CN110173714B - Liquid fuel puffing fission device system for heating in winter and refrigerating in summer - Google Patents
Liquid fuel puffing fission device system for heating in winter and refrigerating in summer Download PDFInfo
- Publication number
- CN110173714B CN110173714B CN201910244401.4A CN201910244401A CN110173714B CN 110173714 B CN110173714 B CN 110173714B CN 201910244401 A CN201910244401 A CN 201910244401A CN 110173714 B CN110173714 B CN 110173714B
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid
- outlet pipe
- pipe
- oil
- 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.)
- Active
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 111
- 239000000446 fuel Substances 0.000 title claims abstract description 62
- 230000004992 fission Effects 0.000 title claims abstract description 41
- 238000010438 heat treatment Methods 0.000 title claims abstract description 20
- 230000001007 puffing effect Effects 0.000 title abstract description 5
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 78
- 238000000926 separation method Methods 0.000 claims abstract description 45
- 238000002309 gasification Methods 0.000 claims abstract description 29
- 238000002485 combustion reaction Methods 0.000 claims abstract description 28
- 239000002828 fuel tank Substances 0.000 claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 230000001105 regulatory effect Effects 0.000 claims abstract description 8
- 238000001816 cooling Methods 0.000 claims description 34
- 239000007921 spray Substances 0.000 claims description 17
- 238000007789 sealing Methods 0.000 claims description 12
- 238000011084 recovery Methods 0.000 claims description 5
- 239000007789 gas Substances 0.000 abstract description 50
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 16
- 239000003345 natural gas Substances 0.000 abstract description 8
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 238000005057 refrigeration Methods 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-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
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000002283 diesel fuel 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
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 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
- 230000005611 electricity Effects 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000008236 heating water Substances 0.000 description 1
- 230000003116 impacting effect 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
- 239000010742 number 1 fuel oil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Classifications
-
- 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
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/10—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium
- F24H1/12—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium
- F24H1/124—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium using fluid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/0005—Details for water heaters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/06—Arrangement of mountings or supports for heaters, e.g. boilers, other than space heating radiators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/18—Arrangement or mounting of grates or heating means
- F24H9/1809—Arrangement or mounting of grates or heating means for water heaters
- F24H9/1832—Arrangement or mounting of combustion heating means, e.g. grates or burners
- F24H9/1836—Arrangement or mounting of combustion heating means, e.g. grates or burners using fluid fuel
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Feeding And Controlling Fuel (AREA)
Abstract
The invention relates to the technical field of heating and refrigeration, in particular to a liquid fuel puffing fission device system for heating in winter and refrigerating in summer, which comprises a fission gasification terminal, a gasification base station, a wall-mounted 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 hanging stove comprises a hanging stove body and a combustion chamber arranged in the hanging stove body, a heat exchanger is arranged in the combustion chamber, a methanol burning stove is arranged below the heat exchanger, water in the heat exchanger is heated through the methanol burning stove, a liquid inlet of the methanol burning stove is communicated with an outlet of a flow regulating pump, and a flue communicated with the combustion chamber is arranged on the hanging stove body. The fission gas-liquid conversion system provided by the invention has the advantages of simple structure, stable operation and low energy consumption. Methanol is used as fuel for heating, so that wall-hanging furnaces can be used for heating in special areas (without natural gas).
Description
Technical Field
The invention relates to the technical field of heating and refrigeration, in particular to a liquid fuel puffing fission device system for heating in winter and refrigerating in summer.
Background
In the face of exhaustion of fossil energy, alternative energy sources to fossil energy are actively sought, and national governments are strongly pushing energy diversification strategies. 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. The solar energy is also biomass energy, is the same as nuclear energy, solar energy, wind energy and hydraulic energy, and is an environment-friendly clean energy widely popularized by the governments of various countries at present; is deeply favored by enterprises of various countries. 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 and can greatly relieve the pollution to the atmosphere in China. 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.
