CN204689945U - Waste oil cracking rectifying gas-liquid separator - Google Patents
Waste oil cracking rectifying gas-liquid separator Download PDFInfo
- Publication number
- CN204689945U CN204689945U CN201520349789.1U CN201520349789U CN204689945U CN 204689945 U CN204689945 U CN 204689945U CN 201520349789 U CN201520349789 U CN 201520349789U CN 204689945 U CN204689945 U CN 204689945U
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- China
- Prior art keywords
- gas
- liquid separation
- storage tank
- oil
- tower
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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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- 239000007788 liquid Substances 0.000 title claims abstract description 46
- 239000002699 waste material Substances 0.000 title claims abstract description 24
- 238000005336 cracking Methods 0.000 title claims abstract description 16
- 238000001816 cooling Methods 0.000 claims abstract description 40
- 238000000926 separation method Methods 0.000 claims abstract description 34
- 238000003860 storage Methods 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000001737 promoting effect Effects 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 43
- 238000000034 method Methods 0.000 description 6
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- 238000004821 distillation Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 238000009874 alkali refining Methods 0.000 description 1
- 239000002199 base oil Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Waste oil cracking rectifying gas-liquid separator of the present utility model, it is characterized in that: above gas-liquid separation tower, be provided with cooling tower, storage tank is provided with in the below of gas-liquid separation tower, cooling tube is provided with in cooling tower, the top of cooling tube communicates with Oil/Gas Pipe, water intaking valve is connected with in the bottom of cooling tower, top is connected with outlet valve, oil nozzle is provided with out in gas-liquid separation tower, go out oil nozzle to be communicated with the bottom of cooling tube, oil outlet pipe is provided with in the bottom of gas-liquid separation tower, oil outlet pipe is provided with fuel-displaced porthole, delivery valve, gas-liquid separation tower is connected with tensimeter, vacuum pump, muffler is provided with between the top and the top of gas-liquid separation tower of storage tank, muffler is provided with storage tank return-air valve, storage tank delivery valve is also provided with in the bottom of storage tank, storage tank is also provided with oil-release valve, liquidometer, tensimeter.It is rational in infrastructure, simply, easy to operate for this device, and use safety, gas-liquid separation production cost is low, has promotional value.
Description
Technical field
The utility model relates to oil conditioner, more specifically relates to a kind of waste oil cracking rectifying gas-liquid separator.
Background technology
Waste oil refers to that oil plant in use for some time, and owing to polluting the immersion of impurity and the deterioration by oxidation of fractions, can not use necessary renew oil in continuation, the oil changed is referred to as waste oil.Waste oil carry out purifying regeneration process can close to or reach the standard of fresh oil, also waste oil regeneration can be become fuel oil or base oil, turn waste into wealth, benefit the nation and the people.At present, technology of waste oil regenerating, mainly contains five kinds: acid-alkali refining method, filter sieve partition method, centrifugal separation, gasification separation method, distillation hydrofining method, its Processes and apparatus has his own strong points, and respectively has shortage.Although gasification separation method is generally acknowledged better, existing equipment is more complicated, is not suitable with the use of medium and small waste oil treatment unit, meanwhile, the effect of gas-liquid separation is poor, for this reason, have much room for improvement waste oil regeneration instrument and supplies, explores a kind of waste oil cracking rectifying gas-liquid separator.
Summary of the invention
The purpose of this utility model: a kind of waste oil cracking rectifying gas-liquid separator is provided.
The technical solution of the utility model is: a kind of waste oil cracking rectifying gas-liquid separator, it is characterized in that: above gas-liquid separation tower, be provided with cooling tower, storage tank is provided with in the below of gas-liquid separation tower, cooling tube is provided with in cooling tower, the top of cooling tube communicates with Oil/Gas Pipe, water intaking valve is connected with in the bottom of cooling tower, top is connected with outlet valve, oil nozzle is provided with out in gas-liquid separation tower, go out oil nozzle to be communicated with the bottom of cooling tube, oil outlet pipe is provided with in the bottom of gas-liquid separation tower, oil outlet pipe is provided with fuel-displaced porthole, delivery valve, gas-liquid separation tower is connected with tensimeter, vacuum pump, muffler is provided with between the top and the top of gas-liquid separation tower of storage tank, muffler is provided with storage tank return-air valve, storage tank delivery valve is also provided with in the bottom of storage tank, storage tank is also provided with oil-release valve, liquidometer, tensimeter.
Described waste oil cracking rectifying gas-liquid separator, the cooling tube helically type of the cooling tower described in it, the heat-eliminating medium of cooling tower is water, and pump makes water enter top outflow from the bottom of cooling tower.
Waste oil cracking rectifying gas-liquid separator described above, the vacuum tightness that the vacuum pump described in it controls in gas-liquid separation tower is 1 to 360Pa.
Waste oil cracking rectifying gas-liquid separator of the present utility model mainly will be gasified by reactor heating pyrolyze and by the gaseous state of rectifying tower catalytic distillation oil, carry out cooling, being separated at this device, by gaseous state oil liquefy oil and be kept at storage tank, meanwhile, the assorted gas in gaseous state oil is passed through vacuum pump sucking-off.
The beneficial effects of the utility model, waste oil cracking rectifying gas-liquid separator of the present utility model is the important component part of waste oil cracking rectifying regenerating unit, it is rational in infrastructure, simply, easy to operate, use safety, the speed of gaseous state oil cooling liquefy oil is fast, equipment runs under negative pressure or normal pressure, and gas-liquid separation production cost is low, has promotional value.
Accompanying drawing explanation
Accompanying drawing is structural representation of the present utility model.
Mark Oil/Gas Pipe 1, outlet valve 2, snifting valve 3, cooling tube 4, cooling tower 5, water intaking valve 6 in figure, go out oil nozzle 7, gas-liquid separation tower 8, fuel-displaced porthole 9, delivery valve 10, storage tank 11, storage tank delivery valve 12, storage tank return-air valve 13, vacuum pump 14, tensimeter 15, liquidometer 16.
Embodiment
Below by embodiment, the utility model is further described.
Embodiment,
With reference to accompanying drawing, a kind of waste oil cracking rectifying gas-liquid separator, cooling tower 5 is provided with above gas-liquid separation tower 8, storage tank 11 is provided with in the below of gas-liquid separation tower 8, cooling tube 4 is provided with in cooling tower 5, the top of cooling tube 4 communicates with Oil/Gas Pipe 1, water intaking valve 6 is connected with in the bottom of cooling tower 5, top is connected with outlet valve 2, oil nozzle 7 is provided with out in gas-liquid separation tower 8, go out oil nozzle 7 to be communicated with the bottom of cooling tube 4, oil outlet pipe is provided with in the bottom of gas-liquid separation tower 8, oil outlet pipe is provided with fuel-displaced porthole 9, delivery valve 10, gas-liquid separation tower 8 is connected with tensimeter 15, vacuum pump 14, muffler is provided with between the top of storage tank 11 and the top of gas-liquid separation tower 8, muffler is provided with storage tank return-air valve 13, storage tank delivery valve 12 is also provided with in the bottom of storage tank 11, storage tank 11 is also provided with oil-release valve 3, liquidometer 16, tensimeter, the cooling tube 4 helically type of described cooling tower 5, the heat-eliminating medium of cooling tower 5 is water, and pump makes water enter top outflow from the bottom of cooling tower 5, described vacuum pump 14 vacuum tightness controlled in gas-liquid separation tower 8 is 1 to 360Pa, and the concrete selection of vacuum tightness should adapt with production technique.
Claims (3)
1. a waste oil cracking rectifying gas-liquid separator, it is characterized in that: be provided with cooling tower (5) in the top of gas-liquid separation tower (8), storage tank (11) is provided with in the below of gas-liquid separation tower (8), cooling tube (4) is provided with in cooling tower (5), the top of cooling tube (4) communicates with Oil/Gas Pipe (1), water intaking valve (6) is connected with in the bottom of cooling tower (5), top is connected with outlet valve (2), oil nozzle (7) is provided with out in gas-liquid separation tower (8), go out oil nozzle (7) to be communicated with the bottom of cooling tube (4), oil outlet pipe is provided with in the bottom of gas-liquid separation tower (8), oil outlet pipe is provided with fuel-displaced porthole (9), delivery valve (10), gas-liquid separation tower (8) is connected with tensimeter (15), vacuum pump (14), muffler is provided with between the top of storage tank (11) and the top of gas-liquid separation tower (8), muffler is provided with storage tank return-air valve (13), storage tank delivery valve (12) is also provided with in the bottom of storage tank (11), storage tank (11) is also provided with oil-release valve (3), liquidometer (16), tensimeter.
2. by waste oil cracking rectifying gas-liquid separator according to claim 1, it is characterized in that: cooling tube (4) the helically type of described cooling tower (5), the heat-eliminating medium of cooling tower (5) is water, and pump makes water enter top outflow from the bottom of cooling tower (5).
3. by the waste oil cracking rectifying gas-liquid separator described in claim 1 or 2, it is characterized in that: the vacuum tightness that described vacuum pump (14) controls in gas-liquid separation tower (8) is 1 to 360Pa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520349789.1U CN204689945U (en) | 2015-05-27 | 2015-05-27 | Waste oil cracking rectifying gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520349789.1U CN204689945U (en) | 2015-05-27 | 2015-05-27 | Waste oil cracking rectifying gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204689945U true CN204689945U (en) | 2015-10-07 |
Family
ID=54230258
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520349789.1U Expired - Fee Related CN204689945U (en) | 2015-05-27 | 2015-05-27 | Waste oil cracking rectifying gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204689945U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104845658A (en) * | 2015-05-27 | 2015-08-19 | 重庆方盛净化设备有限公司 | Cracking-rectifying gas-liquid separation device for waste oil |
| CN107860249A (en) * | 2017-12-15 | 2018-03-30 | 重庆方盛净化设备有限公司 | Waste oil regeneration rectifying catalysis system residual heat using device |
| CN115340883A (en) * | 2022-08-10 | 2022-11-15 | 王飞 | Waste oil cracking rectification gas-liquid separation equipment and separation method |
-
2015
- 2015-05-27 CN CN201520349789.1U patent/CN204689945U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104845658A (en) * | 2015-05-27 | 2015-08-19 | 重庆方盛净化设备有限公司 | Cracking-rectifying gas-liquid separation device for waste oil |
| CN107860249A (en) * | 2017-12-15 | 2018-03-30 | 重庆方盛净化设备有限公司 | Waste oil regeneration rectifying catalysis system residual heat using device |
| CN107860249B (en) * | 2017-12-15 | 2023-09-19 | 重庆方盛净化设备有限公司 | Waste heat utilization device of waste oil regeneration rectification catalytic system |
| CN115340883A (en) * | 2022-08-10 | 2022-11-15 | 王飞 | Waste oil cracking rectification gas-liquid separation equipment and separation method |
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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: 20151007 |