CN110145758B - Liquid fuel puffing fission device system for refrigeration and fuel gas - Google Patents
Liquid fuel puffing fission device system for refrigeration and fuel gas Download PDFInfo
- Publication number
- CN110145758B CN110145758B CN201910245390.1A CN201910245390A CN110145758B CN 110145758 B CN110145758 B CN 110145758B CN 201910245390 A CN201910245390 A CN 201910245390A CN 110145758 B CN110145758 B CN 110145758B
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- fission
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- 239000007788 liquid Substances 0.000 title claims abstract description 109
- 239000000446 fuel Substances 0.000 title claims abstract description 62
- 230000004992 fission Effects 0.000 title claims abstract description 46
- 239000002737 fuel gas Substances 0.000 title claims abstract description 11
- 238000005057 refrigeration Methods 0.000 title claims abstract description 10
- 230000001007 puffing effect Effects 0.000 title abstract description 6
- 239000007789 gas Substances 0.000 claims abstract description 88
- 238000000926 separation method Methods 0.000 claims abstract description 45
- 238000002309 gasification Methods 0.000 claims abstract description 30
- 239000002828 fuel tank Substances 0.000 claims abstract description 17
- 230000001105 regulatory effect Effects 0.000 claims abstract description 8
- 238000011084 recovery Methods 0.000 claims abstract description 6
- 238000001816 cooling Methods 0.000 claims description 31
- 210000000078 claw Anatomy 0.000 claims description 25
- 239000007921 spray Substances 0.000 claims description 17
- 238000007789 sealing Methods 0.000 claims description 13
- 230000000712 assembly Effects 0.000 claims description 5
- 238000000429 assembly Methods 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 abstract description 6
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 24
- 239000003921 oil Substances 0.000 description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000003245 coal Substances 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000002283 diesel fuel Substances 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000010742 number 1 fuel oil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
- F23K5/02—Liquid fuel
- F23K5/14—Details thereof
- F23K5/22—Vaporising devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24C—DOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
- F24C15/00—Details
- F24C15/10—Tops, e.g. hot plates; Rings
- F24C15/107—Pan supports or grates therefor
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24C—DOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
- F24C3/00—Stoves or ranges for gaseous fuels
- F24C3/08—Arrangement or mounting of burners
- F24C3/085—Arrangement or mounting of burners on ranges
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2300/00—Pretreatment and supply of liquid fuel
- F23K2300/20—Supply line arrangements
- F23K2300/205—Vaporising
Abstract
The invention belongs to the technical field of combustion devices, and particularly relates to a liquid fuel puffing fission device system for refrigeration and fuel gas, which comprises a fission gasification terminal, a gasification base station, a gas furnace and an exhaust device; the fission gasification terminal comprises a fission tube and a resonance box; 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 gas stove comprises a gas stove panel and a burner, wherein the burner is arranged on the gas stove panel and comprises a furnace chamber, a furnace end and an ignition needle, the furnace end and the ignition needle are arranged at the bottom of the furnace chamber, the furnace end is communicated with an outlet of a flow regulating pump, and an adjustable pot frame is arranged on the gas panel. The body fuel tank realizes the recovery of the fuel at the outlet of the gasification terminal and the stable storage of the liquid fuel; the oil storage device is provided with the breather valve, so that the stability in the oil storage device is ensured. The fission gas-liquid conversion system provided by the invention has the advantages of simple structure, stable operation and low energy consumption.
Description
Technical Field
The invention belongs to the technical field of combustion devices, and particularly relates to a liquid fuel puffing fission device system for refrigeration and fuel gas.
Background
In the face of exhaustion of fossil energy, alternative energy sources to fossil energy are actively sought. Many boiler research institutions at home and abroad aim at clean and cheap alternative fuels such as natural gas, methanol, electricity and the like. Alcohol-based fuel is the most potential novel alternative energy source, and is fuel prepared by taking alcohols (such as methanol, ethanol, butanol and the like) as main substances. It is in liquid or solid form. It is also a biomass energy, which is the same as nuclear energy, solar energy, wind energy, and hydraulic energy. The molecular formula of the methanol is single compared with that of coal, gasoline and diesel oil, the combustion emission is very clean, and no particulate matters (PM 2.5 and PM 10), ozone, sulfur dioxide, CO, mercury and compounds thereof are contained, 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. Especially lean oil, less gas and more coal are the main characteristics of the energy structure in the present stage of China, so that methanol is an important derivative product of coal chemical industry and is one of the currently recognized alternative fuels with great prospect. The liquid methanol has high combustion energy consumption as fuel, needs to be preheated and has insufficient combustion; the burning energy consumption of the gaseous methanol as the fuel is relatively low, the burning is more sufficient, the promotion value is realized, but carbon is easy to accumulate; atomized methanol has less carbon deposition, but has high energy consumption.
