A dock oil and gas recovery device
By designing a terminal oil and gas recovery device with multi-stage repeated condensation and adsorption, the problem of insufficient oil and gas recovery in the prior art is solved, and an efficient and environmentally friendly oil and gas recovery effect is achieved.
Patent Information
- Application Number
- CN202421375982.8
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-06-17
- Publication Date
- 2025-04-11
- Estimated Expiration
- 2034-06-17
AI Technical Summary
After the existing terminal oil and gas recovery devices are single-time adsorption and condensation treatment, it is difficult to ensure the full recovery of oil and gas, resulting in emission pollution.
A multi-stage repeated condensation and adsorption terminal oil and gas recovery device is designed, including multiple condensers, gas-liquid separators, adsorption beds and vacuum pumps, to ensure sufficient oil and gas recovery through multi-stage treatment.
Through multi-stage condensation and adsorption treatment, the adequacy and efficiency of oil and gas recovery are significantly improved, emission pollution is avoided, and the environment is clean.
Smart Images

Figure CN222738796U_ABST
Abstract
Description
Technical Field
[0001] The utility model belongs to the technical field of recovery, and in particular relates to a wharf oil and gas recovery device. Background Art
[0002] Oil and gas recovery at the terminal refers to the technology of collecting and treating the oil and gas generated during the loading and unloading process of the marine terminal to reduce environmental pollution and improve energy utilization. This technology can effectively reduce the impact of hydrocarbons on the environment and human health, while improving energy utilization efficiency and reducing production costs. Oil and gas recovery at the terminal generally includes three steps: collection, treatment and utilization. The collection methods include adsorption, condensation and combustion. The treatment process is mainly separation and purification to remove impurities and moisture to obtain high-purity hydrocarbons. Finally, the treated hydrocarbons can be used in equipment such as heating furnaces and generators in the production process, or sold and reused. The whole process will involve related oil and gas recovery equipment.
[0003] However, in the current recovery process, only one-time adsorption and condensation treatment is performed, which makes it difficult to ensure the recovery effect of oil and gas, and still causes emission pollution. Therefore, it is necessary to design a wharf oil and gas recovery device to ensure that impurities can be fully adsorbed and oil and gas can be fully recovered. Summary of the invention
[0004] In order to solve the deficiencies in the prior art, the utility model provides a dock oil and gas recovery device.
[0005] In order to achieve the above purpose, the utility model provides the following technical solutions:
[0006] A dock oil and gas recovery device comprises a first condenser, a first filter, a first gas-liquid separator, a first adsorption bed, a first exhaust fan, a first cooler, a first storage tank, a second storage tank, a first vacuum pump, a second condenser, a second gas-liquid separator, a third condenser, a third gas-liquid separator and a third storage tank, wherein a first inlet end of the first condenser is connected to a ship loading waste gas source, a first outlet end of the first condenser is connected to a first inlet end of the first gas-liquid separator, a first outlet end of the first gas-liquid separator is connected to a first inlet end of the first storage tank, a second outlet end of the first gas-liquid separator is connected to a first inlet end of the first filter, a first outlet end of the first filter is connected to a first inlet and outlet of the first adsorption bed, a second inlet and outlet of the first adsorption bed is connected to a first inlet end of the first exhaust fan, a first inlet end of the first cooler is connected to a first inlet end of the first adsorption bed, and a second inlet and outlet of the first adsorption bed are connected to a first inlet end of the first exhaust fan. The first inlet and outlet of an adsorption bed are connected, the first outlet end of the first cooler is connected to the first inlet end of the second storage tank, the first outlet end of the second storage tank is connected to the first inlet end of the first vacuum pump, the first outlet end of the first vacuum pump is connected to the first inlet end of the second condenser, the first outlet end of the second condenser is connected to the first inlet end of the second gas-liquid separator, the first outlet end of the second gas-liquid separator is connected to the first inlet end of the third storage tank, the second outlet end of the second gas-liquid separator is connected to the first inlet end of the third condenser, the first outlet end of the third condenser is connected to the first inlet end of the third gas-liquid separator, the first outlet end of the third gas-liquid separator is connected to the second inlet end of the third storage tank, and the second outlet end of the third gas-liquid separator is connected to the first inlet and outlet of the first adsorption bed.
