CN112604384A - Gas-liquid separation equipment with high separation speed - Google Patents
Gas-liquid separation equipment with high separation speed Download PDFInfo
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- CN112604384A CN112604384A CN202011385246.7A CN202011385246A CN112604384A CN 112604384 A CN112604384 A CN 112604384A CN 202011385246 A CN202011385246 A CN 202011385246A CN 112604384 A CN112604384 A CN 112604384A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
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- Chemical Kinetics & Catalysis (AREA)
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- Oil, Petroleum & Natural Gas (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses gas-liquid separation equipment with high separation speed, relates to the technical field of gas-liquid separation, and aims to solve the problem of low separation efficiency caused by slow gas-liquid separation of the conventional gas-liquid separation equipment. The lower extreme four corners of casing all is provided with the bottom sprag seat, the both sides of casing are provided with inlet pipe, first blast pipe respectively, the inside of casing is provided with gas-liquid separation board device, every the inside of gas-liquid separation board device all is provided with condensing equipment, every the inside gravity gas-liquid separation pipe that all is provided with of lower extreme of gas-liquid separation board device, every the inner wall top of gravity gas-liquid separation pipe all is provided with gas collecting pipe, every the below of gravity gas-liquid separation pipe all is provided with gas-liquid propelling movement pipe, every the inside of gas-liquid propelling movement pipe all is provided with the fan, the below of gas-liquid separation board device is provided with the catch tray, the lower extreme of catch tray is provided with the liquid collecting pipe, the below of inlet pipe is.
Description
Technical Field
The invention relates to the technical field of gas-liquid separation, in particular to gas-liquid separation equipment with high separation speed.
Background
The gas-liquid separator can be arranged at the inlet and outlet of the gas compressor for gas-liquid separation, gas phase demisting after the condensation cooler on the top of the fractionating tower, and gas phase demisting of various gas washing towers, absorption towers and desorption towers. The gas-liquid separator can also be applied to various industrial and civil occasions such as gas dust removal, oil-water separation, liquid impurity removal and the like. Because the specific gravity of the gas is different from that of the liquid, when the liquid flows together with the gas, the liquid is subjected to a larger action of gravity to generate a downward speed, and the gas still flows towards the original direction, namely the liquid and the gas have a tendency to separate in a gravity field, and the downward liquid is attached to the wall surface, gathered together and discharged through a discharge pipe. Because of the different specific gravity of gas and liquid, when the liquid and gas are mixed and flow together, if the liquid and gas meet the barrier, the gas can be baffled and moved away, and the liquid can continuously have a forward speed due to inertia, and the forward liquid is adhered to the barrier wall surface, and is downward converged together due to the action of gravity, and is discharged through a discharge pipe.
However, the existing gas-liquid separation equipment has the problem of low separation efficiency because the gas-liquid separation is slow; therefore, the existing requirements are not met, and a gas-liquid separation device with high separation speed is provided for the requirements.
Disclosure of Invention
The invention aims to provide a gas-liquid separation device with high separation speed so as to solve the problems in the background technology.
In order to achieve the purpose, the invention provides the following technical scheme: a gas-liquid separation device with high separation speed comprises a shell, wherein bottom supporting seats are arranged at four corners of the lower end of the shell and are connected with flanges, a feed pipe and a first exhaust pipe are respectively arranged at two sides of the shell and are connected with the flanges of the feed pipe and the first exhaust pipe, a gas-liquid separation plate device is arranged in the shell and is welded with the inner wall of the shell, a condensing device is arranged in each gas-liquid separation plate device and is connected with the inner wall of the gas-liquid separation plate device through bolts, a gravity gas-liquid separation pipe is arranged in the lower end of each gas-liquid separation plate device and is welded with the gas-liquid separation plate device, a gas collecting pipe is arranged above the inner wall of each gravity gas-liquid separation pipe and is welded with the gas-liquid separation plate device, every the below of gravity gas-liquid separation pipe all is provided with the gas-liquid propelling movement pipe, and gas-liquid propelling movement pipe and gas-liquid separation board device inner wall welded connection, every the inside of gas-liquid propelling movement pipe all is provided with the fan, and fan and gas-liquid propelling movement inside pipe wall welded connection, the below of gas-liquid separation board device is provided with the collecting tray, and collecting tray and shells inner wall welded connection, the lower extreme of collecting tray is provided with the liquid collecting pipe, and liquid collecting pipe and collecting tray welded connection, the below of inlet pipe is provided with the coolant circulating pump, and coolant circulating pump and shells outer wall bolted connection, the outer wall of coolant circulating pump is provided with the fin, and fin and coolant circulating pump welded connection.
Preferably, every condensing equipment's lower extreme all is provided with condensation heat conduction board, and condensation heat conduction board and condensing equipment welded connection, condensation heat conduction board's outer wall is provided with the condenser pipe, and condenser pipe and condensing equipment pipe connection.
Preferably, each condensing device is provided with a condensing heat pipe and a condensing cold pipe, the condensing heat pipe and the condensing cold pipe are connected with the condensing device through pipelines, and the condensing heat pipe and the condensing cold pipe are connected with the cooling liquid circulating pump through the pipelines in a flange manner.
Preferably, both sides of each fan are provided with a liquid drop attachment net, and the liquid drop attachment nets are connected with the gas-liquid pushing pipe in a welding mode.
Preferably, the upper end of the gas collecting pipe is provided with a second exhaust pipe, the second exhaust pipe is connected with the gas collecting pipe through a flange, the upper end of the second exhaust pipe is provided with a second exhaust pipe electromagnetic valve, and the second exhaust pipe electromagnetic valve is connected with the second exhaust pipe through a flange.
Preferably, one side of the second exhaust pipe is provided with a return pipe, the return pipe is connected with a flange of the second exhaust pipe, one end of the return pipe is connected with a flange of the inlet pipe, a return pipe electromagnetic valve is arranged on the return pipe, and the return pipe electromagnetic valve is connected with a flange of the return pipe.
Preferably, the second exhaust pipe is provided with a gas-liquid hygrometer, and the gas-liquid hygrometer is connected with the second exhaust pipe through a flange.
Preferably, a liquid collecting pipe electromagnetic valve is arranged on the liquid collecting pipe, and the liquid collecting pipe electromagnetic valve is connected with the liquid collecting pipe through a flange.
Compared with the prior art, the invention has the beneficial effects that:
1. according to the invention, through the arrangement of the gas-liquid separation plate device, the gas-liquid mixture firstly enters the inner wall of the shell from the feeding pipe, then the gas-liquid mixture meets the gas-liquid separation plate device, the condensing device in the gas-liquid separation plate device continuously cools the surface of the gas-liquid separation plate device contacted with the condensing device, water vapor is condensed into water drops on the surface of the gas-liquid separation plate device when meeting the surface of the low-temperature gas-liquid separation plate device, the water drops on the surface of the gas-liquid separation plate device slide along the surface of the gas-liquid separation plate device and fall into the liquid collecting tray for collection, when the other part of the non-liquefied gas-liquid mixture passes through the gravity gas-liquid separation pipe, the gas can move upwards from the inside of the gas collecting pipe due to the difference of gravity specific gravity of the gas and the liquid can slide along the inner wall of the gravity gas, the gas-liquid separation device is blown out by the fan, gas-liquid separation is carried out on the second gas-liquid separation plate device according to the process, finally separated gas is respectively led out by the second exhaust pipe and the first exhaust pipe on the gas collecting pipe, and collected liquid is collected by the liquid collecting disc and led out by the liquid collecting pipe.
2. Through the second blast pipe, the second blast pipe solenoid valve, the gas-liquid hygrometer, the back flow, the setting of back flow solenoid valve, after the gas of separation gets into the second blast pipe from the gas collecting pipe, the gas-liquid mixture proportion in the gas-liquid hygrometer real-time supervision second blast pipe, after liquid content reaches the separation standard, the back flow solenoid valve is closed and the second blast pipe solenoid valve is opened and is derived gas, if not up to standard, then close the second blast pipe solenoid valve and open the back flow solenoid valve, make the gas-liquid mixture body carry out gas-liquid separation work again, gas-liquid separation's efficiency and separation degree have greatly been improved.
3. Through the setting of condensing equipment, coolant liquid circulating pump, the coolant liquid circulating pump is with the condensation heat conduction board under the inside coolant liquid pump income condensing equipment, and the low temperature condenser pipe absorbs the heat on the condensation heat conduction board and makes gas-liquid separation board device reduction problem do benefit to the liquefied steam, and the fin of coolant liquid circulating pump outer wall has greatly improved the heat dissipation of its inside coolant liquid and has handled.
Drawings
FIG. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a schematic view of the gas-liquid separation plate apparatus of the present invention;
FIG. 3 is an enlarged view of a portion of the present invention at A;
FIG. 4 is an enlarged view of a portion of the present invention at B;
FIG. 5 is an enlarged view of a portion of the present invention at C;
in the figure: 1. a housing; 2. a bottom support seat; 3. a feed pipe; 4. a first exhaust pipe; 5. a gas-liquid separation plate device; 6. a condensing unit; 7. a gravity gas-liquid separation tube; 8. a gas collection tube; 9. a gas-liquid pushing pipe; 10. a fan; 11. a liquid collecting tray; 12. a liquid collection tube; 13. a coolant circulation pump; 14. a liquid collecting pipe electromagnetic valve; 15. a condensation heat transfer plate; 16. a condenser tube; 17. condensing the heat pipe; 18. condensing the cold pipe; 19. a droplet deposition network; 20. a second exhaust pipe; 21. a second exhaust pipe solenoid valve; 22. a gas-liquid hygrometer; 23. a return pipe; 24. a return pipe solenoid valve; 25. and a heat sink.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments.
Referring to fig. 1-5, an embodiment of the present invention is shown: a gas-liquid separation device with high separation speed comprises a shell 1, wherein bottom supporting seats 2 are arranged at four corners of the lower end of the shell 1, the bottom supporting seats 2 are connected with flanges, a feeding pipe 3 and a first exhaust pipe 4 are respectively arranged at two sides of the shell 1, the feeding pipe 3 and the first exhaust pipe 4 are connected with the shell 1 through flanges, a gas-liquid separation plate device 5 is arranged inside the shell 1, the gas-liquid separation plate device 5 is connected with the inner wall of the shell 1 in a welded mode, a condensing device 6 is arranged inside each gas-liquid separation plate device 5, the condensing device 6 is connected with the inner wall of the gas-liquid separation plate device 5 through bolts, a gravity gas-liquid separation pipe 7 is arranged inside the lower end of each gas-liquid separation plate device 5, the gravity gas-liquid separation pipe 7 is connected with the gas-liquid separation plate device 5 in a welded mode, and a gas collecting pipe 8 is, and the gas collecting pipe 8 is welded with the gas-liquid separating plate device 5, a gas-liquid propelling pipe 9 is arranged below each gravity gas-liquid separating pipe 7, the gas-liquid pushing pipes 9 are welded with the inner wall of the gas-liquid separation plate device 5, a fan 10 is arranged inside each gas-liquid pushing pipe 9, and the fan 10 is welded with the inner wall of the gas-liquid pushing pipe 9, a liquid collecting tray 11 is arranged below the gas-liquid separation plate device 5, and the liquid collecting tray 11 is welded with the inner wall of the shell 1, the lower end of the liquid collecting tray 11 is provided with a liquid collecting pipe 12, and the liquid collecting pipe 12 is welded with the liquid collecting tray 11, a cooling liquid circulating pump 13 is arranged below the feeding pipe 3, and the cooling liquid circulating pump 13 is connected with the outer wall of the shell 1 through bolts, the outer wall of the cooling liquid circulating pump 13 is provided with radiating fins 25, and the radiating fins 25 are welded with the cooling liquid circulating pump 13.
Further, every condensing equipment 6's lower extreme all is provided with condensation heat conduction board 15, and condensation heat conduction board 15 and condensing equipment 6 welded connection, condensation heat conduction board 15's outer wall is provided with condenser pipe 16, and condenser pipe 16 and 6 pipe connection of condensing equipment, and condenser pipe 16 absorbs the heat on the condensation heat conduction board 15 to make gas-liquid separation board device 5 cool down.
Further, every all be provided with condensation heat pipe 17, cold pipe 18 on the condensing equipment 6, condensation heat pipe 17, cold pipe 18 and 6 pipe connection of condensing equipment, and condensation heat pipe 17, cold pipe 18 and coolant liquid circulating pump 13 pipe flange joint, condensation heat pipe 17, cold pipe 18 with condensing equipment 6 and 13 pipe connection of coolant liquid circulating pump for the transmission coolant liquid.
Furthermore, both sides of each fan 10 are provided with a liquid drop attachment net 19, the liquid drop attachment nets 19 are connected with the gas-liquid propelling pipe 9 in a welding mode, and the liquid drop attachment nets 19 enable fine suspended water drops passing through the gas-liquid propelling pipe 9 to be attached when contacting the liquid drop attachment nets 19, so that gas-liquid separation is achieved.
Further, the upper end of the gas collecting pipe 8 is provided with a second exhaust pipe 20, the second exhaust pipe 20 is in flange connection with the gas collecting pipe 8, the upper end of the second exhaust pipe 20 is provided with a second exhaust pipe electromagnetic valve 21, the second exhaust pipe electromagnetic valve 21 is in flange connection with the second exhaust pipe 20, and the second exhaust pipe electromagnetic valve 21 is closed to achieve communication of the return pipe 23, so that the gas-liquid mixture which is not completely separated is separated again.
Further, one side of the second exhaust pipe 20 is provided with a return pipe 23, the return pipe 23 is in flange connection with the second exhaust pipe 20, one end of the return pipe 23 is in flange connection with the inlet pipe 3, the return pipe 23 is provided with a return pipe electromagnetic valve 24, the return pipe electromagnetic valve 24 is in flange connection with the return pipe 23, and the gas-liquid mixture which is not completely separated passes through the return pipe 23 and enters the device again for re-separation.
Further, a gas-liquid hygrometer 22 is disposed on the second exhaust pipe 20, the gas-liquid hygrometer 22 is connected to the second exhaust pipe 20 through a flange, and the gas-liquid hygrometer 22 is used for monitoring a gas-liquid separation state in the second exhaust pipe 20 in real time.
Further, a liquid collecting pipe electromagnetic valve 14 is arranged on the liquid collecting pipe 12, the liquid collecting pipe electromagnetic valve 14 is in flange connection with the liquid collecting pipe 12, and the liquid collecting pipe electromagnetic valve 14 is used for controlling the communication of the liquid collecting pipe 12 so as to lead out the collected liquid.
The working principle is as follows: when the device is used, a gas-liquid mixture firstly enters the inner wall of the shell 1 from the feeding pipe 3, then the gas-liquid mixture meets the gas-liquid separation plate device 5, the condensing device 6 in the gas-liquid separation plate device 5 continuously cools the surface of the gas-liquid separation plate device 5 contacted with the condensing device, the cooling liquid circulating pump 13 pumps the internal cooling liquid into the condensation heat conduction plate 15 under the condensing device 6, the low-temperature condensing pipe 16 absorbs the heat on the condensation heat conduction plate 15 to reduce the problem of the gas-liquid separation plate device 5 and facilitate the liquefied water vapor, the radiating fins 25 on the outer wall of the cooling liquid circulating pump 13 greatly improve the radiating treatment of the internal cooling liquid, the water vapor meets the surface of the low-temperature gas-liquid separation plate device 5 and can be condensed into water drops to be attached to the surface of the gas-liquid separation plate device 5, and then the water drops on the surface of, when the other part of the non-liquefied water-vapor mixture passes through the gravity gas-liquid separation pipe 7, because of different gravity of gas and liquid, the gas moves upwards from the inside of the gas collection pipe 8, the liquid slides down along the inner wall of the gravity gas-liquid separation pipe 7 due to inertia and finally falls into the liquid collection tray 11 for collection, the excess water-vapor mixture is sucked from the gas-liquid propelling pipe 9 and blown out by the fan 10, and gas-liquid separation is performed on the second gas-liquid separation plate device 5 according to the process, the finally separated gas is respectively led out by the second exhaust pipe 20 and the first exhaust pipe 4 on the gas collection pipe 8, the collected liquid is collected by the liquid collection tray 11 and led out through the liquid collection pipe 12, the device greatly improves the gas-liquid separation rate, reduces the volume occupation of the device, and after the separated gas enters the second exhaust pipe 20 from the gas collection pipe 8, the gas-liquid hygrometer 22 monitors the gas-liquid mixture proportion in the second exhaust pipe 20 in real time, and when the liquid content reaches the separation standard, the return pipe solenoid valve 24 is closed and the second exhaust pipe solenoid valve 21 is opened to lead out gas, and if the liquid content does not reach the separation standard, the second exhaust pipe solenoid valve 21 is closed and the return pipe solenoid valve 24 is opened, so that the gas-liquid mixture body performs gas-liquid separation again, and the gas-liquid separation efficiency and the separation degree are greatly improved.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Claims (8)
1. The utility model provides a gas-liquid separation equipment that separating speed is fast, includes casing (1), its characterized in that: the lower end four corners of the shell (1) are respectively provided with a bottom supporting seat (2), the bottom supporting seats (2) are connected with flanges, the two sides of the shell (1) are respectively provided with a feeding pipe (3) and a first exhaust pipe (4), the feeding pipe (3) and the first exhaust pipe (4) are connected with the shell (1) by flanges, the shell (1) is internally provided with a gas-liquid separation plate device (5), the gas-liquid separation plate device (5) is welded with the inner wall of the shell (1), the inside of each gas-liquid separation plate device (5) is provided with a condensing device (6), the condensing device (6) is connected with the inner wall of the gas-liquid separation plate device (5) through bolts, the inside of the lower end of each gas-liquid separation plate device (5) is provided with a gravity gas-liquid separation pipe (7), and the gravity gas-liquid separation pipe (7) is welded with the gas-, a gas collecting pipe (8) is arranged above the inner wall of each gravity gas-liquid separation pipe (7), the gas collecting pipe (8) is connected with a gas-liquid separation plate device (5) in a welded mode, a gas-liquid pushing pipe (9) is arranged below each gravity gas-liquid separation pipe (7), the gas-liquid pushing pipe (9) is connected with the inner wall of the gas-liquid separation plate device (5) in a welded mode, a fan (10) is arranged inside each gas-liquid pushing pipe (9), the fan (10) is connected with the inner wall of the gas-liquid pushing pipe (9) in a welded mode, a liquid collecting disc (11) is arranged below the gas-liquid separation plate device (5), the liquid collecting disc (11) is connected with the inner wall of the shell (1) in a welded mode, a liquid collecting pipe (12) is arranged at the lower end of the liquid collecting disc (11), the liquid collecting pipe (12) is connected with the liquid collecting disc (11) in a welded mode, and a, and the cooling liquid circulating pump (13) is connected with the outer wall of the shell (1) through bolts, the outer wall of the cooling liquid circulating pump (13) is provided with radiating fins (25), and the radiating fins (25) are welded with the cooling liquid circulating pump (13).
2. The gas-liquid separation apparatus with a high separation speed according to claim 1, characterized in that: every the lower extreme of condensing equipment (6) all is provided with condensation heat conduction board (15), and condensation heat conduction board (15) and condensing equipment (6) welded connection, the outer wall of condensation heat conduction board (15) is provided with condenser pipe (16), and condenser pipe (16) and condensing equipment (6) pipe connection.
3. The gas-liquid separation apparatus with a high separation speed according to claim 1, characterized in that: every all be provided with condensing heat pipe (17), cold condenser pipe (18) on condensing equipment (6), condensing heat pipe (17), cold condenser pipe (18) and condensing equipment (6) pipe connection, and condensing heat pipe (17), cold condenser pipe (18) and coolant liquid circulating pump (13) pipe flange joint.
4. The gas-liquid separation apparatus with a high separation speed according to claim 1, characterized in that: and both sides of each fan (10) are provided with liquid drop attaching nets (19), and the liquid drop attaching nets (19) are connected with the gas-liquid pushing pipe (9) in a welding mode.
5. The gas-liquid separation apparatus with a high separation speed according to claim 1, characterized in that: the upper end of the gas collecting pipe (8) is provided with a second exhaust pipe (20), the second exhaust pipe (20) is connected with the gas collecting pipe (8) in a flange mode, the upper end of the second exhaust pipe (20) is provided with a second exhaust pipe electromagnetic valve (21), and the second exhaust pipe electromagnetic valve (21) is connected with the second exhaust pipe (20) in a flange mode.
6. The gas-liquid separation apparatus with a high separation speed according to claim 5, wherein: one side of second blast pipe (20) is provided with back flow pipe (23), back flow pipe (23) and second blast pipe (20) flange joint, and the one end and inlet pipe (3) flange joint of back flow pipe (23), be provided with back flow solenoid valve (24) on back flow pipe (23), and back flow solenoid valve (24) and back flow pipe (23) flange joint.
7. The gas-liquid separation apparatus with a high separation speed according to claim 5, wherein: and a gas-liquid hygrometer (22) is arranged on the second exhaust pipe (20), and the gas-liquid hygrometer (22) is connected with the second exhaust pipe (20) through a flange.
8. The gas-liquid separation apparatus with a high separation speed according to claim 1, characterized in that: the liquid collecting pipe (12) is provided with a liquid collecting pipe electromagnetic valve (14), and the liquid collecting pipe electromagnetic valve (14) is connected with the liquid collecting pipe (12) in a flange mode.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011385246.7A CN112604384A (en) | 2020-12-01 | 2020-12-01 | Gas-liquid separation equipment with high separation speed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011385246.7A CN112604384A (en) | 2020-12-01 | 2020-12-01 | Gas-liquid separation equipment with high separation speed |
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| Publication Number | Publication Date |
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| CN112604384A true CN112604384A (en) | 2021-04-06 |
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| CN202011385246.7A Pending CN112604384A (en) | 2020-12-01 | 2020-12-01 | Gas-liquid separation equipment with high separation speed |
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| TW200624025A (en) * | 2004-12-31 | 2006-07-01 | Foxconn Tech Co Ltd | Liquid cooling device |
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| CN104353260A (en) * | 2014-11-06 | 2015-02-18 | 北京林业大学 | Composite condensation device used in vehicle-mounted biomass thermal cracking equipment |
| CN205287992U (en) * | 2016-01-07 | 2016-06-08 | 江苏托球农化股份有限公司 | Gas and liquid separator |
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| CN108807313A (en) * | 2018-07-05 | 2018-11-13 | 安康学院 | A kind of heat dissipation from microelectronic devices device |
| CN208952289U (en) * | 2018-09-06 | 2019-06-07 | 许海梅 | A kind of environmental protecting device applied to building cooling |
| CN210949013U (en) * | 2019-07-11 | 2020-07-07 | 江苏大象机械有限公司 | Cooling and lubricating device of slurry pump |
| CN111981882A (en) * | 2020-08-20 | 2020-11-24 | 华北电力大学 | Discontinuous phase separation loop heat pipe |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2089233A (en) * | 1980-12-11 | 1982-06-23 | Champion Spark Plug Co | Spray booth apparatus |
| US20030221815A1 (en) * | 2002-06-03 | 2003-12-04 | Chin-Wen Wang | Hydronic pump type heat radiator |
| TW200624025A (en) * | 2004-12-31 | 2006-07-01 | Foxconn Tech Co Ltd | Liquid cooling device |
| CN201163626Y (en) * | 2008-01-11 | 2008-12-10 | 林于纮 | Chip fast-cooling device |
| CN104353260A (en) * | 2014-11-06 | 2015-02-18 | 北京林业大学 | Composite condensation device used in vehicle-mounted biomass thermal cracking equipment |
| CN205287992U (en) * | 2016-01-07 | 2016-06-08 | 江苏托球农化股份有限公司 | Gas and liquid separator |
| CN106288257A (en) * | 2016-10-30 | 2017-01-04 | 苏州市克拉思科文化传播有限公司 | A kind of high efficiency smart cleaning system |
| CN108807313A (en) * | 2018-07-05 | 2018-11-13 | 安康学院 | A kind of heat dissipation from microelectronic devices device |
| CN208952289U (en) * | 2018-09-06 | 2019-06-07 | 许海梅 | A kind of environmental protecting device applied to building cooling |
| CN210949013U (en) * | 2019-07-11 | 2020-07-07 | 江苏大象机械有限公司 | Cooling and lubricating device of slurry pump |
| CN111981882A (en) * | 2020-08-20 | 2020-11-24 | 华北电力大学 | Discontinuous phase separation loop heat pipe |
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