CN211119465U - Gas system - Google Patents

Gas system Download PDF

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Publication number
CN211119465U
CN211119465U CN201920409227.XU CN201920409227U CN211119465U CN 211119465 U CN211119465 U CN 211119465U CN 201920409227 U CN201920409227 U CN 201920409227U CN 211119465 U CN211119465 U CN 211119465U
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China
Prior art keywords
gas
outlet pipe
liquid
pipe
oil
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CN201920409227.XU
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Chinese (zh)
Inventor
王彦泽
颜园甲
陈瑜
罗安文
郭鹍鹏
王苾
李鑫
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Taiyuan Meijia hydrogen New Energy Technology Co.,Ltd.
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Taiyuan Jintan Energy Technology Co ltd
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Abstract

The utility model belongs to the technical field of combustion devices, in particular to a gas system, which comprises a fission gasification terminal, a gasification base station and a gas furnace; the fission gasification terminal includes 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 furnace includes gas-cooker panel and combustor, the combustor sets up on the gas-cooker panel, the combustor includes furnace chamber, furnace end and ignition needle all set up in the furnace chamber bottom, the furnace end and the export UNICOM of flow control pump, be equipped with adjustable pot frame on the gas-cooker panel. The solid 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.

Description

Gas system
Technical Field
The utility model belongs to the technical field of burner, concretely relates to gas system.
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
To the technical problem, the utility model provides a gas system, this system handles liquid fuel through the resonance of high-speed collision, resonance case and fission pipe to use fuel supply gas furnace.
In order to solve the technical problem, the utility model discloses a technical scheme be:
a gas system comprising a fission gasification terminal, a gasification base station, and a gas furnace;
the fission gasification terminal includes a fission tube and a resonance box; a first port and a second port are respectively arranged at two ends of the fission tube body; the first port is fixedly connected with a high-pressure sprayer, a nozzle of the high-pressure sprayer is arranged in the fission tube body, the other end of the high-pressure sprayer is communicated with an inlet tube, the high-pressure sprayer 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 pressure 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, a flow regulating pump is arranged on the gas outlet pipe, and a recovery pump is arranged on the liquid outlet pipe; 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 outlet 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;
the gas furnace includes gas-cooker panel and combustor, the combustor sets up on the gas-cooker panel, the combustor includes furnace chamber, furnace end and ignition needle all set up in the furnace chamber bottom, the furnace end and the export UNICOM of flow control pump, be equipped with adjustable pot frame on the gas-cooker panel.
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; 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; a cooling jacket is arranged outside the liquid fuel tank and is connected with an outlet of the cooling pipe; and the oil storage device is provided with a breather valve.
The adjustable pot rack comprises a bottom ring and a pot claw assembly, the pot claw assembly is at least three, the pot claw assembly comprises a connecting block and a pot claw, the pot claw is hinged to the connecting block, a limiting block is arranged on the connecting block, the rotating angle of the pot claw is limited by the limiting block, and the connecting block is detachably connected with the bottom ring.
The connecting block is inserted with the bottom ring, and a corresponding slot is arranged on the connecting block.
The connecting block is at least provided with two slots.
And a threaded hole is formed in the connecting block and penetrates through the slot.
Compared with the prior art, the utility model, the beneficial effect who has is:
the utility model provides a fission gas-liquid conversion system, which sprays liquid fuel into a fission tube in a high-speed atomizing flow form through high-pressure gas, continuously collides with the inner wall of the fission tube and collides with each high-speed atomizing flow to form gas fuel, and then outputs the gas fuel for use through an outlet pipe; the resonance of the high-pressure gas in the resonance box and the liquid fuel in the fission tube in the process of impacting the fission tube through the gasification of the liquid fuel 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 liquid fuel and 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 diagram of the present invention;
FIG. 2 is a schematic view of the whole structure of the gas stove of the present invention;
FIG. 3 is a schematic structural view of the adjustable pot rack of the present invention;
fig. 4 is a schematic view of the threaded hole of the present invention;
FIG. 5 is a schematic view of the adjustable pot rack of the present invention in use;
FIG. 6 is a schematic structural view of the arc-shaped support ring of the present invention;
fig. 7 is a schematic structural diagram of the slot of the present invention.
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, a gas system includes a fission gasification terminal, a gasification base station, and a gas furnace;
