CN201676627U - Oil gas absorption tower - Google Patents
Oil gas absorption tower Download PDFInfo
- Publication number
- CN201676627U CN201676627U CN2010201683135U CN201020168313U CN201676627U CN 201676627 U CN201676627 U CN 201676627U CN 2010201683135 U CN2010201683135 U CN 2010201683135U CN 201020168313 U CN201020168313 U CN 201020168313U CN 201676627 U CN201676627 U CN 201676627U
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- CN
- China
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- oil
- gas
- tower body
- absorption tower
- sieve
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- 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
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- Filtering Of Dispersed Particles In Gases (AREA)
- Treating Waste Gases (AREA)
Abstract
An oil gas absorption tower relates to an absorption tower, which is characterized in that the lower part of the tower body is provided with an air inlet and an oil outlet, the upper part of the tower body is provided with an absorber oil inlet, the top of the tower body is provided with a wire gauze filter and a gas outlet, and the tower body between the gas outlet and the absorber oil inlet is provided with sieve plates in a horizontally cross way; and the sieve plate is provided with sieve pores. The utility model has the beneficial effects that through the multiple cross impacts of the absorber oil with the oil gas and nitrogen on the sieve plates arranged in a horizontally cross way, the oil and gas in volatilized gas can be separated, the recovery rate of solvent is improved, the operation is simple and practical, and the gas is collected after being exhausted, which is environment friendly and has no pollution.
Description
Technical field
The utility model relates to a kind of absorption tower, specifically a kind of oil gas absorption tower.
Background technology
In coal-based needle coke pretreatment of raw material operation, when mixed solvent and pitch mixing, sedimentation operation, the volatilization of solvent causes solvent loss serious, simultaneously also can bring pollution to environment, do not meet environmental requirement, if use a kind of equipment oil gas to be washed, separates aborning, so not only can improve the mixed solvent rate of recovery, but also can reach the purpose of environmental protection with washing oil.
The utility model content
The utility model purpose is for the better mixed solvent rate of recovery that improves, and by with washing oil oil gas being washed and separating, reaches the purpose of environmental protection simultaneously, thereby a kind of practical easy-operating oil gas of coal-based needle coke production and processing absorption tower that is used for is provided.
The utility model is to solve the problems of the technologies described above the technical scheme that is adopted to be: a kind of oil gas absorption tower, be provided with air inlet and oil-out in the tower body bottom, tower body top is provided with the washing oil inlet, the top of tower body is provided with wire gauzee filter and gas discharge outlet, and level is staggeredly equipped with sieve plate in the tower body between air inlet and the washing oil inlet.
The utility model, described sieve plate is provided with sieve aperture.
The beneficial effects of the utility model are: by washing oil and oil gas and nitrogen in sieve plate place crossing collision repeatedly that level is crisscross arranged, thereby the Oil-gas Separation with in the Volatile Gas has improved solvent recovering rate, practicality simple to operate, gas is collected after discharging, and is environment friendly and pollution-free.
Description of drawings
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the structural representation of sieve plate in the utility model;
Mark is among the figure: 1, tower body, 2, air inlet, 3, oil-out, 4, the washing oil inlet, 5, sieve plate, 6, wire gauzee filter, 7, gas discharge outlet, 8, sieve aperture.
The specific embodiment
As depicted in figs. 1 and 2, a kind of oil gas absorption tower, by tower body 1, air inlet 2, oil-out 3, washing oil inlet 4, sieve plate 5, wire gauzee filter 6 and gas discharge outlet 7 are formed, tower body 1 is an airtight container, tower body 1 bottom left end is provided with air inlet 2, tower body 1 bottom right-hand member is provided with oil-out 3, tower body 1 top is provided with washing oil inlet 4, level is staggeredly equipped with five rectangular-shaped sieve plates 5 in the tower body 1 between air inlet 2 and the washing oil inlet 4, sieve plate 5 tops are provided with wire gauzee filter 6 and wire gauzee filter 6 and also are positioned at washing oil 4 tops that enter the mouth, the top of tower body 1 also is provided with gas discharge outlet 7, and sieve plate 5 is provided with sieve aperture 8.
Air inlet 2 in the utility model is to be used for oil-feed gas and nitrogen, and described wire gauzee filter 6 can adopt a kind of wire mesh demister, and gas can be removed the mist of carrying secretly in the gas by behind the wire mesh demister.Washing oil enters into tower body 1 by washing oil inlet 4, meanwhile oil gas and nitrogen also enter into tower body 1 by air inlet 2, washing oil flows to oil-out 3 along sieve plate 5 or by sieve aperture 8, nitrogen and oil gas then rise to gas discharge outlet 7 directions along sieve plate 5 or by sieve aperture 8, crossing the melting that washing oil and oil gas and nitrogen process sieve plate are more than 5 time, with oily gentle washing the in the Volatile Gas, separate, washing, isolated gas then rises with oil gas and nitrogen, through can further removing oil remaining in nitrogen and the oil gas after wire gauzee filter 6 filtrations, nitrogen after the filtration and oil gas are discharged by gas discharge outlet 7 and are collected; Oil after the separation is then discharged by oil-out 3 and is collected.
The utility model mainly be by washing oil and oil gas and nitrogen at sieve plate place that level is crisscross arranged repeatedly crossing collision, wash and separate, thereby the Oil-gas Separation with in the Volatile Gas has improved solvent recovering rate, practicality simple to operate, gas is collected after discharging, and is environment friendly and pollution-free.
Claims (2)
1. oil gas absorption tower, it is characterized in that: be provided with air inlet (2) and oil-out (3) in tower body (1) bottom, tower body (1) top is provided with washing oil inlet (4), the top of tower body (1) is provided with wire gauzee filter (6) and gas discharge outlet (7), and the interior level of tower body (1) between air inlet (2) and the washing oil inlet (4) is staggeredly equipped with sieve plate (5).
2. a kind of oil gas according to claim 1 absorption tower is characterized in that: described sieve plate (5) is provided with sieve aperture (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201683135U CN201676627U (en) | 2010-04-23 | 2010-04-23 | Oil gas absorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201683135U CN201676627U (en) | 2010-04-23 | 2010-04-23 | Oil gas absorption tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201676627U true CN201676627U (en) | 2010-12-22 |
Family
ID=43341691
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201683135U Expired - Fee Related CN201676627U (en) | 2010-04-23 | 2010-04-23 | Oil gas absorption tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201676627U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102284231A (en) * | 2011-06-14 | 2011-12-21 | 福州市英袖能源科技有限公司 | Scrubber tower |
| CN102371106A (en) * | 2011-06-10 | 2012-03-14 | 景东力奥林产集团林业化工有限公司 | Rosin resin tail gas treating tank and method |
| CN102614744A (en) * | 2011-01-27 | 2012-08-01 | 宜兴协联生物化学有限公司 | Water spray absorber |
| CN104474840A (en) * | 2014-11-18 | 2015-04-01 | 肇庆宏旺金属实业有限公司 | Oil-gas separation device |
| CN106310884A (en) * | 2016-08-21 | 2017-01-11 | 江苏恒新能源科技有限公司 | Labyrinth type mixed absorbing tower |
| CN109550376A (en) * | 2017-09-26 | 2019-04-02 | 萍乡市普天高科实业有限公司 | A kind of equipment and its technique for flue gas desulfurization and denitrification |
-
2010
- 2010-04-23 CN CN2010201683135U patent/CN201676627U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102614744A (en) * | 2011-01-27 | 2012-08-01 | 宜兴协联生物化学有限公司 | Water spray absorber |
| CN102371106A (en) * | 2011-06-10 | 2012-03-14 | 景东力奥林产集团林业化工有限公司 | Rosin resin tail gas treating tank and method |
| CN102284231A (en) * | 2011-06-14 | 2011-12-21 | 福州市英袖能源科技有限公司 | Scrubber tower |
| CN104474840A (en) * | 2014-11-18 | 2015-04-01 | 肇庆宏旺金属实业有限公司 | Oil-gas separation device |
| CN106310884A (en) * | 2016-08-21 | 2017-01-11 | 江苏恒新能源科技有限公司 | Labyrinth type mixed absorbing tower |
| CN109550376A (en) * | 2017-09-26 | 2019-04-02 | 萍乡市普天高科实业有限公司 | A kind of equipment and its technique for flue gas desulfurization and denitrification |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101222 Termination date: 20150423 |
|
| EXPY | Termination of patent right or utility model |