The gas wall-mounted boiler is mainly used for providing daily water and heating water, and heats a water source through heat generated after gas such as natural gas is combusted, so that the purposes of heating and water supply (hot water) are achieved. For some special areas, the natural gas conveying pipelines are not available, so that the natural gas wall-mounted furnace cannot be used. Therefore, it is necessary to provide a gas wall-mounted stove which is convenient for the special region.
Disclosure of Invention
In view of the above technical problems, the present invention provides a liquid fuel expansion fischerer system for heating in winter and cooling in summer, which processes liquid fuel by high-speed collision and resonance of a resonance tank and a fissile pipe, and uses the fuel as heating and cooling.
In order to solve the technical problems, the invention adopts the following technical scheme:
a liquid fuel puffing fission device system for heating in winter and refrigerating in summer comprises a fission gasification terminal, a gasification base station, a wall hanging 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 wall-mounted furnace comprises a wall-mounted furnace body and a combustion chamber arranged in the wall-mounted furnace body, a heat exchanger is arranged in the combustion chamber, a methanol combustion furnace is arranged below the heat exchanger, water in the heat exchanger is heated through the methanol combustion furnace, a liquid inlet of the methanol combustion furnace is communicated with an outlet of a flow regulating pump, and a flue communicated with the combustion chamber is arranged on the wall-mounted furnace body;
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 hanging plate is connected with the wall-mounted furnace body, the hanging plate comprises a plate body and a hook assembly, the hook assembly comprises a connecting plate and a hook, the hook is fixedly connected with the connecting plate, the connecting plate is connected with the plate body in a sliding mode, a limiting piece is arranged between the connecting plate and the plate body, and the sliding of the connecting plate is limited through the limiting piece.
The two ends of the plate body are respectively provided with a side plate, the cross section of the connecting plate is L-shaped, the connecting plate is connected with the plate body and the side plates in a sliding way, and the plate body and the side plates are respectively provided with corresponding sliding grooves.
The limiting piece is a bolt, the bolt is connected with the connecting plate through a connecting block, a corresponding threaded through hole is formed in the connecting block, a protrusion is arranged on the side plate, and the end part of the bolt abuts against the protrusion.
And a wind shield is arranged at the air outlet.
Compared with the prior art, the invention has the beneficial effects that:
spraying the liquid fuel into the fission tube in a high-speed atomizing flow mode through high-pressure air, continuously colliding with the inner wall of the fission tube and colliding with each high-speed atomizing flow to form gas fuel, and outputting the gas fuel 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.
A methanol combustion furnace is arranged below the heat exchanger, and the water in the heat exchanger is heated by the methanol combustion furnace. Methanol is used as fuel for heating, so that wall-hanging furnaces can be used for heating in special areas (without natural gas).
Drawings
FIG. 1 is a schematic diagram of the present invention;
FIG. 2 is a schematic diagram of the overall structure of the wall-mounted boiler of the present invention;
FIG. 3 is a schematic view of the structure of the hanger plate of the present invention;
FIG. 4 is a partial schematic view of the direction A of FIG. 3;
FIG. 5 is a partial schematic view of the direction B of FIG. 3;
FIG. 6 is a schematic view of a split structure of a hanger plate of the present invention;
FIG. 7 is a partial enlarged view of FIG. 6C;
FIG. 8 is a partial enlarged view of D in FIG. 6;
FIG. 9 is a schematic view of the structure of the hanger of the present invention;
FIG. 10 is a schematic view of the structure of the exhaust device of the present invention;
FIG. 11 is a schematic view of the split structure of the exhaust device of the present invention;
fig. 12 is a schematic view of the structure of the wind deflector of the present invention.