Disclosure of Invention
In view of the above technical problems, the present invention provides a liquid fuel expansion fission reactor system for cooling and burning gas, which processes liquid fuel by high-speed collision, resonance of a resonance tank and a fission tube, and supplies the fuel to a gas furnace and cooling.
In order to solve the technical problems, the invention adopts the following technical scheme:
a liquid fuel puffing fission device system for refrigeration and fuel gas comprises a fission gasification terminal, a gasification base station, a gas furnace and an exhaust device;
the fission gasification terminal comprises a fission tube and a resonance box; the two ends of the fission tube body are respectively provided with a first port and a second port; the first port is fixedly connected with a high-pressure spray head, a nozzle of the high-pressure spray head is arranged in a tube body of the fission tube, the other end of the high-pressure spray head is communicated with an inlet tube, the high-pressure spray head sprays a plurality of high-speed jet flows, the inlet tube comprises a gas inlet tube and a liquid inlet tube, the gas inlet tube is used for introducing high-pressure air, the liquid inlet tube is used for introducing liquid fuel, a booster pump is arranged on the liquid inlet tube, and a mixing cavity is arranged between the inlet tube and the nozzle; the second port is fixedly connected with an outlet pipe, the outlet pipe is a T-shaped pipe, the cross arm is a gas outlet pipe, the vertical arm 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 resonant tank body, 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, an exhaust 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 outlet pipe; the high-pressure spray head is connected with the first port in a sealing way; the outlet pipe is connected with the second port in a sealing way; the resonance box is connected with the fission tube in a sealing way; 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;
the gas stove comprises a gas stove panel and a burner, wherein the burner is arranged on the gas stove panel and comprises a furnace chamber, a furnace end and an ignition needle, the furnace end and the ignition needle are arranged at the bottom of the furnace chamber, the furnace end is communicated with an outlet of a flow regulating pump, and an adjustable pot rack is arranged on the gas stove panel;
the exhaust device comprises a hollow exhaust box, an exhaust duct is arranged in the hollow exhaust box, an air inlet and an air outlet are arranged on the hollow exhaust box, and the air inlet is communicated with the cooling pipe.
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; the gas-liquid separation device is internally provided with a gas-liquid separation pipe, 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, a fuel liquid outlet pipe is arranged at the lowest part of the inclined plane, and a one-way valve is arranged on the fuel liquid outlet pipe; a cooling jacket is arranged outside the liquid fuel tank and is connected with a cooling pipe outlet; the oil storage device is provided with a breather valve.
The adjustable pot rack comprises a bottom ring and a pot claw assembly, wherein at least three pot claw assemblies are arranged, each pot claw assembly comprises a connecting block and a pot claw, each pot claw is hinged to each connecting block, a limiting block is arranged on each connecting block, the rotating angle of each pot claw is limited through each limiting block, and each connecting block is detachably connected with the bottom ring.
The connecting block is inserted with the bottom ring, and corresponding slots are arranged on the connecting block.
At least two slots are arranged on the connecting block.
The connecting block is provided with a threaded hole which penetrates through the slot.
And a wind shield is arranged at the air outlet.
Compared with the prior art, the invention has the beneficial effects that:
the invention provides a liquid fuel puffing fission device system for refrigeration and fuel gas, which is characterized in that liquid fuel is sprayed into a fission tube through high-speed atomization flow by high-pressure air, and is continuously collided with the inner wall of the fission tube and collided with each high-speed atomization flow to form gas fuel, and then is output through an outlet tube for use; the resonance of the process of impacting the fission tube by the high-pressure gas in the resonance box and the liquid fuel in the fission tube is realized through the resonance box, so that the gasification of the liquid fuel is enhanced; the outlet pipe adopts a T-shaped pipe, and large fog drops carried in the gas fuel flow fall into the liquid outlet for recovery under the action of gravity; the method comprises the steps of absorbing a large amount of heat in the fuel liquid gasification process, introducing cooling gas into a cooling jacket of a liquid fuel tank through a cooling pipe, improving the separation efficiency of liquid fuel and gas in an oil-gas separation device, reducing the gasification of the liquid fuel in an oil storage device, and ensuring the stability of a system; the liquid fuel tank realizes the recovery of the fuel at the outlet of the gasification terminal and the stable storage of the liquid fuel; the oil storage device is provided with the breather valve, so that the stability in the oil storage device is ensured. The fission gas-liquid conversion system provided by the invention has the advantages of simple structure, stable operation and low energy consumption.