the fission gasification terminal comprises a fission tube 1 and a resonance box 7; a first port 2 and a second port 3 are respectively arranged at two ends of a tube body of the fission tube 1; 2 fixedly connected with high pressure nozzle 4 of first port, the nozzle setting of high pressure nozzle 4 is in 1 body of fission pipe, and high pressure nozzle 4 other end intercommunication inlet tube 5, and high pressure nozzle 4 sprays many high-speed efflux, and high-speed efflux penetrates directly 1 body inner wall of fission pipe and continues to collide with 1 body inner wall of fission pipe and rather than the high-speed efflux of alternately high-speed behind the reflection, forms tiny particle, discharges fission pipe 1 under the effect of high-pressure gas. The inlet pipe 5 comprises a gas inlet pipe 501 and a liquid inlet pipe 502, 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 resonance box body, 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 from the cooling pipe 10;
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 outlet pipe 6 of the gasification terminal; 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 a gasification terminal gas outlet pipe 501; specifically, the method comprises the following steps: high-pressure air is introduced into the gas inlet pipe, and liquid fuel is introduced into the liquid inlet pipe; adjusting the inlet pressure of liquid fuel to 0.1MPa, the flow rate to 500 ml/h, the inlet pressure of high-pressure air to 2-6MPa and the flow rate to 4-10 m/s, introducing liquid fuel and 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;
the gas furnace includes gas-cooker panel 41 and combustor 411, and combustor 411 sets up on gas-cooker panel 41, and combustor 411 includes furnace chamber 4111, furnace end 4112 and ignition needle 4113, and furnace end 4112 and ignition needle 4113 all set up in the furnace chamber 4111 bottom, and furnace end 4112 and the export UNICOM of flow control pump 603 provide fuel for the burning. An adjustable pot frame 42 is arranged on the gas panel 1. The cavity 4111 is a ring-shaped sealing structure.
In the embodiment, 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 7 is hermetically connected with the fission tube 1; the cooling pipe 10 is hermetically connected with the resonance box 7 at the outer walls of the two ends of the resonance box 7.
In the 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 is communicated with the oil storage device 13 through the fuel liquid outlet pipe 122. A gas-liquid separation pipe 14 is arranged in the oil-gas separation device 12, the gas-liquid separation pipe 14 is a coiled pipe, the tail end of the gas-liquid separation pipe 14 is a waste 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, the lowest part of the inclined plane is provided with a fuel liquid outlet pipe 122, and the fuel liquid outlet pipe 122 is provided with a one-way valve. The liquid fuel tank is externally provided with a cooling jacket 15, and the cooling jacket 15 is connected with the outlet of the cooling pipe 10. The oil storage device 13 is provided with a breather valve 16.
As shown in fig. 2 to 7, the adjustable pot holder 42 is placed on the gas range panel 41, the adjustable pot holder 42 includes a bottom ring 43 and at least three pot claw assemblies 44, and the number of the pot claw assemblies 44 can be set according to actual conditions.
The pan claw assembly 44 comprises a connecting block 45 and a pan claw 46, one end of the pan claw 46 is hinged to 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 by the limiting block 47, and the connecting block 45 is detachably connected with the bottom ring 43. One, preferably two, limiting blocks 47 can be arranged; when one is arranged, the angle of the pot claws 46 when closed can be limited; when two are provided, the angle of the pot claws 46 can be limited when the pot claws are closed and opened.
When a pot with a small bottom area such as a medicine pot, a milk pot and the like needs to be used, the pot claws 46 can be rotated inwards, so that the distance between the pot claws 46 is reduced, and a good supporting effect can be realized on the pot with the small bottom area. On the contrary, when a pot with a larger bottom area is placed, such as a frying pan, a steaming pan and the like, the pot claws 46 can be rotated outwards, so that the distance between the pot claws 46 is increased, and the pot with the larger bottom area can be supported.
Further, the bottom of the connecting block 45 is provided with a corresponding slot 48, and is inserted into the bottom ring 43 through the slot 48; since the bottom ring 43 is a circular ring structure, the slot is correspondingly arc-shaped.
Further, at least two slots 48 are formed on the connecting block 45. A plurality of slots 48 are provided and the corresponding slot 48 may be selected as desired to provide fine adjustment of the position between the connector block 45 and the bottom ring 43.
Further, in order to ensure the fastening of the connection, a threaded hole 49 is formed on the connecting block 45, and the threaded hole 49 penetrates through the slot 48. After the connecting block 45 is inserted into the bottom ring 43 through the slot 48, a bolt is screwed into the threaded hole 49, and the bolt penetrates through the slot 48 to abut against the bottom ring 43, so that the fixing effect is further achieved.
Further, the stopper 47 is preferably wedge-shaped.
Further, the pot claw 46 is provided with an arc-shaped support ring 410. After the pot claws 46 are closed, the contact area between the pot claws and the pot can be increased through the arc-shaped support ring 410, and the stable placement of the pot is ensured.
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 (6)