Detailed Description
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 fission device system for heating in winter and refrigerating in summer comprises a fission gasification terminal, a gasification base station, a wall-mounted 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 wall-mounted furnace comprises a wall-mounted furnace body 31 and a combustion chamber 311 arranged in the wall-mounted furnace body 31, wherein a heat exchanger 312 is arranged in the combustion chamber 311, a methanol combustion furnace 313 is arranged below the heat exchanger 312, water in the heat exchanger 312 is heated through the methanol combustion furnace 313, and a flue 314 communicated with the combustion chamber 311 is arranged on the wall-mounted furnace body 31. The liquid inlet of the methanol combustion furnace 313 is communicated with the outlet of the flow regulating pump 603, and fuel is provided for the methanol combustion furnace 313. The methanol combustion furnace in the prior art is used for replacing a natural gas burner, so that the problems in the prior art can be solved, and heating in special areas is facilitated.
As shown in fig. 10 to 12, 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 9, the wall hanging furnace further comprises a hanging plate 32 connected with the wall hanging furnace body 31, the hanging plate 32 comprises a plate body 33 and a hook assembly 34, the hook assembly 34 comprises a connecting plate 341 and a hook 342, the hook 342 is fixedly connected with the connecting plate 341, the connecting plate 341 is slidingly connected with the plate body 33, a limiting piece 35 is arranged between the connecting plate 341 and the plate body 33, and sliding of the connecting plate 341 is limited through the limiting piece 35.
The purpose of the hook assembly 34 is to achieve the position adjustment between the hooks 342 and the plate 33, so the number of the hook assemblies 34 can be set according to practical situations, and two hooks 342 are preferably provided, namely, the positions of the two hooks 342 are adjustable; of course, one can be provided, and the other is a common fixed hook structure.
When in use, the wall body is perforated, the plate body 33 is fixed on the wall body, and the plate body 33 is provided with corresponding connecting through holes 331. After fixing, placing the level on the two hooks 342, and sliding the connecting plate 341 of one of the hooks 342 to enable the positions of the two hooks 342 to be on the same horizontal plane; after adjustment, the limiting piece 35 is used for limiting and fixing.
Because the wall-hanging furnace body 31 is hung on the hooks 342, when the two hooks 342 are positioned on the same horizontal plane, the levelness of the wall-hanging furnace body 31 is ensured.
Further, in order to ensure the overall stability, the two ends of the plate body 33 are respectively provided with a side plate 36, the cross section of the connecting plate 341 is L-shaped, the connecting plate 341 is slidably connected with the plate body 33 and the side plate 36, that is, the back surface of the connecting plate 341 is slidably connected with the plate body 33, the side surface of the connecting plate 341 is slidably connected with the side plate 36, and the plate body 33 and the side plate 36 are respectively provided with corresponding sliding grooves 37.
Further, the limiting member 35 is a bolt, the bolt is connected with the connecting plate 341 through the connecting block 38, a corresponding threaded through hole is formed in the connecting block 38, the end portion of the bolt can penetrate through the threaded through hole to abut against the protrusion 39 on the side plate 36, and the protrusion 39 is located below the connecting block 38. When in adjustment, the extending length of the screw is changed by rotating the screw.
Further, the protrusions 39 and the connection blocks 38 may be located on the inner surfaces of the side plates 36 and the connection plates 341; preferably: the projection 39 is located on the outer surface of the side plate 36 and the connecting piece 38 is located on the outer surface of the connecting piece 341, the side plate 36 being provided with a corresponding opening 310 through which opening 310 the coupling piece can protrude.
Further, the inner surface of the hook 342 is preferably circular arc shaped.
