CN210545162U - Liquid fuel puffing fission gas-liquid conversion system - Google Patents
Liquid fuel puffing fission gas-liquid conversion system Download PDFInfo
- Publication number
- CN210545162U CN210545162U CN201920409140.2U CN201920409140U CN210545162U CN 210545162 U CN210545162 U CN 210545162U CN 201920409140 U CN201920409140 U CN 201920409140U CN 210545162 U CN210545162 U CN 210545162U
- Authority
- CN
- China
- Prior art keywords
- liquid
- gas
- pipe
- fission
- liquid fuel
- 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 - Fee Related
Links
Images
Landscapes
- Separation By Low-Temperature Treatments (AREA)
Abstract
The utility model relates to a liquid fuel handles technical field, more specifically relates to a popped fission gas-liquid conversion system of liquid fuel, sprays liquid fuel into the fission pipe through high-speed atomizing stream form through high-pressure gas, constantly collides and each high-speed collision that atomizes of fission pipe inner wall, after forming gas fuel, exports through the outlet pipe and uses; the resonance of the high-pressure gas in the resonance box and the process of impact of the gasification of the liquid fuel in the fission tube on the fission tube is realized through the resonance box, and the gasification of the liquid fuel is enhanced; the fuel liquid absorbs a large amount of heat in the gasification process, and the cooling gas is introduced into the cooling jacket of the liquid fuel tank through the cooling pipe, so that the separation efficiency of the liquid fuel and the gas in the oil-gas separation device is improved, the gasification of the liquid fuel in the oil storage device is reduced, and the stability of the system is ensured. The fission gas-liquid conversion system provided by the utility model has the advantages of simple structure, stable operation and less energy consumption.
Description
Technical Field
The utility model relates to a liquid fuel handles technical field, more specifically relates to a popped fission gas-liquid conversion system of liquid fuel.
Background
In the face of the exhaustion of petrochemical energy, people actively seek for alternative energy of fossil energy, and the national government vigorously pushes an energy diversification strategy. Many boiler research institutions at home and abroad aim at clean and cheap alternative fuels, such as natural gas, methanol, electricity and the like. The alcohol-based fuel is the most potential novel alternative energy, and is the fuel mainly prepared from alcohols (such as methanol, ethanol, butanol and the like). It is in liquid or solid form. It is also a biomass energy, and is the same as nuclear energy, solar energy, wind energy and hydraulic energy, and is an environment-friendly clean energy which is widely popularized by governments in various countries at present; is very popular with the enterprise organizations of various countries. The methanol has a single molecular formula compared with coal, gasoline and diesel oil, the combustion emission of the methanol is very clean, no particulate matters (PM2.5, PM10), ozone, sulfur dioxide, CO, mercury and compounds thereof exist, and the emission of nitrogen oxides is more than 10 times lower than that of a natural gas boiler. The methanol fuel can replace coal and diesel oil, and can greatly relieve the air pollution which is difficult to bypass China. Especially lean oil, less gas and more coal are the main characteristics of the energy structure at the present stage in China, so that methanol is one of the accepted alternative fuels with great prospect at present as an important derivative product in the coal chemical industry. The liquid methanol as fuel has high combustion energy consumption, needs preheating and is not fully combusted; gaseous methanol as fuel has relatively low combustion energy consumption, more complete combustion and popularization value, but is easy to deposit carbon; the atomized methanol has less carbon deposition but high energy consumption.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a popped fission gas-liquid conversion system of liquid fuel handles liquid fuel through the resonance of high-speed collision, resonance case and fission pipe, prepares the fuel stable, that the energy consumption is low, be difficult for the carbon deposit.