Drawings
FIG. 1 is a schematic diagram of the present invention;
FIG. 2 is a schematic view of the overall structure of the gas burner of the present invention;
FIG. 3 is a schematic view of the structure of the adjustable pot holder of the present invention;
FIG. 4 is a schematic view of a threaded bore of the present invention;
FIG. 5 is a schematic view of the use of the adjustable pot holder of the present invention;
FIG. 6 is a schematic view of the structure of the arcuate support ring of the present invention;
FIG. 7 is a schematic diagram of a slot according to the present invention;
FIG. 8 is a schematic view of the structure of the exhaust device of the present invention;
FIG. 9 is a schematic view of the split structure of the exhaust device of the present invention;
FIG. 10 is a schematic view of the structure of a wind deflector of the present invention;
description of the embodiments
The following description of the embodiments of the present invention will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
As shown in fig. 1, a liquid fuel expansion fischerer system for cooling and burning gas comprises a fissile gasification terminal, a gasification base station, a gas furnace and an exhaust device;
the fission gasification terminal comprises a fission tube 1 and a resonance box 7; the two ends of the tube body of the fission tube 1 are respectively provided with a first port 2 and a second port 3; the first port 2 is fixedly connected with a high-pressure spray head 4, a nozzle of the high-pressure spray head 4 is arranged in the pipe body of the fission pipe 1, the other end of the high-pressure spray head 4 is communicated with an inlet pipe 5, the high-pressure spray head 4 sprays a plurality of high-speed jet flows, the high-speed jet flows directly irradiate the inner wall of the pipe body of the fission pipe 1 after being reflected and continuously collide with the inner wall of the pipe body of the fission pipe 1 and the high-speed jet flows crossed with the inner wall of the pipe body of the fission pipe 1 at a high speed to form tiny particles, and the tiny particles are discharged out of the fission pipe 1 under the action of high-pressure air. The inlet pipe 5 comprises a gas inlet pipe 501 and a liquid inlet pipe 502, wherein the gas inlet pipe 501 is used for introducing high-pressure air, the liquid inlet pipe 502 is used for introducing liquid fuel, a pressurizing pump 503 is arranged on the liquid inlet pipe 502, and a mixing cavity is arranged between the inlet pipe 5 and the nozzle; the second port 3 is fixedly connected with an outlet pipe 6, the outlet pipe 6 is a T-shaped pipe, the cross arm is a gas outlet pipe 601, the vertical arm 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 7 is nested outside the fission tube 1, a constant pressure valve 8, a high pressure air inlet 9 and a cooling tube 10 are arranged on the box body of the resonance box 7, high pressure air is filled in the box body of the resonance box, and the high pressure air inlet 9 is used for introducing high pressure air; the cooling pipe 10 penetrates through the box body of the resonance box 7, normal-temperature air is introduced into the cooling pipe 10, and low-temperature air is output by the cooling pipe 10;
specific: the gas inlet pipe is filled with high-pressure air, and the liquid inlet pipe is filled with liquid fuel; the inlet pressure of the liquid fuel is regulated to be 0.1MPa, the flow rate is 500 milliliters/hour, the inlet pressure of the high-pressure air is 2-6MPa, the flow rate is 4-10 m/s, the liquid fuel and the gas fuel are introduced, the high-pressure air is filled into the resonance box through the high-pressure air inlet until the fuel gas is discharged from the outlet pipe of the fission tube, the high-pressure air is stopped being filled into the resonance box, and the constant pressure valve constant pressure is set.
