CN203370439U - Oil steam recovery system - Google Patents
Oil steam recovery system Download PDFInfo
- Publication number
- CN203370439U CN203370439U CN201320439417.9U CN201320439417U CN203370439U CN 203370439 U CN203370439 U CN 203370439U CN 201320439417 U CN201320439417 U CN 201320439417U CN 203370439 U CN203370439 U CN 203370439U
- Authority
- CN
- China
- Prior art keywords
- oil
- valve
- absorber
- recovery system
- pipeline
- 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 - Lifetime
Links
Images
Landscapes
- Fuel-Injection Apparatus (AREA)
Abstract
The utility model discloses an oil steam recovery system. The oil steam recovery system comprises a water cooler, an absorber, a main heat exchanger, a gas-water separator, an oil-gas separator, a refrigerating system, a plurality of valves and two pumps, which are connected with one another by a pipeline; a diesel spray and absorption circulation system is formed by the absorber, the water cooler, an oil pump, an electrostatic eliminator, the valves and an ejector which are connected with one another by a pipeline. The oil steam recovery system has the advantages that an oil gas flow pipeline is not in direct contact with any electric appliance and rotating equipment, so that the oil steam recovery system is absolutely safe; the oil steam recovery system utilizes an aviation expansion refrigeration technology and an aviation refueling jet technology, completely reaches the national emission standard and is very advanced; the oil steam recovery system does not use refrigerants such as Freon, and does not use consumables such as carbon fibers, thus achieving an environment-friendly effect; the oil steam recovery system does not consume expensive substances such as a special absorbent, carbon fibers and activated carbon, does not need desorption, is high in refrigeration speed and relatively low in average power consumption and has an economical effect; the oil steam recovery system is ready to use after being switched on according to site conditions, does not need precooling for a long time, and is simple to operate.
Description
Technical field
The utility model relates to the petrochemical industry oil vapour and reclaims field, relates in particular to the oil vapour recovery system.
Background technology
Oil is one of main energy of China, and oil product is huge in storage and transport process evaporating loss economic loss.Consume mainly occurs in receipts oil and the processes such as automobile fuel filler, rail tank car unloading system liquid-ring vacuum pump exhaust of oil of oil transferring, Station in City ground tank of blending in the pipe of product oil, rail tank car, road tank car, waterborne vessel, and oil gas volatilization causes the indirect losses such as potential safety hazard, environmental pollution more huge.Therefore, need to provide a kind of new technical scheme to solve the problems referred to above.
The utility model content
Evaporate in order to overcome existing oil product environmental problem, the potential safety hazard that the economic loss that causes and volatilization cause in storage and transport process, the utility model provides a kind of oil vapour recovery system.
The technical solution adopted in the utility model:
A kind of oil vapour recovery system, comprise absorber, water cooler, main heat exchanger, moisture trap, gs-oil separator and refrigeration system.The valve I is connected with an end of water cooler I by pipeline, the other end of water cooler I connects the moisture trap upper end, the lower end of moisture trap is connected with injector by pipeline, the injector lower end connects absorber, the other end of absorber is connected with an end of main heat exchanger by pipeline, main heat exchanger is connected with refrigeration system, the other end of main heat exchanger connects an end of gs-oil separator, the other end connection valve III of gs-oil separator, the valve III connects the oil pump II, the other end of gs-oil separator is connected with the water cooler I, the other end connection valve II of water cooler I, the valve II connects injector, the other joint noise reduction device of injector, the lower end connection valve IV of absorber, the absorber lower end also is provided with pipeline and is connected with the water cooler II, the other end of water cooler II is connected with the oil pump I by pipeline, the other end of oil pump I is fixedly connected with the Xelminator I, the Xelminator I is connected with the valve V again, the other end of valve V connects the injector head of injector, the lower end of absorber is connected with the valve VI, the other end of valve VI is connected with the oil pump II, described absorber forms diesel injection absorption cycle system by pipeline with water cooler II, oil pump I, Xelminator I, valve V together with injector.
Described absorber comprises absorber cavity, blender and Xelminator II, and the Xelminator II is fixed in blender near on the pipeline of import, has a plurality of mixing mouthful on blender.
The beneficial effects of the utility model: the oil gas flow line does not directly contact with rotating machinery with any electrical equipment, thoroughly eliminates safe hidden trouble, and is perfectly safe; Use aviation swell refrigeration technology, air fuel handing fluidics, reach discharging standards fully, very advanced; Do not use the cold-producing mediums such as freon, pollution-free, do not use carbon fiber equal loss material, non-secondary pollution, environmental protection; Do not consume the expensive materials such as special absorptive agent, carbon fiber, active carbon, do not need desorb, refrigerating speed is fast, and average power consumption is relatively low, economy; Can without long-time precooling, be particularly suitable for the interval work situation according to field condition with using with opening, automaticity is high, and a complete set of PLC and PC desktop computer are controlled, simple to operate.
The accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Wherein: 1, valve I, 2, the valve II, 3, injector, 4, muffler, 5, water cooler I, 6, moisture trap, 7, the valve V, 8, the Xelminator I, 9, injector, 10, the oil pump I, 11, the Xelminator II, 12, the water cooler II, 13, valve IV, 14, refrigeration system, 15, main heat exchanger, 16, gs-oil separator, 17, absorber, 18, the valve III, 19, blender, 20, the oil pump II, 21, the valve VI.
The specific embodiment
As shown in Figure 1, this system comprises valve I 1, valve II 2, injector 3, muffler 4, water cooler I 5, moisture trap 6, valve V 7, Xelminator I 8, injector 9, oil pump I 10, Xelminator II 11, water cooler II 12, valve IV 13, refrigeration system 14, main heat exchanger 15, gs-oil separator 16, absorber 17, valve III 18, blender 19, oil pump II 20 and valve VI 21.
Valve I 1 is connected with an end of water cooler I 5 by pipeline, the other end of water cooler I 5 connects moisture trap 6 upper ends, the lower end of moisture trap 6 is connected with injector 9 by pipeline, injector 9 lower ends connect absorber 17, the other end of absorber 17 is connected with an end of main heat exchanger 15 by pipeline, main heat exchanger 15 is connected with refrigeration system 14, the other end of main heat exchanger 15 connects an end of gs-oil separator 16, the other end connection valve III 18 of gs-oil separator 16, valve III 18 connects oil pump II 20, the other end of gs-oil separator 16 is connected with water cooler I 5, the other end connection valve II 2 of water cooler I 5, valve II 2 connects injector 3, the other joint noise reduction device 4 of injector 3, the lower end connection valve IV 13 of absorber 17, absorber 17 lower ends also are provided with pipeline and are connected with water cooler II 12, the other end of water cooler II 12 is connected with oil pump I 10 by pipeline, the other end of oil pump I 10 is fixedly connected with Xelminator I 8, Xelminator I 8 is connected with valve V 7 again, the other end of valve V 7 connects the injector head of injector 9, the lower end of absorber is connected with valve VI 21, the other end of valve VI 21 is connected with oil pump II 20.
Absorber 17 comprises absorber cavity, blender 19 and Xelminator II 11, and Xelminator II 11 is fixed in blender 19 near on the pipeline of import, has a plurality of mixing mouthful on blender 19.
Absorber forms diesel injection absorption cycle system by pipeline with water cooler II 12, oil pump I 10, Xelminator I 8, valve V 7 together with injector 9.
Recovery method: open valve IV 13, diesel oil is sent in absorber 17 by valve, in absorber 17 liquid level reach total liquid level 50% the time, shut off valve IV 13; Open valve I 1, II 2, III 18, V 7, start oil pump, the system entry into service, oil gas is sent into 5 precoolings of water cooler I and dewaters by valve I 1, oil gas be take by valve II 2 injector 3 that diesel oil is medium and is sucked, in moisture trap 6, fully gas-liquid mixed enters absorber 17 by injector 9 and fully mixes, unabsorbed C
1, C
2gas is cooling by gs-oil separator 16 separation through main heat exchanger 15 heat exchange, then enters pump II 20 through valve III 18, and then utilizes; The diesel injection absorption cycle system that diesel oil in absorber 17 forms by water cooler II 12, oil pump I 10, Xelminator I 8, valve V 7 and injector 9 is at the jet mineralization pressure liquid of injector, absorb fast fluid, promote the abundant mixing of oil gas, liquid level in absorber 17 reaches 85%, close all valves, oil pump, then the Open valve VI 21, and absorber is communicated with oil pump II 20, recycled, finally completed the cyclic process that an oil vapour reclaims.
The beneficial effects of the utility model: the oil gas flow line does not directly contact with rotating machinery with any electrical equipment, thoroughly eliminates safe hidden trouble, and is perfectly safe; Use aviation swell refrigeration technology, air fuel handing fluidics, reach discharging standards fully, very advanced; Do not use the cold-producing mediums such as freon, pollution-free, do not use carbon fiber equal loss material, non-secondary pollution, environmental protection; Do not consume the expensive materials such as special absorptive agent, carbon fiber, active carbon, do not need desorb, refrigerating speed is fast, and average power consumption is relatively low, economy; Can without long-time precooling, be particularly suitable for the interval work situation according to field condition with using with opening, automaticity is high, and a complete set of PLC and PC desktop computer are controlled, simple to operate.
Claims (2)
1. an oil vapour recovery system, it is characterized in that this system comprises absorber, water cooler, main heat exchanger, moisture trap, gs-oil separator and refrigeration system, the valve I is connected with an end of water cooler I by pipeline, the other end of water cooler I connects the moisture trap upper end, the lower end of moisture trap is connected with injector by pipeline, the injector lower end connects absorber, the other end of absorber is connected with an end of main heat exchanger by pipeline, main heat exchanger is connected with refrigeration system, the other end of main heat exchanger connects an end of gs-oil separator, the other end connection valve III of gs-oil separator, the valve III connects the oil pump II, the other end of gs-oil separator is connected with the water cooler I, the other end connection valve II of water cooler I, the valve II connects injector, the other joint noise reduction device of injector, the lower end connection valve IV of absorber, the absorber lower end also is provided with pipeline and is connected with the water cooler II, the other end of water cooler II is connected with the oil pump I by pipeline, the other end of oil pump I is fixedly connected with the Xelminator I, the Xelminator I is connected with the valve V again, the other end of valve V connects the injector head of injector, the lower end of absorber is connected with the valve VI, the other end of valve VI is connected with the oil pump II, described absorber forms diesel injection absorption cycle system by pipeline with water cooler II, oil pump I, Xelminator I, valve V together with injector.
2. a kind of oil vapour recovery system according to claim 1, it is characterized in that: described absorber comprises absorber cavity, blender and Xelminator II, described Xelminator II is fixed in blender near on the pipeline of import, has a plurality of mixing mouthful on described blender.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320439417.9U CN203370439U (en) | 2013-07-23 | 2013-07-23 | Oil steam recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320439417.9U CN203370439U (en) | 2013-07-23 | 2013-07-23 | Oil steam recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203370439U true CN203370439U (en) | 2014-01-01 |
Family
ID=49832996
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320439417.9U Expired - Lifetime CN203370439U (en) | 2013-07-23 | 2013-07-23 | Oil steam recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203370439U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103349885A (en) * | 2013-07-23 | 2013-10-16 | 蔡兵 | Oil steam recovery system and recovery method |
| CN109045761A (en) * | 2018-07-13 | 2018-12-21 | 佛山市三水区精联自动化设备有限公司 | A kind of hydrocarbon vapour-recovery unit |
-
2013
- 2013-07-23 CN CN201320439417.9U patent/CN203370439U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103349885A (en) * | 2013-07-23 | 2013-10-16 | 蔡兵 | Oil steam recovery system and recovery method |
| CN103349885B (en) * | 2013-07-23 | 2015-04-15 | 蔡兵 | Oil steam recovery system and recovery method |
| CN109045761A (en) * | 2018-07-13 | 2018-12-21 | 佛山市三水区精联自动化设备有限公司 | A kind of hydrocarbon vapour-recovery unit |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106481974A (en) | A kind of BOG accumulation of energy pressure reduction LNG gas station | |
| CN201769651U (en) | Refrigerator car with function of liquefied natural gas (LNG) cold energy recovery | |
| CN203370439U (en) | Oil steam recovery system | |
| CN103821592A (en) | LNG automobile cold energy recovery gradient utilization method and device | |
| CN204716420U (en) | Case sled formula natural gas generator group device | |
| CN103832244B (en) | A kind of LNG cold energy reclaims the method and apparatus being used for automobile zero-emission and air-conditioning | |
| CN202481606U (en) | Jet-type oil gas recycling system | |
| CN103349885B (en) | Oil steam recovery system and recovery method | |
| CN204472492U (en) | A kind of commercial refrigeration car LNG cold energy recovery system | |
| CN203950890U (en) | The dc-battery cooling system of the cooling use of pure electric automobile battery | |
| CN102491019B (en) | Jet type oil and gas recovering system and method | |
| CN203560708U (en) | Secondary circulating cooling water system for cold oil | |
| CN104406327A (en) | Multi-mode waste heat driven automobile air conditioning system | |
| CN201828083U (en) | Waste-heat injecting refrigerator using R236FA as refrigerant | |
| CN102698566A (en) | High and medium pressure regeneration system for flue gas decarbonization | |
| CN203730099U (en) | Cold energy recovery and gradient utilization device for LNG (liquefied natural gas) vehicle | |
| CN202605975U (en) | High-pressure and medium-pressure regenerating device for decarbonizing smoke | |
| CN102654326A (en) | Double-injection refrigeration device synergized by gas-liquid ejector | |
| CN202266346U (en) | Engine exhaust afterheat recycling control system based on organic rankine cycle | |
| CN205102628U (en) | Saving energy and increasing efficiency's condenser water charging system | |
| CN103707738A (en) | Method and device for recovering LNG cold energy for automobile air conditioner system | |
| CN202270465U (en) | Combined device for absorbing acid gas | |
| CN104236162B (en) | Refrigeration/heating device of locomotive | |
| CN203769942U (en) | Liquid-state air refrigeration generating device for data centre | |
| CN208281062U (en) | A kind of system using liquid oxygen misting cooling heat engine inlet air |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20140101 Effective date of abandoning: 20150415 |
|
| RGAV | Abandon patent right to avoid regrant |