CN203530277U - Mixed oil evaporation device - Google Patents
Mixed oil evaporation device Download PDFInfo
- Publication number
- CN203530277U CN203530277U CN201320461129.3U CN201320461129U CN203530277U CN 203530277 U CN203530277 U CN 203530277U CN 201320461129 U CN201320461129 U CN 201320461129U CN 203530277 U CN203530277 U CN 203530277U
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- condenser
- mixed oil
- vaporizer
- stripping tower
- evaporation device
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Abstract
The utility model relates to the technical field of grease processing, and particularly relates to a mixed oil evaporation device. The mixed oil evaporation device comprises a mixed oil tank, a first evaporator and a first flash evaporation box which are sequentially connected, wherein the bottom of the first flash evaporation box is connected with a second evaporator, the top of the first flash evaporation box is connected with a first condenser, the second evaporator is connected with a second flash evaporation box, the bottom of the second flash evaporation box is connected with a stripping tower, the top of the second flash evaporation box is connected with a second condenser, the top of the stripping tower is connected with a third condenser, the first condenser, the second condenser and the third condenser are respectively connected with a water ring vacuum pump, and the water ring vacuum pump is connected with a fourth condenser. The mixed oil evaporation device has the advantages of being simple and convenient to operate, lowering the production cost and avoiding the waste of energy sources.
Description
Technical field
The utility model relates to a kind of grease processing technology field, is specifically related to a kind of miscella evaporation device.
Background technology
In oil processing industry, in vapo(u)rization system, to lean on high temperature by the solvent in mixing oil and separating of oil, generally, temperature requirement is high, and thermal waste is serious, reduces and produces the target that consumption is the continuous pursuit of enterprise.
Utility model content
According to above deficiency of the prior art, the technical problems to be solved in the utility model is: a kind of miscella evaporation device is provided, can save energy, reduce production costs, easy and simple to handle.
The utility model solves the technical scheme that its technical problem adopts:
A kind of miscella evaporation device is provided, comprise that miscella tank, the first vaporizer and the first shwoot case are connected successively, the first shwoot case bottom is connected with the second vaporizer, the first shwoot box top is connected with the first condenser, the second vaporizer is connected with the second shwoot case, the second shwoot case bottom is connected with stripping tower, the second shwoot box top is connected with the second condenser, stripping tower top is connected with the 3rd condensing tower, the first condenser, the second condenser and the 3rd condenser are connected with water ring vacuum pump respectively, and water ring vacuum pump is connected with the 4th condenser.
Described stripping tower bottom is provided with crude oil outlet.
Principle of work and process:
Mixing oil flows out from miscella tank, and successively through the first vaporizer, the first shwoot case, the second vaporizer, the second shwoot case and stripping tower evaporates and stripping, the crude oil obtaining enters refining oil workshop from crude oil outlet.Solvent gas in the first shwoot case, the second shwoot case and stripping tower enters respectively the first condenser, the second condenser and the 3rd condenser condenses.In the first condenser, the second condenser and the 3rd condenser, uncooled solvent gas enters the 4th condenser condenses by water ring vacuum pump.Water ring vacuum pump vacuumizes the first vaporizer, the second vaporizer and stripping tower, and vacuum tightness reaches 47KPa, makes mixing oil under negative pressure, carry out separation.
The beneficial effect that the utility model has is:
Mixing oil enters after shwoot case, and because volume increases rapidly, pressure reduces, and solvent gas is accelerated separated with mixing oil.The utility model is easy and simple to handle, reduced production cost, avoided the waste of the energy.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation;
In figure: 1, miscella tank; 2, the first vaporizer; 3, the first shwoot case; 4, the second vaporizer; 5, the second shwoot case; 6, stripping tower; 7, the first condenser; 8, the second condenser; 9, the 3rd condenser; 10, water ring vacuum pump; 11, the 4th condenser; 12, crude oil outlet.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described further:
As shown in Figure 1, the utility model is included in miscella tank 1, the first vaporizer 2 is connected successively with the first shwoot case 3, the first shwoot case 3 bottoms are connected with the second vaporizer 4, the first shwoot case 3 tops are connected with the first condenser 7, the second vaporizer 4 is connected with the second shwoot case 5, the second shwoot case 5 bottoms are connected with stripping tower 6, the second shwoot case 5 tops are connected with the second condenser 8, stripping tower 6 tops are connected with the 3rd condensing tower 9, the first condenser 7, the second condenser 8 is connected with water ring vacuum pump 10 respectively with the 3rd condenser 9, water ring vacuum pump 10 is connected with the 4th condenser 11.
Mixing oil flows out from miscella tank 1, evaporates and stripping successively through the first vaporizer 2, the first shwoot case 3, the second vaporizer 4, the second shwoot case 5 and stripping tower 6, and the crude oil obtaining enters refining oil workshop from crude oil outlet 12.Solvent gas in the first shwoot case 3, the second shwoot case 5 and stripping tower 6 enters respectively the first condenser 7, the second condenser 8 and the 3rd condenser 9 condensations.In the first condenser 7, the second condenser 8 and the 3rd condenser 9, uncooled solvent gas enters the 4th condenser 11 condensations by water ring vacuum pump 10.Water ring vacuum pump 10 pairs of the first vaporizers 2, the second vaporizer 4 and stripping towers 6 vacuumize, and vacuum tightness reaches 47KPa, makes mixing oil under negative pressure, carry out separation.
Claims (2)
1. a miscella evaporation device, it is characterized in that miscella tank (1), the first vaporizer (2) is connected successively with the first shwoot case (3), the first shwoot case (3) bottom is connected with the second vaporizer (4), the first shwoot case (3) top is connected with the first condenser (7), the second vaporizer (4) is connected with the second shwoot case (5), the second shwoot case (5) bottom is connected with stripping tower (6), the second shwoot case (5) top is connected with the second condenser (8), stripping tower (6) top is connected with the 3rd condensing tower (9), the first condenser (7), the second condenser (8) is connected with water ring vacuum pump (10) respectively with the 3rd condenser (9), water ring vacuum pump (10) is connected with the 4th condenser (11).
2. miscella evaporation device according to claim 1, is characterized in that described stripping tower (6) bottom is provided with crude oil outlet (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320461129.3U CN203530277U (en) | 2013-07-31 | 2013-07-31 | Mixed oil evaporation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320461129.3U CN203530277U (en) | 2013-07-31 | 2013-07-31 | Mixed oil evaporation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203530277U true CN203530277U (en) | 2014-04-09 |
Family
ID=50416511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320461129.3U Expired - Fee Related CN203530277U (en) | 2013-07-31 | 2013-07-31 | Mixed oil evaporation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203530277U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106629937A (en) * | 2015-11-02 | 2017-05-10 | 中国石油化工股份有限公司 | Waste water processing technology and system |
-
2013
- 2013-07-31 CN CN201320461129.3U patent/CN203530277U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106629937A (en) * | 2015-11-02 | 2017-05-10 | 中国石油化工股份有限公司 | Waste water processing technology and system |
| CN106629937B (en) * | 2015-11-02 | 2020-05-19 | 中国石油化工股份有限公司 | Wastewater treatment process and system |
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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: 20140409 Termination date: 20140731 |
|
| EXPY | Termination of patent right or utility model |