway Station Street, Lintong District, Shaanxi, Xi'an Patentee before: The Northwest Research Institute of Chemical Industry |
|
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20131120 Granted publication date: 20041201 |