In order to achieve the above purpose, the utility model provides a technical scheme does:
a liquid fuel puffing fission gas-liquid conversion system comprises a fission gasification terminal and a gasification base station;
the fission gasification terminal includes a fission tube and a resonance box; the fission pipe is internally provided with a high-pressure spray nozzle, an inlet pipe and an outlet pipe, and the two ends of the fission pipe are respectively provided with a first port and a second port; the first port is fixedly connected with a high-pressure sprayer, the high-pressure sprayer comprises a mixing cavity and a nozzle, and the mixing cavity is communicated with the nozzle; the nozzle comprises a jet cavity and a jet hole, the jet cavity is hemispherical, and the jet cavity is communicated with the fission tube through the jet hole; the rear end of the high-pressure nozzle mixing cavity is communicated with an inlet pipe, the inlet pipe comprises a gas inlet pipe and a liquid inlet pipe, and a pressure pump is arranged on the liquid inlet pipe; the second port is fixedly connected with an outlet pipe, the outlet pipe is a T-shaped pipe, the transverse pipe is a gas outlet pipe, the vertical pipe below the transverse pipe is a liquid outlet pipe, the gas outlet pipe is communicated with the liquid outlet pipe, the gas outlet pipe is provided with a flow regulating pump, and the liquid outlet pipe is provided with a recovery pump; the resonance box is nested outside the fission tube, a constant pressure valve, a high-pressure air inlet and a cooling tube are arranged on the box body of the resonance box, high-pressure air is filled in the box body of the resonance box, and the high-pressure air inlet is used for introducing high-pressure air; the cooling pipe penetrates through the box body of the resonance box, normal-temperature air is introduced into the cooling pipe, and low-temperature air is output by the cooling pipe;
the gasification base station comprises a liquid fuel tank and an air compressor, wherein the liquid fuel tank comprises an oil-gas separation device and an oil storage device; the oil-gas separation device is used for separating liquid fuel and gas in an outlet pipe of the gasification terminal; the oil-gas separation device is connected with a liquid outlet pipe of the outlet pipe, a waste gas outlet pipe is arranged on the upper side of the oil-gas separation device, a fuel liquid outlet pipe is arranged on the lower side of the oil-gas separation device, and the oil-gas separation device is communicated with the oil storage device through the fuel liquid outlet pipe; the oil storage device is used for storing liquid fuel; the lower side of the oil storage device is connected with a gasification terminal liquid inlet pipe; the air compressor machine is used for providing compressed air, the air compressor machine is connected gasification terminal gas inlet pipe.
Further, the high-pressure spray head is connected with the first port in a sealing mode; the outlet pipe is connected with the second port in a sealing way; the resonance box is hermetically connected with the fission tube; the outer walls of the two ends of the cooling pipe in the resonance box are respectively connected with the resonance box in a sealing way.
Further, the fission tube body length/length to diameter ratio is 40: 2-40: 6.
further, the liquid outlet tube of the outlet tube is at a distance of 1-4mm from the fission tube.
Further, the liquid fuel tank is an integrated device, the oil-gas separation device is arranged above the oil storage device, and the oil-gas separation device is communicated with the oil storage device through a fuel liquid outlet pipe.
Further, a gas-liquid separation pipe is arranged in the oil-gas separation device, the gas-liquid separation pipe is a coiled pipe, the tail end of the gas-liquid separation pipe is a gas outlet, and the lowest end of the gas-liquid separation pipe is provided with a one-way valve; the bottom of the oil-gas separation device is an inclined plane, the lowest part of the inclined plane is provided with a fuel liquid outlet pipe, and the fuel liquid outlet pipe is provided with a one-way valve.
Further, a cooling jacket is arranged outside the liquid fuel tank and connected with an outlet of the cooling pipe.
Further, a breather valve is arranged on the oil storage device.
Further, high-pressure air is introduced into a gas inlet pipe of the liquid fuel puffing fission device, and liquid fuel is introduced into a liquid inlet pipe; the inlet pressure of the liquid fuel is 0.1MPa, and the flow rate is 500 ml/h; the pressure of a high-pressure air inlet is 2-6MPa, and the flow speed is 4-10 m/s; liquid fuel and high-pressure air are sprayed with a plurality of high-speed jet flows through a high-pressure nozzle in the liquid fuel swelling and cracking device, the high-speed jet flows directly to the inner wall of the tube body of the cracking tube, after being reflected, the high-speed jet flows continuously collide with the inner wall of the tube body of the cracking tube and the high-speed jet flows crossed with the inner wall of the tube body of the cracking tube at a high speed, the tube body of the cracking tube forms resonance with high-pressure air wrapped outside the tube body of the cracking tube, and energy is transmitted to the high-speed jet flows; the liquid fuel is expanded and cracked by the fission pipe and then is discharged through the outlet pipe, and is separated into gas and liquid in the outlet pipe, and the gas can be directly used as fuel.
Further, the liquid fuel adopts methanol, and the purity of the methanol is more than 92%.
Compared with the prior art, the utility model discloses the beneficial effect who has does:
the utility model provides a liquid fuel swelling fission gas-liquid conversion system, which sprays liquid fuel into a fission pipe in a high-speed atomization flow mode through high-pressure gas, continuously collides with the inner wall of the fission pipe and collides with each high-speed atomization flow to form gas fuel, and then outputs and uses the gas fuel through an outlet pipe; the resonance of the high-pressure gas in the resonance box and the process of impact of the gasification of the liquid fuel in the fission tube on the fission tube is realized through the resonance box, and the gasification of the liquid fuel is enhanced; the outlet pipe adopts a T-shaped pipe, and the large fog drops carried in the gas fuel flow fall into a liquid outlet for recovery under the action of gravity; the fuel liquid absorbs a large amount of heat in the gasification process, and the cooling gas is introduced into a cooling jacket of the liquid fuel tank through a cooling pipe, so that the separation efficiency of the liquid fuel and the gas in the oil-gas separation device is improved, the gasification of the liquid fuel in the oil storage device is reduced, and the stability of the system is ensured; the liquid fuel tank realizes the recovery of the fuel at the outlet of the gasification terminal and simultaneously realizes the stable storage of the liquid fuel; the oil storage device is provided with the breather valve, so that the internal stability of the oil storage device is ensured. The fission gas-liquid conversion system provided by the utility model has the advantages of simple structure, stable operation and less energy consumption.
Drawings
Fig. 1 is a schematic view of a liquid fuel puffing fission gas-liquid conversion system provided by the present invention;
fig. 2 is a cross-sectional view of a high pressure showerhead.
In the figure, 1 is a fission tube, 2 is a first port, and 3 is a second port; 4 is a high-pressure nozzle, 5 is an inlet pipe, 501 is a gas inlet pipe, 502 is a liquid inlet pipe, 503 is a pressure pump, 6 is an outlet pipe, 601 is a gas outlet pipe, 602 is a liquid outlet pipe, 603 is a flow regulating pump, 604 is a recovery pump, 7 is a mixing chamber, 8 is an injection chamber, 9 is an injection hole, 10 is a resonance box, 11 is a constant pressure valve, 12 is a high-pressure gas inlet, 13 is a cooling pipe, 14 is an air compressor, 15 is an oil-gas separation device, 151 is an exhaust gas outlet pipe, 152 is a fuel liquid outlet pipe, 16 is an oil storage device, 17 is a gas-liquid separation pipe, 18 is a cooling jacket, and 19 is a breather valve.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
As shown in fig. 1-2, a liquid fuel swelling fission gas-liquid conversion system comprises a fission gasification terminal and a gasification base station;