The gasification base station comprises a liquid fuel tank and an air compressor 11, wherein the liquid fuel tank comprises an oil-gas separation device 12 and an oil storage device 13; the oil-gas separation device 12 is used for separating liquid fuel and gas in the gasification terminal outlet pipe 6; the oil-gas separation device is connected with a liquid outlet pipe 602 of the outlet pipe 6, an exhaust gas outlet pipe 121 is arranged on the upper side of the oil-gas separation device 12, a fuel liquid outlet pipe 122 is arranged on the lower side of the oil-gas separation device 12, and the oil-gas separation device 12 is communicated with the oil storage device 13 through the fuel liquid outlet pipe 122; the oil storage device 13 is used for storing liquid fuel; the lower side of the oil storage device 13 is connected with a gasification terminal liquid inlet pipe 502; the air compressor 11 is used for providing compressed air, and is connected with the gasification terminal gas outlet pipe 501;
the gas furnace comprises a gas stove panel 41 and a burner 411, the burner 411 is arranged on the gas stove panel 41, the burner 411 comprises a furnace chamber 4111, a furnace end 4112 and an ignition needle 4113, the furnace end 4112 and the ignition needle 4113 are arranged at the bottom of the furnace chamber 4111, and the furnace end 4112 is communicated with an outlet of a flow regulating pump 603 to provide fuel for combustion. An adjustable pot rack 42 is arranged on the gas stove panel 1. The cavity 4111 is a ring-shaped sealing structure.
As shown in fig. 8 to 10, the exhaust device 701 includes a hollow exhaust box 7011, an exhaust duct 7012 is disposed in the hollow exhaust box 7011, an air inlet 7013 and an air outlet 7014 are disposed on the hollow exhaust box 7011, and the air inlet 7013 is communicated with the outlet end of the cooling tube 10. The low-temperature air output by the cooling pipe 10 enters the hollow exhaust box through the air inlet 7013, is split by the exhaust duct, and is finally exhausted through the exhaust outlet 7014. Further, a wind deflector 7015 is provided at the exhaust port 7014.
In this embodiment, the high pressure nozzle 4 is connected with the first port 2 in a sealing manner; the outlet pipe 6 is connected with the second port 3 in a sealing way; the resonance box 7 is connected with the fission tube 1 in a sealing way; the cooling pipes 10 are respectively connected with the resonance box 7 in a sealing way at the outer walls of the two ends in the resonance box 7.
In the present embodiment, the liquid fuel tank is an integrated device, the oil-gas separation device 12 is disposed above the oil storage device 13, and the oil-gas separation device 12 communicates with the oil storage device 13 through the fuel liquid outlet pipe 122. The gas-liquid separation device 12 is internally provided with a gas-liquid separation pipe 14, the gas-liquid separation pipe 14 is a coiled pipe, the tail end of the gas-liquid separation pipe 14 is an exhaust gas outlet pipe 121, and the lowest end of the gas-liquid separation pipe 14 is provided with a one-way valve; the bottom of the oil-gas separation device 12 is an inclined plane, a fuel liquid outlet pipe 122 is arranged at the lowest part of the inclined plane, and a one-way valve is arranged on the fuel liquid outlet pipe 122. A cooling jacket 15 is arranged outside the liquid fuel tank, and the cooling jacket 15 is connected with the outlet of the cooling pipe 10. The oil reservoir 13 is provided with a breather valve 16.
As shown in fig. 2 to 7, the adjustable pot rack 42 is placed on the gas range panel 41, and the adjustable pot rack 42 includes a bottom ring 43 and a plurality of pot claw assemblies 44, and the number of the pot claw assemblies 44 can be set according to the actual situation, and at least three pot claw assemblies are provided.
The pan claw assembly 44 comprises a connecting block 45 and a pan claw 46, one end of the pan claw 46 is hinged with the connecting block 45, a limiting block 47 is arranged on the connecting block 45, the rotating angle of the pan claw 46 is limited through the limiting block 47, and the connecting block 45 is detachably connected with the bottom ring 43. The limiting blocks 47 can be arranged in one, preferably two; when one is provided, the angle at which the claws 46 are closed can be limited; when two are provided, the angle of the closing and opening of the pan claw 46 can be limited.
When the cookers with smaller bottom areas such as a medicine pot, a milk pot and the like are needed, the cookers 46 can be rotated inwards, so that the distance between the cookers 46 is reduced, and the cookers with smaller bottom areas can be well supported. Conversely, when a pan with a larger bottom area, such as a frying pan, a steaming pan, etc., is placed, each of the pan claws 46 can be rotated outwards, so that the distance between the pan claws 46 is increased, and the pan with a larger bottom area can be supported.
Further, the bottom of the connecting block 45 is provided with a corresponding slot 48, and is spliced with the bottom ring 43 through the slot 48; since the bottom ring 43 is a circular ring structure, the slots are also correspondingly arcuate.
Further, at least two slots 48 are provided on the connection block 45. A plurality of slots 48 are provided, and the corresponding slots 48 can be selected as desired to fine tune the position between the connection block 45 and the bottom ring 43.