[0007] Furthermore, the wharf oil and gas recovery device includes a fourth storage tank, a first liquid outlet pump and a second liquid outlet pump, the first inlet end of the fourth storage tank is connected to the second outlet end of the first vacuum pump, the first outlet end of the fourth storage tank and the first outlet end of the third storage tank are both connected to the first inlet end of the first liquid outlet pump, the first outlet end of the first liquid outlet pump is connected to the second inlet end of the first storage tank, and the first inlet end of the second liquid outlet pump is connected to the first outlet end of the first storage tank.
[0008] Furthermore, the wharf oil and gas recovery device includes a second cooler and a first cooling fan, the first inlet end of the second cooler is connected to the first inlet and outlet of the first adsorption bed, the first outlet end of the second cooler is connected to the first inlet end of the first cooling fan, and the first outlet end of the first cooling fan is connected to the second inlet and outlet of the first adsorption bed.
[0009] Furthermore, the wharf oil and gas recovery device includes a second adsorption bed and a third adsorption bed, the first inlet and outlet of the first adsorption bed, the first inlet and outlet of the second adsorption bed, and the first inlet and outlet of the third adsorption bed are all connected to the second outlet end of the third gas-liquid separator, and the second inlet and outlet of the second adsorption bed and the second inlet and outlet of the third adsorption bed are both connected to the second inlet and outlet of the first adsorption bed.
[0010] Furthermore, the wharf oil and gas recovery device includes a second vacuum pump, a fourth condenser and a fifth condenser, the first inlet end of the second vacuum pump is connected to the first inlet end of the first vacuum pump, the first outlet end of the second vacuum pump is connected to the first outlet end of the first vacuum pump, the first inlet end of the fourth condenser is connected to the first inlet end of the third condenser, the first outlet end of the fourth condenser is connected to the first outlet end of the third condenser, the first inlet end of the fifth condenser is connected to the first inlet end of the first condenser, and the first outlet end of the fifth condenser is connected to the first outlet end of the first condenser.
[0011] The utility model discloses a wharf oil and gas recovery device, which has the beneficial effect of being stable and reliable in structure compared with the prior art, and is capable of adsorbing wharf exhaust gas and recovering oil and gas through condensation, thereby avoiding environmental pollution; through multi-stage repeated condensation and adsorption, the sufficiency and efficiency of oil and gas recovery can be guaranteed, thereby avoiding emission pollution. BRIEF DESCRIPTION OF THE DRAWINGS
[0012] Figure 1 It is a structural schematic diagram of a preferred embodiment provided by the utility model.
[0013] Figure 2 It is a structural schematic diagram of the first storage tank of the preferred embodiment provided by the utility model.
[0014] Figure 3 It is a structural schematic diagram of the second storage tank of the preferred embodiment provided by the utility model.
[0015] Figure 4 It is a structural schematic diagram of the first adsorption bed of the preferred embodiment provided by the utility model.
[0016] The reference numerals include: 1. first adsorption bed; 2. second adsorption bed; 3. third adsorption bed; 4. first condenser; 5. fifth condenser; 6. first gas-liquid separator; 7. first filter; 8. first storage tank; 9. second liquid outlet pump; 10. first cooler; 11. second storage tank; 12. first vacuum pump; 13. second vacuum pump; 14. second condenser; 15. second gas-liquid separator; 16. third condenser; 17. fourth condenser; 18. third gas-liquid separator; 19. third storage tank; 20. first liquid outlet pump; 21. second cooler; 22. first cooling fan; 23. fourth storage tank. DETAILED DESCRIPTION
[0017] The utility model discloses a wharf oil and gas recovery device. The specific implementation manner of the utility model is further described below in conjunction with a preferred embodiment.