the fission gasification terminal includes a fission tube 1 and a resonance box 10; a high-pressure spray nozzle 4, an inlet pipe 5 and an outlet pipe 6 are arranged in the fission pipe 1, and a first port 2 and a second port 3 are respectively arranged at two ends of the fission pipe 1; the first port 2 is fixedly connected with a high-pressure sprayer 4, the high-pressure sprayer comprises a mixing cavity 7 and a nozzle, and the mixing cavity 7 is communicated with the nozzle; the nozzle comprises a spray cavity 8 and a spray hole 9, the spray cavity 8 is hemispherical, and the spray cavity 8 is communicated with the fission tube 1 through the spray hole 9; the rear end of a mixing cavity 7 of the high-pressure nozzle 4 is communicated with an inlet pipe 5, the inlet pipe 5 comprises a gas inlet pipe 501 and a liquid inlet pipe 502, and a pressure pump 503 is arranged on the liquid inlet pipe 501; the second port 3 is fixedly connected with an outlet pipe 6, the outlet pipe 6 is a T-shaped pipe, a transverse pipe is a gas outlet pipe 601, a vertical pipe below the transverse pipe is a liquid outlet pipe 602, the gas outlet pipe 601 is communicated with the liquid outlet pipe 602, a flow regulating pump 603 is arranged on the gas outlet pipe 601, and a recovery pump 604 is arranged on the liquid outlet pipe 602; the resonance box 10 is nested outside the fission tube 1, a constant pressure valve 11, a high-pressure air inlet 12 and a cooling tube 13 are arranged on the box body of the resonance box 10, high-pressure air is filled in the box body of the resonance box 10, and the high-pressure air inlet 12 is used for introducing high-pressure air; the cooling pipe 13 penetrates through the box body of the resonance box 10, normal-temperature air is introduced into the cooling pipe 13, and low-temperature air is output from the cooling pipe 13;
the gasification base station comprises a liquid fuel tank and an air compressor 14, wherein the liquid fuel tank comprises an oil-gas separation device 15 and an oil storage device 16; the oil-gas separation device 15 is used for recovering liquid in the liquid outlet pipe 602; the oil-gas separation device 15 is connected with a liquid outlet pipe 602 of the outlet pipe 6, an exhaust gas outlet pipe 151 is arranged on the upper side of the oil-gas separation device 15, a fuel liquid outlet pipe 152 is arranged on the lower side of the oil-gas separation device 15, and the oil-gas separation device 15 is communicated with the oil storage device 16 through the fuel liquid outlet pipe 152; the oil storage device 16 is used for storing liquid fuel; the lower side of the oil storage device 16 is connected with a gasification terminal liquid inlet pipe 502; the air compressor 14 is used for providing compressed air, and the air compressor 14 is connected with a gasification terminal gas inlet pipe 501.
Further, the high-pressure nozzle 4 is hermetically connected with the first port 2; the outlet pipe 6 is connected with the second port 3 in a sealing way; the resonance box 10 is hermetically connected with the fission tube 1; the cooling pipes 13 are hermetically connected to the resonance box 10 at the outer walls of the two ends of the resonance box 10.
In this embodiment, the length/length to diameter ratio of the body of the fission tube 1 is 40: 2-40: 6, the liquid outlet pipe 602 of said outlet pipe 6 being at a distance of 1-4mm from the fission pipe.
Further, the liquid fuel tank is an integrated device, the oil-gas separation device 15 is arranged above the oil storage device 16, and the oil-gas separation device 15 is communicated with the oil storage device 16 through a fuel liquid outlet pipe 152.
Further, a gas-liquid separation pipe 17 is arranged in the oil-gas separation device 15, the gas-liquid separation pipe 17 is a coiled pipe, the tail end of the gas-liquid separation pipe 17 is a waste gas outlet pipe 151, and the lowest end of the gas-liquid separation pipe 17 is provided with a one-way valve; the bottom of the oil-gas separation device 15 is an inclined plane, the lowest part of the inclined plane is provided with a fuel liquid outlet pipe 152, and the fuel liquid outlet pipe 152 is provided with a one-way valve.
Further, a cooling jacket 18 is arranged outside the liquid fuel tank, and the cooling jacket 18 is connected with the outlet of the cooling pipe 13. The oil storage device is provided with a breather valve 19.
Further, high-pressure air is introduced into a gas inlet pipe of the liquid fuel puffing fission device, and liquid fuel is introduced into a liquid inlet pipe; adjusting the inlet pressure of the liquid fuel to 0.1MPa, the flow rate to 500 ml/h, the inlet pressure of the high-pressure air to 2-6MPa and the flow rate to 4-10 m/s, introducing the liquid fuel and the gas fuel, filling high-pressure air into the resonance box through the high-pressure air inlet until the fuel gas is discharged from the outlet pipe of the fission pipe, stopping filling the high-pressure air into the resonance box, and setting a constant pressure valve for constant pressure; liquid fuel and high-pressure air are sprayed with a plurality of high-speed jet flows through a high-pressure nozzle in the liquid fuel swelling and cracking device, the high-speed jet flows directly to the inner wall of the tube body of the cracking tube, after being reflected, the high-speed jet flows continuously collide with the inner wall of the tube body of the cracking tube and the high-speed jet flows crossed with the inner wall of the tube body of the cracking tube at a high speed, the tube body of the cracking tube forms resonance with high-pressure air wrapped outside the tube body of the cracking tube, and energy is transmitted to the high-speed jet flows; the liquid fuel is expanded and cracked by the fission pipe and then is discharged through the outlet pipe, and is separated into gas and liquid in the outlet pipe, and the gas can be directly used as fuel.
In the embodiment, the liquid fuel adopts methanol, and the purity of the methanol is more than 92%.
In the embodiment, when in implementation, the liquid fuel is pressurized to form a liquid flow, and then enters the high-pressure nozzle 4 through the liquid inlet pipe 502, the gas is pressurized to form a gas flow, and then enters the high-pressure nozzle through the gas inlet pipe 501, the liquid flow and the gas flow meet in the high-pressure nozzle 4 and are ejected through the high-pressure nozzle 4 to form a plurality of high-pressure jets to be ejected into the tube body of the fission tube 1, the high-pressure jets continuously collide and reflect on the inner wall of the tube body of the fission tube 1, and the high-pressure jets continuously collide with each other, at the same time, the high-pressure air distributed outside the tube body of the fission tube 1 resonates with the tube body of the fission tube 1, droplets of the liquid fuel are continuously broken and worn in the collision process (absorbing energy and heat, overcoming surface tension), the surface is promoted to be renewed, and the surface area of the droplets is increased until stable, and are discharged, the residual gas outputs fuel gas through the gas outlet 601, the fuel gas is high-pressure gas carrying fuel droplets with extremely small particle size, the storage is stable, the energy consumption is low in the using process, and carbon deposition is not easy to generate. The liquid fuel expansion process takes up heat from the surroundings continuously, and uses this heat absorption process for the production of cold gas, which is fed to the cooling jacket 18.
The above description has been made in detail only for the preferred embodiment of the present invention, but the present invention is not limited to the above embodiment, and various changes can be made without departing from the spirit of the present invention within the knowledge scope of those skilled in the art, and all such changes are intended to be encompassed by the present invention.
Claims (9)
1. The liquid fuel puffing fission gas-liquid conversion system is characterized in that: the system comprises a fission gasification terminal and a gasification base station;
the fission gasification terminal includes a fission tube and a resonance box; the fission pipe is internally provided with a high-pressure spray nozzle, an inlet pipe and an outlet pipe, and the two ends of the fission pipe are respectively provided with a first port and a second port; the first port is fixedly connected with a high-pressure sprayer, the high-pressure sprayer comprises a mixing cavity and a nozzle, and the mixing cavity is communicated with the nozzle; the nozzle comprises a jet cavity and a jet hole, the jet cavity is hemispherical, and the jet cavity is communicated with the fission tube through the jet hole; the rear end of the high-pressure nozzle mixing cavity is communicated with an inlet pipe, the inlet pipe comprises a gas inlet pipe and a liquid inlet pipe, and a pressure pump is arranged on the liquid inlet pipe; the second port is fixedly connected with an outlet pipe, the outlet pipe is a T-shaped pipe, the transverse pipe is a gas outlet pipe, the vertical pipe below the transverse pipe is a liquid outlet pipe, the gas outlet pipe is communicated with the liquid outlet pipe, the gas outlet pipe is provided with a flow regulating pump, and the liquid outlet pipe is provided with a recovery pump; the resonance box is nested outside the fission tube, a constant pressure valve, a high-pressure air inlet and a cooling tube are arranged on the box body of the resonance box, high-pressure air is filled in the box body of the resonance box, and the high-pressure air inlet is used for introducing high-pressure air; the cooling pipe penetrates through the box body of the resonance box, normal-temperature air is introduced into the cooling pipe, and low-temperature air is output by the cooling pipe;
the gasification base station comprises a liquid fuel tank and an air compressor, wherein the liquid fuel tank comprises an oil-gas separation device and an oil storage device; the oil-gas separation device is used for separating liquid fuel and gas in an outlet pipe of the gasification terminal; the oil-gas separation device is connected with a liquid outlet pipe of the outlet pipe, a waste gas outlet pipe is arranged on the upper side of the oil-gas separation device, a fuel liquid outlet pipe is arranged on the lower side of the oil-gas separation device, and the oil-gas separation device is communicated with the oil storage device through the fuel liquid outlet pipe; the oil storage device is used for storing liquid fuel; the lower side of the oil storage device is connected with a gasification terminal liquid inlet pipe; the air compressor is used for providing compressed air and is connected with a gasification terminal gas inlet pipe; the high-pressure spray head is hermetically connected with the first port; the outlet pipe is connected with the second port in a sealing way; the resonance box is hermetically connected with the fission tube; the outer walls of the two ends of the cooling pipe in the resonance box are respectively connected with the resonance box in a sealing way.
2. The liquid fuel expanded fission gas-liquid conversion system according to claim 1, wherein: the length-to-diameter ratio of the fission tube body is 40: 2-40: 6.
3. the liquid fuel expanded fission gas-liquid conversion system according to claim 1, wherein: the distance from the liquid outlet pipe of the outlet pipe to the fission pipe is 1-4 mm.
4. The liquid fuel expanded fission gas-liquid conversion system according to claim 1, wherein: the liquid fuel tank is an integrated device, the oil-gas separation device is arranged above the oil storage device, and the oil-gas separation device is communicated with the oil storage device through a fuel liquid outlet pipe.
5. The liquid fuel expanded fission gas-liquid conversion system according to claim 4, wherein: a gas-liquid separation pipe is arranged in the oil-gas separation device, the gas-liquid separation pipe is a coiled pipe, the tail end of the gas-liquid separation pipe is a gas outlet, and the lowest end of the gas-liquid separation pipe is provided with a one-way valve; the bottom of the oil-gas separation device is an inclined plane, the lowest part of the inclined plane is provided with a fuel liquid outlet pipe, and the fuel liquid outlet pipe is provided with a one-way valve.
6. The liquid fuel puffed fission gas-liquid conversion system according to claim 1 or 4, wherein: and a cooling jacket is arranged outside the liquid fuel tank and is connected with the outlet of the cooling pipe.
7. The liquid fuel puffed fission gas-liquid conversion system according to claim 1 or 4, wherein: and the oil storage device is provided with a breather valve.
8. The liquid fuel puffed fission gas-liquid conversion system according to claim 1 or 4, wherein: high-pressure air is introduced into the gas inlet pipe, the pressure of the high-pressure air inlet is 2-6MPa, and the flow speed is 4-10 m/s; liquid fuel is introduced into the liquid inlet pipe, the pressure of the liquid fuel inlet is 0.1MPa, and the flow rate is 500 ml/h; liquid fuel and high-pressure air are sprayed with a plurality of high-speed jet flows through a high-pressure nozzle in the liquid fuel swelling and cracking device, the high-speed jet flows directly to the inner wall of the tube body of the cracking tube, after being reflected, the high-speed jet flows continuously collide with the inner wall of the tube body of the cracking tube and the high-speed jet flows crossed with the inner wall of the tube body of the cracking tube at a high speed, the tube body of the cracking tube forms resonance with high-pressure air wrapped outside the tube body of the cracking tube, and energy is transmitted to the high-speed jet flows; the liquid fuel is expanded and cracked by the fission pipe and then is discharged through the outlet pipe, and is separated into gas and liquid in the outlet pipe, and the gas can be directly used as fuel.
9. The liquid fuel puffed fission gas-liquid conversion system according to claim 1 or 4, wherein: the liquid fuel adopts methanol, and the purity of the methanol is more than 92%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920409140.2U CN210545162U (en) | 2019-03-28 | 2019-03-28 | Liquid fuel puffing fission gas-liquid conversion system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920409140.2U CN210545162U (en) | 2019-03-28 | 2019-03-28 | Liquid fuel puffing fission gas-liquid conversion system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210545162U true CN210545162U (en) | 2020-05-19 |
Family
ID=70668636
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920409140.2U Expired - Fee Related CN210545162U (en) | 2019-03-28 | 2019-03-28 | Liquid fuel puffing fission gas-liquid conversion system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210545162U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110102243A (en) * | 2019-03-28 | 2019-08-09 | 万荣金坦能源科技有限公司 | A kind of liquid fuel extruding fission gas-liquid converting system and its method of fissioning |
-
2019
- 2019-03-28 CN CN201920409140.2U patent/CN210545162U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110102243A (en) * | 2019-03-28 | 2019-08-09 | 万荣金坦能源科技有限公司 | A kind of liquid fuel extruding fission gas-liquid converting system and its method of fissioning |
| CN110102243B (en) * | 2019-03-28 | 2023-05-23 | 万荣金坦能源科技有限公司 | Liquid fuel puffing fission gas-liquid conversion system and fission method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110102243B (en) | Liquid fuel puffing fission gas-liquid conversion system and fission method thereof | |
| CN210545162U (en) | Liquid fuel puffing fission gas-liquid conversion system | |
| CN210229979U (en) | Cryogenic liquid fuel puffing fission system | |
| CN210458076U (en) | Liquid fuel swelling fission terminal | |
| CN210237552U (en) | Liquid fuel puffing cracker capable of refrigerating | |
| CN210458077U (en) | Liquid fuel puffing fission device | |
| CN109855111B (en) | Gas system | |
| CN201535216U (en) | System for supplying fuel with nanometer bubbles for diesel engine | |
| CN109847686B (en) | Refrigerating liquid fuel puffing and fissioning system and method | |
| CN201487952U (en) | Combined low-energy-consumption multi-stage supersonic coal-water slurry atomizing nozzle | |
| CN211119465U (en) | Gas system | |
| CN211119466U (en) | Liquid fuel puffing splitter system for refrigeration and fuel gas | |
| CN210458075U (en) | Liquid fuel swelling fission device | |
| CN110105998B (en) | Liquid fuel puffing fission device and fission method thereof | |
| CN110105997B (en) | Liquid fuel puffing fission terminal and fission method thereof | |
| CN110105996B (en) | Liquid fuel puffing fission device capable of refrigerating and fission method thereof | |
| CN211420085U (en) | Liquid fuel puffing fission device system for heating | |
| CN210463078U (en) | Liquid fuel puffing fission device system for heating in winter and refrigerating in summer | |
| CN210001833U (en) | liquid fuel puffing and cracking device capable of refrigerating | |
| CN110105999B (en) | Liquid fuel puffing fission device capable of refrigerating and fission method | |
| CN109852447B (en) | Liquid fuel puffing fission device capable of refrigerating | |
| CN101660397A (en) | Gas generator for oil thermal production | |
| CN210449208U (en) | Liquid fuel puffing splitter system for heating and fuel gas | |
| CN110145758B (en) | Liquid fuel puffing fission device system for refrigeration and fuel gas | |
| CN210001832U (en) | liquid fuel puffing and cracking device capable of refrigerating |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200519 Termination date: 20210328 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |