CN201261775Y - Coal gas washing purification apparatus - Google Patents
Coal gas washing purification apparatus Download PDFInfo
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- CN201261775Y CN201261775Y CN 200820029293 CN200820029293U CN201261775Y CN 201261775 Y CN201261775 Y CN 201261775Y CN 200820029293 CN200820029293 CN 200820029293 CN 200820029293 U CN200820029293 U CN 200820029293U CN 201261775 Y CN201261775 Y CN 201261775Y
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- separator
- washing tower
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Abstract
The utility model discloses a coal gas washing and purifying device, which comprises a Venturi scrubber, a separator and a scrubbing tower. The processes of wetting, cementing and amplifying can be performed on solid particles, such as clinkers entrained in raw gas in the Venturi scrubber, the air enters into the separator, and the first grade purification is performed in the separator; after the liquid water and the clinkers are removed preliminarily, the air enters into the washing tower, and a second grade purification is performed. Therefore, the ash content of the coal gas at the outlet is less than 1 mg/m <3>, the vapors on the coal gas are saturated, and an appropriate gas-steam ratio is reached, thereby creating favorable service conditions for downstream process, such as the production of methanol and synthetic ammonia. Black water discharged from the separator and the bottom part of the washing tower is merged into a black water treatment system for being treated and recovered.
Description
Technical field
The utility model relates to a kind of coal gas washing purification apparatus, particularly a kind of coal gas washing purification apparatus that is suitable for chilling technology.
Background technology
Coal Gasification Technology is the key of clean coal technology as the frontier technology of coal deep processing, conversion, is " tap " technology, and Application Areas is very extensive.Up to now, the applied main flow Coal Gasification Technology of extensive gasification production still is the air-flow bed coal-gasification technology.The Coal Chemical Industry industry of China is in the flourish stage at present, have powerful market outlook, units such as Xi'an Thermal Power Research Institute Co., Ltd., Xibei Chemical Inst and East China University of Science have all developed the air-flow bed coal-gasification technology with independent intellectual property right.
In the air-flow bed coal-gasification technology, the technology after the gasification has two kinds of useless pot technology and chilling technologies usually.Useless pot technology is made up of equipment such as one or more levels waste heat boiler and nonaqueous dust cleaners, and it is that latent heat by one or more levels waste heat boiler absorption raw gas produces high and medium voltage steam, only includes a spot of water vapour in the gas phase.Chilling technology then is made up of Quench and washing, purifying equipment etc., and the heat of high temperature rough gas is absorbed by water vapor, includes a large amount of water vapour in the gas phase, can satisfy the needs of conversion process in the productions such as coal hydrogen manufacturing, coal system methyl alcohol and synthetic ammonia.
Coal gas washing purification apparatus and technology that present Coal Chemical Industry industry chilling process is adopted, be that the raw gas after the Quench is sent into Venturi scrubber, carry out the solid particulates of carrying secretly in the raw gas such as lime-ash wetting, bonding and increase, directly sending into washing tower then washs, the said apparatus that perhaps adopts the secondary Venturi scrubber to join washing tower carries out gas washing and purifies, and the Heisui River after the washing drains into the usage on black water system and handles and reclaim.This coal gas washing purification apparatus and technology, not only facility investment is big, and washing effect is not good, is easy to generate situations such as dust stratification, obstruction in washing tower, influences the steady running of full factory.
Coal gas washing purification apparatus described in the utility model and technology, be that the raw gas after the Quench is introduced Venturi scrubber, in Venturi scrubber, carry out the solid particulates of carrying secretly in the raw gas such as lime-ash wetting, bonding and increase, and then send into and carry out first class purification in the separator, tentatively remove liquid water and lime-ash in the raw gas, and then enter washing tower and carry out secondary purification, the ash content that makes outlet coal gas is less than 1mg/m
3, coal gas is vapo(u)rous, reaches suitable steam-to-gas ratio.This coal gas washing purification apparatus and technology, be that lime-ash in the raw gas and water vapour are tentatively washed by separator, and then carry out the secondary fine purifiation by washing tower, doing so not only can water saving, effectively improve the efficient and the effect of raw gas washing, and can alleviate the load of every washing, purifying equipment, thereby reduce size, volume and the investment of washing, purifying equipment.Aspect system loss, because the washing water recycle pump that adopts can recycle washing water, reduced the consumption of washing water, alleviated the burden of follow-up usage on black water operation.Washing tower of the present utility model can be adjusted the steam-to-gas ratio that purifies back coal gas, makes the needs that satisfy conversion process in the productions such as coal hydrogen manufacturing, coal system methyl alcohol and synthetic ammonia through the steam-to-gas ratio of coal gas behind the secondary purification.
Process system of the present utility model is simple in structure, and is cheap, and the efficiency of dust collection height is Coal Chemical Industry (synthetic ammonia, methyl alcohol, system H
2, synthetic oil) optimal selection of industry.
Summary of the invention
The purpose of this utility model is to provide the coal gas washing purification apparatus that a kind of process system is simple in structure, efficiency of dust collection is high, equipment manufacturing cost is low and can economize on water.
For achieving the above object, coal gas washing purification apparatus of the present utility model, comprise the inlet mouth Venturi scrubber that is connected with raw gas, the air outlet of Venturi scrubber is connected with the inlet mouth of separator, the air outlet of separator is connected with the inlet mouth of washing tower, be provided with Heisui River control valve D2 and D3 in the lower end of separator, the top of washing tower is provided with the make up water import, the lower end of washing tower is provided with Heisui River control valve D5, the bottom of washing tower also is connected with the washing water recycle pump, and the washing water recycle pump is connected with the water-in of Venturi scrubber by variable valve D1 respectively, be connected with the water-in of washing tower by variable valve D4.
Separator of the present utility model inside is provided with the eddy flow plate; The inside of washing tower is provided with traverse baffle scum dredger, some grades of tower trays and Heisui River storage tank from top to bottom.
The utility model the washing water recycle pump will be squeezed in the Venturi scrubber from a part of Heisui River that washing tower Heisui River storage tank comes mix with raw gas, wetting, enter separator then and carry out the one-level washing, enter washing tower again, in washing tower, will carry out the counter current contact washing with a part of Heisui River of coming from washing tower Heisui River storage tank after the washing water recycle pump boosts with by the technology moisturizing that the make up water inlet adds, will send into the downstream through the coal gas after washing tower carries out the secondary washing, purifying then through the coal gas after the one-level washing.
The technology that the Venturi scrubber that the utility model adopted, separator and washing tower gas washing purify, system architecture is simple, efficiency of dust collection is high, equipment manufacturing cost is low and can economize on water, and the gas exit ash content is less than 1mg/m
3, coal gas is vapo(u)rous, reaches suitable steam-to-gas ratio and can directly send into transformation system and enter the downstream transforms operation and do not need to add again steam, and be the optimal selection of Coal Chemical Industry (synthetic ammonia, methyl alcohol, system H2, synthetic oil) industry.
Description of drawings
Fig. 1 is a gas washing purification process one-piece construction synoptic diagram of the present utility model;
Fig. 2 is the structural representation of separator of the present utility model (2);
Fig. 3 is the structural representation of washing tower of the present utility model (3).
Embodiment:
Below in conjunction with Fig. 1, Fig. 2 and Fig. 3 the utility model is described in further detail.
Referring to Fig. 1, coal gas washing purification apparatus of the present utility model comprises the Venturi scrubber 1 that inlet mouth is connected with raw gas, the air outlet of Venturi scrubber 1 is connected with the inlet mouth of separator 2, the air outlet of separator 2 is connected with the inlet mouth of washing tower 3, be provided with eddy flow plate 5 in separator inside, be provided with Heisui River control valve D2 and D3 in the lower end of separator 2, the top of washing tower 3 is provided with make up water import 9, the lower end of washing tower 3 is provided with Heisui River control valve D5, the bottom of washing tower 3 is connected with washing water recycle pump 4, and washing water recycle pump 4 is connected with the water-in of Venturi scrubber 1 by variable valve D1 respectively, be connected with the water-in of washing tower 3 by variable valve D4.In washing tower, also be provided with traverse baffle scum dredger 6, some grades of tower trays 7 and Heisui River storage tank 8.
Implementation step of the present utility model:
Washing water recycle pump 4 will be squeezed into from a part of Heisui River of washing tower Heisui River storage tank 8 in the Venturi scrubber 1 and mix from out-of-bounds raw gas, the solid particulates of carrying secretly in raw gas in Venturi scrubber 1 such as lime-ash carry out wetting, bonding and increase, and enter separator 2 by separator gas inlet 12 then; Raw gas enters downtake 10 via separator gas inlet 12 in separator 2, most of lime-ash in the raw gas etc. enters liquid phase and flows downward, raw gas upwards flows, annular space between downtake 10 and airway rises and enters upcast 11, further dewater and dedusting through eddy flow plate 5 again, coal gas after the one-level washing is sent washing tower 3 by separator gas exit 13, and the Heisui River that separator 2 produces enters the usage on black water system through separator Heisui River outlet 14; The coal gas after one-level washing of going out from separator 2 separator gas exits 13, the water-bath that washing tower gas inlet 15 by washing tower 3 enters washing tower 3 bottoms makes progress and flows, in the some grades of tower trays 7 that washing tower 3 tops are provided with send into from washing tower 3 Heisui River internal recycle imports 17 from a part of Heisui River of washing water recycle pump 4 and the technology moisturizings that add by make up water inlet 9, counter current contact is carried out washing, purifying, upwards remove mist in the coal gas then by the traverse baffle scum dredger 6 on washing tower 3 tops, send into the subsequent conversion operation through the coal gas behind the washing tower 3 secondary washing, purifyings by the washing tower gas exit 18 of washing tower 3, the Heisui River that washing tower 3 produces enters the usage on black water system by washing tower Heisui River outlet 19.
The Heisui River that washing tower 3 produces is divided into the Heisui River control valve D5 control of three tunnel: one route washing tower, 3 lower ends setting and sends into out-of-bounds usage on black water system; The bottom of washing tower 3 is connected with washing water recycle pump 4, two-way Heisui River is the Heisui River of sending into Venturi scrubber 1 through washing water recycle pump 4 respectively by variable valve D1 control in addition, is come out to enter then the Heisui River of washing tower 3 Heisui River internal recycle inlets 17 by washing tower 3 Heisui River internal recycle outlets 16 by variable valve D4 control.
The Venturi scrubber that the utility model proposes, separator and washing tower coal gas washing purification apparatus and technology, the gas exit ash content behind this technology washing, purifying is less than 1mg/m
3, coal gas is vapo(u)rous, reaches suitable steam-to-gas ratio, can directly send into transformation system and does not need to add steam again.That this process system has is simple in structure, efficiency of dust collection is high, equipment manufacturing cost is low and advantage such as water saving, is Coal Chemical Industry (synthetic ammonia, methyl alcohol, system H
2, synthetic oil) optimal selection of industry.
Claims (3)
1, a kind of coal gas washing purification apparatus, comprise the inlet mouth Venturi scrubber (1) that is connected with raw gas, it is characterized in that: the air outlet of Venturi scrubber (1) is connected with the inlet mouth of separator (2), the air outlet of separator (2) is connected with the inlet mouth of washing tower (3), be provided with Heisui River control valve D2 and D3 in the lower end of separator (2), the top of washing tower (3) is provided with make up water import (9), the lower end of washing tower (3) is provided with Heisui River control valve D5, the bottom of washing tower (3) also is connected with washing water recycle pump (4), and washing water recycle pump (4) is connected with the water-in of Venturi scrubber (1) by variable valve D1 respectively, be connected with the water-in of washing tower (3) by variable valve D4.
2, coal gas washing purification apparatus according to claim 1 is characterized in that: said separator (2) inside is provided with eddy flow plate (5).
3, coal gas washing purification apparatus according to claim 1 is characterized in that: the inside of said washing tower (3) is provided with traverse baffle scum dredger (6), some grades of tower trays (7) and Heisui River storage tank (8) from top to bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200820029293 CN201261775Y (en) | 2008-06-06 | 2008-06-06 | Coal gas washing purification apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200820029293 CN201261775Y (en) | 2008-06-06 | 2008-06-06 | Coal gas washing purification apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201261775Y true CN201261775Y (en) | 2009-06-24 |
Family
ID=40808247
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200820029293 Expired - Fee Related CN201261775Y (en) | 2008-06-06 | 2008-06-06 | Coal gas washing purification apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201261775Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101302446B (en) * | 2008-06-06 | 2011-04-06 | 西安热工研究院有限公司 | Coal gas washing purification apparatus and process |
| CN108383139A (en) * | 2018-04-20 | 2018-08-10 | 包头市远达鑫化工有限公司 | The process units and method of ammonium hydrogen carbonate |
-
2008
- 2008-06-06 CN CN 200820029293 patent/CN201261775Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101302446B (en) * | 2008-06-06 | 2011-04-06 | 西安热工研究院有限公司 | Coal gas washing purification apparatus and process |
| CN108383139A (en) * | 2018-04-20 | 2018-08-10 | 包头市远达鑫化工有限公司 | The process units and method of ammonium hydrogen carbonate |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090624 Termination date: 20130606 |