Further, in order to secure the fastening of the coupling, the connection block 45 is provided with a screw hole 49, and the screw hole 49 passes through the insertion slot 48. After the connecting block 45 is inserted into the bottom ring 43 through the slot 48, a bolt is screwed in the threaded hole 49, and the bolt passes through the slot 48 to prop against the bottom ring 43, so that the fixing function is further realized.
Further, the stopper 47 is preferably wedge-shaped.
Further, the pan claw 46 is provided with an arc-shaped support ring 410. When the pan claw 46 is closed, the contact area between the pan claw and the pan can be increased through the arc-shaped supporting ring 410, so that the pan can be stably placed.
The preferred embodiments of the present invention have been described in detail, but the present invention is not limited to the above embodiments, and various changes can be made within the knowledge of those skilled in the art without departing from the spirit of the present invention, and the various changes are included in the scope of the present invention.
Claims (4)
1. A liquid fuel expansion fission reactor system for refrigeration and fuel gas, characterized by: comprises a fission gasification terminal, a gasification base station, a gas furnace and an exhaust device;
the fission gasification terminal comprises a fission tube and a resonance box; the two ends of the fission tube body are respectively provided with a first port and a second port; the first port is fixedly connected with a high-pressure spray head, a nozzle of the high-pressure spray head is arranged in a tube body of the fission tube, the other end of the high-pressure spray head is communicated with an inlet tube, the high-pressure spray head sprays a plurality of high-speed jet flows, the inlet tube comprises a gas inlet tube and a liquid inlet tube, the gas inlet tube is used for introducing high-pressure air, the liquid inlet tube is used for introducing liquid fuel, a booster pump is arranged on the liquid inlet tube, and a mixing cavity is arranged between the inlet tube and the nozzle; the second port is fixedly connected with an outlet pipe, the outlet pipe is a T-shaped pipe, the cross arm is a gas outlet pipe, the vertical arm 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 resonant tank body, 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, an exhaust 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 outlet pipe; the high-pressure spray head is connected with the first port in a sealing way; the outlet pipe is connected with the second port in a sealing way; the resonance box is connected with the fission tube in a sealing way; 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;
the gas stove comprises a gas stove panel and a burner, wherein the burner is arranged on the gas stove panel and comprises a furnace chamber, a furnace end and an ignition needle, the furnace end and the ignition needle are arranged at the bottom of the furnace chamber, the furnace end is communicated with an outlet of a flow regulating pump, and an adjustable pot rack is arranged on the gas stove panel;
the air exhaust device comprises a hollow air exhaust box, an air exhaust channel is arranged in the hollow air exhaust box, an air inlet and an air outlet are formed in the hollow air exhaust box, and the air inlet is communicated with the cooling pipe;
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; the gas-liquid separation device is internally provided with a gas-liquid separation pipe, 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, a fuel liquid outlet pipe is arranged at the lowest part of the inclined plane, and a one-way valve is arranged on the fuel liquid outlet pipe; a cooling jacket is arranged outside the liquid fuel tank and is connected with a cooling pipe outlet; a breather valve is arranged on the oil storage device;
the adjustable pot rack comprises a bottom ring and at least three pot claw assemblies, wherein each pot claw assembly comprises a connecting block and a pot claw, each pot claw is hinged with the corresponding connecting block, a limiting block is arranged on each connecting block, the rotating angle of each pot claw is limited by the corresponding limiting block, and each connecting block is detachably connected with the bottom ring; and a wind shield is arranged at the air outlet.
2. A liquid fuel expansion fission system for refrigeration and fuel gas according to claim 1 and wherein: the connecting block is inserted with the bottom ring, and corresponding slots are arranged on the connecting block.
3. A liquid fuel expansion fission system for refrigeration and fuel gas according to claim 1 and wherein: at least two slots are arranged on the connecting block.
4. A liquid fuel expansion fission system for refrigeration and fuel gas according to claim 1 and wherein: the connecting block is provided with a threaded hole which penetrates through the slot.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910245390.1A CN110145758B (en) | 2019-03-28 | 2019-03-28 | Liquid fuel puffing fission device system for refrigeration and fuel gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910245390.1A CN110145758B (en) | 2019-03-28 | 2019-03-28 | Liquid fuel puffing fission device system for refrigeration and fuel gas |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110145758A CN110145758A (en) | 2019-08-20 |
| CN110145758B true CN110145758B (en) | 2023-11-14 |
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ID=67588846
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910245390.1A Active CN110145758B (en) | 2019-03-28 | 2019-03-28 | Liquid fuel puffing fission device system for refrigeration and fuel gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110145758B (en) |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
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