[0018] See attached figure Figure 1-4 , Figure 1 It is a structural schematic diagram of a preferred embodiment provided by the utility model. Figure 2 This is a schematic diagram of the structure of the first storage tank 8 of the preferred embodiment provided by the utility model. Figure 3 1 is a schematic diagram of the structure of the second storage tank 11 of the preferred embodiment provided by the utility model. Figure 4 It is a structural schematic diagram of the first adsorption bed 1 of the preferred embodiment provided by the utility model.
[0019] Preferred embodiments.
[0020] The present embodiment provides a wharf oil and gas recovery device, including a first condenser 4, a first filter 7, a first gas-liquid separator 6, a first adsorption bed 1, a first exhaust fan, a first cooler 10, a first storage tank 8, a second storage tank 11, a first vacuum pump 12, a second condenser 14, a second gas-liquid separator 15, a third condenser 16, a third gas-liquid separator 18 and a third storage tank 19, wherein a first inlet end of the first condenser 4 is connected to a ship loading waste gas source, a first outlet end of the first condenser 4 is connected to a first inlet end of the first gas-liquid separator 6, a first outlet end of the first gas-liquid separator 6 is connected to a first inlet end of the first storage tank 8, a second outlet end of the first gas-liquid separator 6 is connected to a first inlet end of the first filter 7, a first outlet end of the first filter 7 is connected to a first inlet and outlet of the first adsorption bed 1, a second inlet and outlet of the first adsorption bed 1 is connected to a first inlet end of the first exhaust fan, a first inlet end of the first cooler 10 is connected to a first inlet end of the first filter 7, The first inlet and outlet of the first adsorption bed 1 are connected, the first outlet end of the first cooler 10 is connected to the first inlet end of the second storage tank 11, the first outlet end of the second storage tank 11 is connected to the first inlet end of the first vacuum pump 12, the first outlet end of the first vacuum pump 12 is connected to the first inlet end of the second condenser 14, the first outlet end of the second condenser 14 is connected to the first inlet end of the second gas-liquid separator 15, the first outlet end of the second gas-liquid separator 15 is connected to the first inlet end of the third storage tank 19, the second outlet end of the second gas-liquid separator 15 is connected to the first inlet end of the third condenser 16, the first outlet end of the third condenser 16 is connected to the first inlet end of the third gas-liquid separator 18, the first outlet end of the third gas-liquid separator 18 is connected to the second inlet end of the third storage tank 19, and the second outlet end of the third gas-liquid separator 18 is connected to the first inlet and outlet of the first adsorption bed 1.
[0021] Furthermore, the wharf oil and gas recovery device includes a fourth storage tank 23, a first liquid outlet pump 20 and a second liquid outlet pump 9, the first inlet end of the fourth storage tank 23 is connected to the second outlet end of the first vacuum pump 12, the first outlet end of the fourth storage tank 23 and the first outlet end of the third storage tank 19 are both connected to the first inlet end of the first liquid outlet pump 20, the first outlet end of the first liquid outlet pump 20 is connected to the second inlet end of the first storage tank 8, and the first inlet end of the second liquid outlet pump 9 is connected to the first outlet end of the first storage tank 8.
[0022] Furthermore, the wharf oil and gas recovery device includes a second cooler 21 and a first cooling fan 22, the first inlet end of the second cooler 21 is connected to the first inlet and outlet of the first adsorption bed 1, the first outlet end of the second cooler 21 is connected to the first inlet end of the first cooling fan 22, and the first outlet end of the first cooling fan 22 is connected to the second inlet and outlet of the first adsorption bed 1.
[0023] Furthermore, the wharf oil and gas recovery device includes a second adsorption bed 2 and a third adsorption bed 3, the first inlet and outlet of the first adsorption bed 1, the first inlet and outlet of the second adsorption bed 2 and the first inlet and outlet of the third adsorption bed 3 are all connected to the second outlet end of the third gas-liquid separator 18, and the second inlet and outlet of the second adsorption bed 2 and the second inlet and outlet of the third adsorption bed 3 are both connected to the second inlet and outlet of the first adsorption bed 1.
[0024] Furthermore, the wharf oil and gas recovery device includes a second vacuum pump 13, a fourth condenser 17 and a fifth condenser 5, the first inlet end of the second vacuum pump 13 is connected to the first inlet end of the first vacuum pump 12, the first outlet end of the second vacuum pump 13 is connected to the first outlet end of the first vacuum pump 12, the first inlet end of the fourth condenser 17 is connected to the first inlet end of the third condenser 16, the first outlet end of the fourth condenser 17 is connected to the first outlet end of the third condenser 16, the first inlet end of the fifth condenser 5 is connected to the first inlet end of the first condenser 4, and the first outlet end of the fifth condenser 5 is connected to the first outlet end of the first condenser 4.
[0025] Working principle: The shipping waste gas passes through the dock and enters the first condenser 4 or the fifth condenser 5 for condensation treatment, and then is separated by the first gas-liquid separator 6. The liquid substance enters the first storage tank 8, and the gaseous substance enters the first adsorption bed 1, the second adsorption bed 2 and the third adsorption bed 3. The first adsorption bed 1, the second adsorption bed 2 and the third adsorption bed 3 adsorb the waste gas, and the gas enters the first cooler 10 again. After cooling, it enters the second storage tank 11, and is pumped into the second condenser 14 through the first vacuum pump 12 or the second vacuum pump 13. After condensation by the second condenser 14, it enters the second gas-liquid separator 15 for separation, and the liquid substance enters the third storage tank 19. The gaseous substance enters the third condenser 16 or the fourth condenser 17, and enters the third gas-liquid separator 18 after condensation treatment. The liquid substance enters the third storage tank 19, and the gaseous substance enters the first adsorption bed 1, the second adsorption bed 2 and the third adsorption bed 3 for further adsorption. The process is repeated to completely recover the oil and gas. The oil and gas in the second storage tank 11, the third storage tank 19 and the fourth storage tank 23 are all pumped into the first storage tank 8 through the first liquid outlet pump 20, and then the recovered liquid is processed uniformly through the first storage tank 8 and the second liquid outlet pump 9.
[0026] Among them, the first condenser 4, the third condenser 16 and the fourth condenser 17 are connected to chilled brine, and the second cooler 21, the first adsorption bed 1, the second adsorption bed 2, the third adsorption bed 3, the first cooler 10, the first vacuum pump 12, the second vacuum pump 13 and the second condenser 14 are all connected to circulating cooling water to ensure condensation and cooling effects.
[0027] It is worth mentioning that the technical features such as the storage tank involved in this utility model patent application should be regarded as the prior art. The specific structure, working principle and possible control method and spatial layout method of these technical features can be selected by conventional methods in the field, and should not be regarded as the utility model point of this utility model patent. This utility model patent will not be further elaborated.
[0028] For those skilled in the art, it is still possible to modify the technical solutions described in the aforementioned embodiments, or to make equivalent substitutions for some of the technical features therein. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present utility model should be included in the protection scope of the present utility model.
Claims
1. A wharf oil and gas recovery device, characterized in that: The invention comprises a first condenser (4), a first filter (7), a first gas-liquid separator (6), a first adsorption bed (1), a first exhaust fan, a first cooler (10), a first storage tank (8), a second storage tank (11), a first vacuum pump (12), a second condenser (14), a second gas-liquid separator (15), a third condenser (16), a third gas-liquid separator (18) and a third storage tank (19), wherein the first inlet end of the first condenser (4) is connected to a ship loading waste gas source, the first outlet end of the first condenser (4) is connected to the first inlet end of the first gas-liquid separator (6), the first outlet end of the first gas-liquid separator (6) is connected to the first inlet end of the first storage tank (8), the second outlet end of the first gas-liquid separator (6) is connected to the first inlet end of the first filter (7), the first outlet end of the first filter (7) is connected to the first inlet and outlet of the first adsorption bed (1), the second inlet and outlet of the first adsorption bed (1) is connected to the first inlet end of the first exhaust fan, the first inlet end of the first cooler (10) is connected to the first adsorption bed (1), and the second inlet and outlet of the first adsorption bed (1) is connected to the first inlet end of the first exhaust fan. The first inlet and outlet of the adsorption bed (1) are connected, the first outlet end of the first cooler (10) is connected to the first inlet end of the second storage tank (11), the first outlet end of the second storage tank (11) is connected to the first inlet end of the first vacuum pump (12), the first outlet end of the first vacuum pump (12) is connected to the first inlet end of the second condenser (14), the first outlet end of the second condenser (14) is connected to the first inlet end of the second gas-liquid separator (15), the first outlet end of the second gas-liquid separator (15) is connected to the first inlet end of the third storage tank (19), the second outlet end of the second gas-liquid separator (15) is connected to the first inlet end of the third condenser (16), the first outlet end of the third condenser (16) is connected to the first inlet end of the third gas-liquid separator (18), the first outlet end of the third gas-liquid separator (18) is connected to the second inlet end of the third storage tank (19), and the second outlet end of the third gas-liquid separator (18) is connected to the first inlet and outlet of the first adsorption bed (1).
2. The wharf oil and gas recovery device according to claim 1, characterized in that: The wharf oil and gas recovery device comprises a fourth storage tank (23), a first liquid outlet pump (20) and a second liquid outlet pump (9); the first inlet end of the fourth storage tank (23) is connected to the second outlet end of the first vacuum pump (12); the first outlet end of the fourth storage tank (23) and the first outlet end of the third storage tank (19) are both connected to the first inlet end of the first liquid outlet pump (20); the first outlet end of the first liquid outlet pump (20) is connected to the second inlet end of the first storage tank (8); and the first inlet end of the second liquid outlet pump (9) is connected to the first outlet end of the first storage tank (8).
3. The wharf oil and gas recovery device according to claim 2, characterized in that: The wharf oil and gas recovery device comprises a second cooler (21) and a first cooling fan (22); the first inlet end of the second cooler (21) is connected to the first inlet and outlet of the first adsorption bed (1); the first outlet end of the second cooler (21) is connected to the first inlet end of the first cooling fan (22); and the first outlet end of the first cooling fan (22) is connected to the second inlet and outlet of the first adsorption bed (1).
4. The wharf oil and gas recovery device according to claim 3, characterized in that: The wharf oil and gas recovery device comprises a second adsorption bed (2) and a third adsorption bed (3); a first inlet and outlet of the first adsorption bed (1), a first inlet and outlet of the second adsorption bed (2) and a first inlet and outlet of the third adsorption bed (3) are all connected to a second outlet end of the third gas-liquid separator (18); a second inlet and outlet of the second adsorption bed (2) and a second inlet and outlet of the third adsorption bed (3) are both connected to a second inlet and outlet of the first adsorption bed (1).
5. The wharf oil and gas recovery device according to claim 4, characterized in that: The wharf oil and gas recovery device comprises a second vacuum pump (13), a fourth condenser (17) and a fifth condenser (5), wherein a first inlet end of the second vacuum pump (13) is connected to a first inlet end of the first vacuum pump (12), a first outlet end of the second vacuum pump (13) is connected to a first outlet end of the first vacuum pump (12), a first inlet end of the fourth condenser (17) is connected to a first inlet end of the third condenser (16), a first outlet end of the fourth condenser (17) is connected to a first outlet end of the third condenser (16), a first inlet end of the fifth condenser (5) is connected to a first inlet end of the first condenser (4), and a first outlet end of the fifth condenser (5) is connected to a first outlet end of the first condenser (4).