1. A gas system, characterized in that: the system comprises a fission gasification terminal, a gasification base station and a gas furnace;
the fission gasification terminal includes a fission tube and a resonance box; a first port and a second port are respectively arranged at two ends of the fission tube body; the first port is fixedly connected with a high-pressure sprayer, a nozzle of the high-pressure sprayer is arranged in the fission tube body, the other end of the high-pressure sprayer is communicated with an inlet tube, the high-pressure sprayer 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 pressure 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, a flow regulating pump is arranged on the gas outlet pipe, and a recovery pump is arranged on the liquid outlet pipe; 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 outlet 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;
the gas furnace includes gas-cooker panel and combustor, the combustor sets up on the gas-cooker panel, the combustor includes furnace chamber, furnace end and ignition needle all set up in the furnace chamber bottom, the furnace end and the export UNICOM of flow control pump, be equipped with adjustable pot frame on the gas-cooker panel.
2. A gas system according to claim 1, characterized in that: 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; 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; a cooling jacket is arranged outside the liquid fuel tank and is connected with an outlet of the cooling pipe; and the oil storage device is provided with a breather valve.
3. A gas system according to claim 1, characterized in that: the adjustable pot rack comprises a bottom ring and a pot claw assembly, the pot claw assembly is at least three, the pot claw assembly comprises a connecting block and a pot claw, the pot claw is hinged to the connecting block, a limiting block is arranged on the connecting block, the rotating angle of the pot claw is limited by the limiting block, and the connecting block is detachably connected with the bottom ring.
4. A gas system according to claim 3, characterized in that: the connecting block is inserted with the bottom ring, and a corresponding slot is arranged on the connecting block.
5. A gas system according to claim 3, characterized in that: the connecting block is at least provided with two slots.
6. A gas system according to claim 3, characterized in that: and a threaded hole is formed in the connecting block and penetrates through the slot.
CN201920409227.XU 2019-03-28 2019-03-28 Gas system Active CN211119465U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201920409227.XU CN211119465U (en) 2019-03-28 2019-03-28 Gas system

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Application Number Priority Date Filing Date Title
CN201920409227.XU CN211119465U (en) 2019-03-28 2019-03-28 Gas system

Publications (1)

Publication Number Publication Date
CN211119465U true CN211119465U (en) 2020-07-28

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Application Number Title Priority Date Filing Date
CN201920409227.XU Active CN211119465U (en) 2019-03-28 2019-03-28 Gas system

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109855111A (en) * 2019-03-28 2019-06-07 万荣金坦能源科技有限公司 A kind of gas burning system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109855111A (en) * 2019-03-28 2019-06-07 万荣金坦能源科技有限公司 A kind of gas burning system
CN109855111B (en) * 2019-03-28 2024-01-30 万荣金坦能源科技有限公司 Gas system

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Address after: 030006 station 96, Zhongchuang space, Yunzhu company, 12th floor, Danyang science and technology building, No. 9, science and Technology Street, Taiyuan Xuefu Park, Shanxi comprehensive reform demonstration zone, Taiyuan City, Shanxi Province

Patentee after: Taiyuan Meijia hydrogen New Energy Technology Co.,Ltd.

Address before: 030006 station 96, Zhongchuang space, Yunzhu company, 12th floor, Danyang science and technology building, No. 9, science and Technology Street, Taiyuan Xuefu Park, Shanxi comprehensive reform demonstration zone, Taiyuan City, Shanxi Province

Patentee before: Taiyuan Jintan Energy Technology Co.,Ltd.