CN202427265U - Novel oil and steam separator - Google Patents
Novel oil and steam separator Download PDFInfo
- Publication number
- CN202427265U CN202427265U CN2011205695456U CN201120569545U CN202427265U CN 202427265 U CN202427265 U CN 202427265U CN 2011205695456 U CN2011205695456 U CN 2011205695456U CN 201120569545 U CN201120569545 U CN 201120569545U CN 202427265 U CN202427265 U CN 202427265U
- Authority
- CN
- China
- Prior art keywords
- baffle plate
- tank body
- baffle
- tail gas
- oil
- 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
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Abstract
The utility model discloses a novel oil and steam separator, and belongs to the field of oil refining. The shortcoming that the treatment efficiency of tail gas generated in an oil refining process is low in the prior art is overcome. According to the technical scheme, the novel oil and steam separator comprises a tank body, a steam outlet, a steam inlet and a liquid outlet are formed on the tank body, a first baffle plate and a second baffle plate are arranged in the tank body, the first baffle plate is fixedly connected onto the inner wall of the tank body, a steam outlet opening A is formed between the first baffle plate and the inner wall of the tank body, the second baffle plate is an arc body, the periphery of the arc body is hermetically connected with the inner wall of the tank body, and a steam outlet hole is formed in the middle of the arc body. The novel oil and steam separator is mainly used for purifying tail gas generated in an oil refining process and recycling oil drop in the tail gas.
Description
Technical field
The utility model belongs to a kind of exhaust gas processing device of oil and fat refining, specifically, relates in particular to a kind of novel fuel and vapor separator.
Background technology
In many operations of oil and fat refining, all have gas to discharge, these gases are called as tail gas, contain media such as oil, water, steam in the tail gas mostly; These media form a kind of vaporific mist; Do not add being discharged in the air of processing, promptly cause waste to strengthen production cost, pollute surrounding enviroment again.Original technology is used the spinning liquid isolation technics to the processing of these tail gas more; Opening gets into tail gas to cyclone hydraulic separators in the tangential of tank body, and tail gas gets into tangentially running behind the tank body, owing to centrifugally do effect; Drop is got rid of on tank skin to be stayed; Other gas is discharged from, but this technical efficiency is low, can only separate 70% drop.
Summary of the invention
The purpose of the utility model provides a kind of fuel and vapor separator, to overcome the inefficient defective of vent gas treatment that oil and fat refining process produces in the prior art.
The utility model has adopted following technical scheme: a kind of novel fuel and vapor separator; Comprise tank body; Tank body is provided with venthole, air intake, liquid outlet; Said tank interior is provided with first baffle plate, second baffle, and said first baffle plate is fixedly connected on the inner tank wall, is provided with out vapour opening A between first plate washer and the inner tank wall; Said second baffle is periphery and the airtight circular arc body that is connected of inner tank wall, and the center is provided with vapor opening.
Said second baffle top preferably is provided with the 3rd baffle plate, and the 3rd baffle plate is identical with the structure of first baffle plate.
Compared with prior art, the beneficial effect of the utility model: use the utility model effectively to improve the efficient of handling waste gas, therefore reduced the pollution to environment, the recovery of grease drop has simultaneously reduced production cost.
Description of drawings
Fig. 1 is the structural representation of the utility model;
Fig. 2 is the A-A cutaway view of Fig. 1;
Fig. 3 is the structural representation of first baffle plate of the utility model;
Fig. 4 is the structural representation of the second baffle of the utility model.
Among the figure: 1, venthole; 2, the 3rd baffle plate; 3, go out vapour opening B; 4, second baffle; 5, vapor opening; 6, go out vapour opening A; 7, first baffle plate; 8, liquid outlet; 9, air intake; 10, tank body.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is described further.
In the drawings, a kind of novel fuel and vapor separator comprises tank body 10, and tank body 10 tops are provided with vapor opening 5, and the bottom is provided with air intake 9 and liquid outlet 8.Tank body 10 inside are provided with first baffle plate 7, second baffle 4 and the 3rd baffle plate 2, and they are fixed on tank body 10 inside from the bottom up successively.First baffle plate 7 is the tetrahedral structure of the hollow that is spliced of three block plates; Its bottom surface does not have steel plate to connect; Therefore three angles of its bottom surface are fixedly connected on respectively on tank body 10 inwalls, and 7 three sides of first baffle plate respectively and form three between tank body 10 inwalls and go out vapour opening A6; Second baffle 4 is the circular-arc baffle plate that a centre is provided with a vapor opening 5, and its periphery and airtight connection of tank body 10 inwalls, second baffle 4 cambered surface openings its objective is that the drop that lets from the 3rd baffle plate 2 drippages imports the vapor opening 5 along cambered surface up; The 3rd baffle plate 2 is located at second baffle 4 tops, and its structure and first baffle plate 7 are just the same, and is fixedly connected in the same way on tank body 10 inwalls, forms three between itself and tank body 10 inwalls and goes out vapour opening B3.
During use, entire equipment is vertically placed, and venthole 1 flange connects exhaust gas treatment device, and air intake 8 flanges connect exhaust emissions.
The operation principle of the utility model: when the mist that contains droplet is flowed through vapour liquid separator with certain speed; Because the inertial impaction effect of gas; Mist at first bumps with first baffle plate 7, most of drop under the effect of tail gas impulse force attached to first baffle plate, 7 lower surfaces on, mist is gone out from going out vapour opening A6 under the extruding of first baffle plate 7; Tail gas of going out and impact are at second baffle 4 lower surfaces; In the tail gas remaining most of drop again attached to second baffle 4 outer surfaces, this moment, the droplet content in the tail gas was considerably less, then tail gas is gone out from vapor opening 5; Run into stopping of the 3rd baffle plate 2 again, small amount of drop is arranged again attached to the 3rd baffle plate 2 lower surfaces.Through stopping of three layers of baffle plate, do not contained drop basically in the tail gas, discharge through venthole 1 from the tail gas that goes out vapour opening B3 effusion at last.Sedimentation under the gravity effect of diffusion and drop of drops is gone up on first baffle plate 7, second baffle 4 and the 3rd baffle plate 2 surfaces; Make drop form bigger drop; Drop is increasing; Up to the drop that gathers arrive greatly climbing power that the gravity that himself produces surpasses gas and surface tension of liquid with joint efforts the time, drop just separates from first baffle plate 7, second baffle 4 and the 3rd baffle plate 2 surfaces.The drop of first baffle plate 7 directly splashes into liquid outlet 8; The drop of second baffle 4 drippages drops in first baffle plate, 7 upper surfaces and further splashes into liquid outlet 8 through going out vapour opening A6; Drop on the 3rd baffle plate 2 successively through the upper surface of second baffle 4 upper surfaces, venthole 5, first baffle plate 7, go out vapour opening A6, splash into liquid outlet 8 at last.Tail gas is through behind the utility model, and the gas that comes out is substantially free of drop.
Claims (2)
1. novel fuel and vapor separator; Comprise tank body (10); Tank body (10) is provided with venthole (1), air intake (9), liquid outlet (8); It is characterized in that: said tank body (10) inside is provided with first baffle plate (7), second baffle (4), and said first baffle plate (7) is fixedly connected on the inwall of tank body (10), is provided with out vapour opening A (6) between first baffle plate (7) and tank body (10) inwall; Said second baffle (4) is periphery and the airtight globoidal structure that is connected of tank body (10) inwall, and the center is provided with vapor opening (5).
2. novel fuel and vapor separator according to claim 1 is characterized in that: said second baffle (4) top is provided with the 3rd baffle plate (2), and the 3rd baffle plate (2) is identical with the structure of first baffle plate (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205695456U CN202427265U (en) | 2011-12-31 | 2011-12-31 | Novel oil and steam separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205695456U CN202427265U (en) | 2011-12-31 | 2011-12-31 | Novel oil and steam separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202427265U true CN202427265U (en) | 2012-09-12 |
Family
ID=46776742
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205695456U Expired - Fee Related CN202427265U (en) | 2011-12-31 | 2011-12-31 | Novel oil and steam separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202427265U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104162316A (en) * | 2014-08-28 | 2014-11-26 | 北京首位能源科技有限公司 | Novel automatic cyclone gas-liquid separation tank |
| CN108014510A (en) * | 2018-01-12 | 2018-05-11 | 无锡宝南机器制造有限公司 | A kind of ring bell-type vapor-liquid separation structure applied to MVR crystallizers |
| CN110237655A (en) * | 2019-06-21 | 2019-09-17 | 南京化工园博瑞德水务有限公司 | A kind of processing equipment of sludge drying tail gas |
| CN113813701A (en) * | 2021-10-19 | 2021-12-21 | 深圳市宏康环境科技有限公司 | Remove comdenstion water device and negative oxygen ion generating equipment |
-
2011
- 2011-12-31 CN CN2011205695456U patent/CN202427265U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104162316A (en) * | 2014-08-28 | 2014-11-26 | 北京首位能源科技有限公司 | Novel automatic cyclone gas-liquid separation tank |
| CN108014510A (en) * | 2018-01-12 | 2018-05-11 | 无锡宝南机器制造有限公司 | A kind of ring bell-type vapor-liquid separation structure applied to MVR crystallizers |
| CN110237655A (en) * | 2019-06-21 | 2019-09-17 | 南京化工园博瑞德水务有限公司 | A kind of processing equipment of sludge drying tail gas |
| CN110237655B (en) * | 2019-06-21 | 2022-05-24 | 南京化工园博瑞德水务有限公司 | Treatment facility of sludge drying tail gas |
| CN113813701A (en) * | 2021-10-19 | 2021-12-21 | 深圳市宏康环境科技有限公司 | Remove comdenstion water device and negative oxygen ion generating equipment |
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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: 20120912 Termination date: 20131231 |