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 fischerer system for winter heating and summer cooling, characterized in that: comprises a fission gasification terminal, a gasification base station, a wall-mounted 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 wall-mounted furnace comprises a wall-mounted furnace body and a combustion chamber arranged in the wall-mounted furnace body, a heat exchanger is arranged in the combustion chamber, a methanol combustion furnace is arranged below the heat exchanger, water in the heat exchanger is heated through the methanol combustion furnace, a liquid inlet of the methanol combustion furnace is communicated with an outlet of a flow regulating pump, and a flue communicated with the combustion chamber is arranged on the wall-mounted furnace body;
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 hanging plate is connected with the wall-mounted furnace body, the hanging plate comprises a plate body and a hook assembly, the hook assembly comprises a connecting plate and a hook, the hook is fixedly connected with the connecting plate, the connecting plate is connected with the plate body in a sliding mode, a limiting piece is arranged between the connecting plate and the plate body, and the sliding of the connecting plate is limited through the limiting piece.
2. A liquid fuel expansion fischerer system for winter heating and summer cooling as claimed in claim 1 wherein: the two ends of the plate body are respectively provided with a side plate, the cross section of the connecting plate is L-shaped, the connecting plate is connected with the plate body and the side plates in a sliding way, and the plate body and the side plates are respectively provided with corresponding sliding grooves.
3. A liquid fuel expansion fischerer system for winter heating and summer cooling as claimed in claim 2 wherein: the limiting piece is a bolt, the bolt is connected with the connecting plate through a connecting block, a corresponding threaded through hole is formed in the connecting block, a protrusion is arranged on the side plate, and the end part of the bolt abuts against the protrusion.
4. A liquid fuel expansion fischerer system for winter heating and summer cooling as claimed in claim 1 wherein: and a wind shield is arranged at the air outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910244401.4A CN110173714B (en) | 2019-03-28 | 2019-03-28 | Liquid fuel puffing fission device system for heating in winter and refrigerating in summer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910244401.4A CN110173714B (en) | 2019-03-28 | 2019-03-28 | Liquid fuel puffing fission device system for heating in winter and refrigerating in summer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110173714A CN110173714A (en) | 2019-08-27 |
| CN110173714B true CN110173714B (en) | 2023-11-17 |
Family
ID=67689364
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910244401.4A Active CN110173714B (en) | 2019-03-28 | 2019-03-28 | Liquid fuel puffing fission device system for heating in winter and refrigerating in summer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110173714B (en) |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2235448Y (en) * | 1995-11-23 | 1996-09-18 | 中国人民解放军总参谋部南京离职干部休养所 | Gasoline vaporizer |
| JPH1182929A (en) * | 1997-09-02 | 1999-03-26 | Central Glass Co Ltd | Method for forming fuel spray in burner, and burner device |
| CN1769655A (en) * | 2004-11-04 | 2006-05-10 | 株式会社日立制作所 | Gas turbine power generating plant |
| JP3123131U (en) * | 2006-04-21 | 2006-07-06 | 元賓 呉 | Liquid light hydrocarbon fuel vaporizer |
| JP2008247688A (en) * | 2007-03-30 | 2008-10-16 | Casio Comput Co Ltd | Vaporizer, driving control method therefor, and power generator provided therewith |
| CN101368735A (en) * | 2007-08-14 | 2009-02-18 | 温佳宸 | Atmospheric liquid fuel gasification structure |
| CN104804786A (en) * | 2014-01-26 | 2015-07-29 | 李卫教 | Preparation technology of methanol-to-hydrocarbon combustion gas for urban pipelines |
| CN107995921A (en) * | 2015-06-16 | 2018-05-04 | 圣时有限责任合伙公司 | Gasification system |
| CN208124342U (en) * | 2018-03-07 | 2018-11-20 | 浙江金正新能源科技有限公司 | Light-hydrocarbon gas supply system |
| CN210463078U (en) * | 2019-03-28 | 2020-05-05 | 万荣金坦能源科技有限公司 | Liquid fuel puffing fission device system for heating in winter and refrigerating in summer |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6899741B2 (en) * | 1999-12-21 | 2005-05-31 | Honda Giken Kogyo Kabushiki Kaisha | Fuel evaporator |
-
2019
- 2019-03-28 CN CN201910244401.4A patent/CN110173714B/en active Active
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2235448Y (en) * | 1995-11-23 | 1996-09-18 | 中国人民解放军总参谋部南京离职干部休养所 | Gasoline vaporizer |
| JPH1182929A (en) * | 1997-09-02 | 1999-03-26 | Central Glass Co Ltd | Method for forming fuel spray in burner, and burner device |
| CN1769655A (en) * | 2004-11-04 | 2006-05-10 | 株式会社日立制作所 | Gas turbine power generating plant |
| JP3123131U (en) * | 2006-04-21 | 2006-07-06 | 元賓 呉 | Liquid light hydrocarbon fuel vaporizer |
| JP2008247688A (en) * | 2007-03-30 | 2008-10-16 | Casio Comput Co Ltd | Vaporizer, driving control method therefor, and power generator provided therewith |
| CN101368735A (en) * | 2007-08-14 | 2009-02-18 | 温佳宸 | Atmospheric liquid fuel gasification structure |
| CN104804786A (en) * | 2014-01-26 | 2015-07-29 | 李卫教 | Preparation technology of methanol-to-hydrocarbon combustion gas for urban pipelines |
| CN107995921A (en) * | 2015-06-16 | 2018-05-04 | 圣时有限责任合伙公司 | Gasification system |
| CN208124342U (en) * | 2018-03-07 | 2018-11-20 | 浙江金正新能源科技有限公司 | Light-hydrocarbon gas supply system |
| CN210463078U (en) * | 2019-03-28 | 2020-05-05 | 万荣金坦能源科技有限公司 | Liquid fuel puffing fission device system for heating in winter and refrigerating in summer |
Also Published As
| Publication number | Publication date |
|---|---|
| CN110173714A (en) | 2019-08-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110102243B (en) | Liquid fuel puffing fission gas-liquid conversion system and fission method thereof | |
| CN210463078U (en) | Liquid fuel puffing fission device system for heating in winter and refrigerating in summer | |
| CN211420085U (en) | Liquid fuel puffing fission device system for heating | |
| CN110173714B (en) | Liquid fuel puffing fission device system for heating in winter and refrigerating in summer | |
| CN109855111B (en) | Gas system | |
| CN109825337B (en) | Liquid fuel puffing fission device system for heating | |
| CN211119464U (en) | Liquid fuel puffing cracker system for heating, refrigerating and fuel gas | |
| CN201547771U (en) | Y-type bubble atomized oil gun | |
| CN210449208U (en) | Liquid fuel puffing splitter system for heating and fuel gas | |
| CN211119465U (en) | Gas system | |
| CN110173713B (en) | Liquid fuel puffing fission device system for heating, refrigerating and fuel gas | |
| CN110170291B (en) | Liquid fuel puffing fission device system for heating and fuel gas | |
| CN211119466U (en) | Liquid fuel puffing splitter system for refrigeration and fuel gas | |
| CN110145758B (en) | Liquid fuel puffing fission device system for refrigeration and fuel gas | |
| CN2433259Y (en) | Light hydrocarbon gas generation device | |
| CN210229979U (en) | Cryogenic liquid fuel puffing fission system | |
| CN201396776Y (en) | Oxygen-enriched air mixed-blowing combustion improver boiler energy-saving device | |
| CN210545162U (en) | Liquid fuel puffing fission gas-liquid conversion system | |
| CN109847686B (en) | Refrigerating liquid fuel puffing and fissioning system and method | |
| CN110105999B (en) | Liquid fuel puffing fission device capable of refrigerating and fission method | |
| CN209181249U (en) | A kind of heat-producing machine | |
| CN210458076U (en) | Liquid fuel swelling fission terminal | |
| CN210237552U (en) | Liquid fuel puffing cracker capable of refrigerating | |
| CN209558923U (en) | A kind of Power Generation by BF Gas unit fume afterheat reusing device | |
| CN109855090B (en) | Efficient biomass liquid fuel atomizing and burning system and method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |