CN109847686A - A kind of liquid fuel extruding fission system and fission method freezed - Google Patents
A kind of liquid fuel extruding fission system and fission method freezed Download PDFInfo
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- CN109847686A CN109847686A CN201910245388.4A CN201910245388A CN109847686A CN 109847686 A CN109847686 A CN 109847686A CN 201910245388 A CN201910245388 A CN 201910245388A CN 109847686 A CN109847686 A CN 109847686A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/30—Nuclear fission reactors
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Abstract
The present invention relates to liquid fuel processing techniques, the liquid fuel extruding fission system and fission method that can freeze more particularly to one kind, liquid fuel is sprayed into fission pipe by high speed atomisation manifold formula by high pressure gas, constantly collision and the collision of each high speed atomisation stream are managed in fission, after forming gaseous fuel, is exported and used by outlet;By resonance box, reinforce the gasification of liquid fuel;Outlet uses T-type pipe, and the big droplet carried secretly in gaseous fuel flow falls into liquid outlet through gravity and recycled;Process heat absorption, is used for air-cooler and cooling jacket cold air source, and air-cooler passes through regulation pipe regulating air volume;Liquid fuel tank realizes the recycling of boiling point outlet fuel;Fuel Tanking Unit setting breather valve, which ensure that in Fuel Tanking Unit, to be stablized.Whole system is not necessarily to applied force, external heat, liquid fuel can be made to stable gaseous fuel, which is more conducive to store and transport under the assistance of high pressure gas.
Description
Technical field
The present invention relates to liquid fuel processing techniques, and more specifically, the liquid fuel extruding that being related to one kind can freeze is split
Change system and fission method.
Background technique
In face of the exhaustion of fossil energy, people energetically seek the alternative energy source of fossil energy, and national government is carried forward vigorously
Energy diversification strategy.Domestic and international many boiler research institutions have all turned one's attention to cleaning, cheap substitute fuel, such as natural
Gas, methanol, electricity etc..Alcohol-based fuel is most potential novel alternative energy source, alcohol-based fuel be exactly with alcohols (such as methanol, ethyl alcohol,
Butanol etc.) fuel that configures based on substance.It is existing for liquid or solid form.It is also a kind of biomass energy,
It is the environment protection clean energy that national governments widely popularize at present as nuclear energy, solar energy, wind power energy, hydraulic energy;Deeply by various countries
The favor of business organization.This is because methanol molecules formula is more single than the molecular formula of coal, gasoline, diesel oil, burning and exhausting is very
Cleaning, without particulate matter (PM2.5, PM10), ozone, sulfur dioxide, CO, mercury and mercuric compounds, discharged nitrous oxides are than natural
Low 10 times of gas boiler or more.Methanol fuel can greatly alleviate the atmosphere pollution for troubling China with Substitute coal, diesel oil.Especially
It is the main feature that oil-poor, few gas, more coals are China's energy resource structure at this stage, therefore, important derivative of the methanol as coal chemical industry
Product is one of the alternative fuel of great future generally acknowledged at present.Liquid methanol is high as fuel combustion energy consumption, needs to preheat,
It burns insufficient;Gaseous methanol is relatively low as fuel combustion energy consumption, burns more abundant, there is a promotional value, but easy carbon distribution;Mist
It is few to change methanol carbon distribution, but energy consumption is high.
Summary of the invention
In the presence of overcoming the shortcomings of the prior art, the present invention provides a kind of liquid fuel extruding fission that can freeze
System and fission method, by high velocity impact, the resonance treatment liquid fuel of resonance box and fission pipe, preparation is stablized, low energy consumption,
It is not easy the fuel of carbon distribution, the preparation of cold air is used for air-cooler by process heat absorption, the preparation for the gas that can be used for freezing.
In order to solve the above-mentioned technical problem, the technical scheme adopted by the invention is as follows:
A kind of liquid fuel extruding fission system freezed, including fission boiling point and gasification base station;
The fission boiling point includes fission pipe and resonance box;High-pressure nozzle, inlet tube are set in the fission pipe pipe and gone out
Mouth pipe, the fission pipe are respectively arranged with first port and second port at tube body both ends;The first port is fixedly connected with
High-pressure nozzle, high-pressure nozzle include mixing chamber and nozzle, and mixing chamber is connected to nozzle;The nozzle includes spray chamber and injection
Hole, spray chamber are hemispherical, and spray chamber is connected to by spray-hole with fission pipe;High-pressure nozzle mixing cavity rear end is connected to inlet tube,
The inlet tube includes gas inlet pipe and liquid inlet duct, is provided with force (forcing) pump on the liquid inlet duct;The second end
Mouth is fixedly connected with outlet, and outlet is T-type pipe, and transverse tube is gas outlet tube, and the vertical tube below transverse tube is liquid outlet tube,
Gas outlet tube is connected with liquid outlet tube, and flow-rate adjustment pump, the liquid outlet tube are provided on the gas outlet tube
On be provided with recovery pump;The resonance box is nested in outside fission pipe, is provided with constant pressure valve and high pressure gas on the resonance box body
Entrance and cooling tube fill pressure-air in the box body that resonates, and high pressure gas entrance is for being passed through high pressure gas;The cooling tube runs through
Resonate box body, and cooling tube is passed through normal temperature air, and cooling tube exports cool air hose and exports Cryogenic air;
The gasification base station includes liquid fuel tank and air compressor machine, and the liquid fuel tank includes that gas and oil separating plant and oil storage fill
It sets;The gas and oil separating plant is for separating liquid fuel and gas in boiling point outlet;The gas and oil separating plant connects
The liquid outlet tube of exit pipe, gas and oil separating plant upside are provided with waste gas outlet pipe, and downside is provided with fuel fluid outlet,
The gas and oil separating plant is connected to by fuel fluid outlet with Fuel Tanking Unit;The Fuel Tanking Unit is for storing liquid fuel;
Boiling point liquid inlet duct is connected on the downside of the Fuel Tanking Unit;It is described used for air compressor in offer compressed air, the air compressor machine
Connect boiling point gas inlet pipe;
The air-cooler includes shell and regulation pipe;The cool air hose runs through air-cooler, and cool air hose is opened up through air-cooler part
There is the first air outlet;The regulation pipe is set on cool air hose, and the regulation pipe offers the second air outlet;The regulation pipe one
End is provided with sawtooth;The regulation pipe both ends are arranged with the first fixing sleeve and the second fixing sleeve, first fixing sleeve and second
Fixing sleeve is fixed in air-cooler by support rod;The second fixing sleeve lower half circumference offers slot, the regulation pipe setting
There is sawtooth one end to be set in the second fixing sleeve, bead, the bead and saw are provided between the sawtooth and the second fixing sleeve
Tooth engagement connection, second fixing sleeve end and regulation pipe are provided with sawtooth one end end spacing less than bead diameter.
Further, the high-pressure nozzle and first port are tightly connected;The outlet and second port are tightly connected;
The resonance box is connect with the fission seal of tube;Cooling tube both ends outer wall in resonance box is tightly connected with resonance box respectively.
Further, the fission pipe tube length and diameter ratio are 40:2-40:6.
Further, the distance of the liquid outlet tube distance fission pipe of the outlet is 1-4mm.
Further, the second outlet air open area is not less than the first outlet air open area.
Further, the shell offers cold air outlet.
A kind of liquid fuel extruding fission method, comprising the following steps:
(1) gas inlet pipe of liquid fuel extruding fission device is passed through pressure-air, and liquid inlet duct is passed through liquid fuel;Altogether
Vibration case high pressure gas entrance is passed through high pressure gas;Adjustment liquid fuel inlet port pressure is 0.1MPa, and flow velocity is 500 mls/hour;High pressure
Air inlet pressure 2-6MPa, flow velocity 4m/s-10m/s;
(2) liquid fuel and pressure-air are high through a plurality of high-speed jet of liquid fuel extruding fission device mesohigh spray head injection
Rapid fire stream direct projection fission pipe inboard wall of tube body continues and fission pipe inboard wall of tube body and the high-speed jet intersected with it high speed after reflection
Collision, fission pipe tube body is wrapped in outer high pressure gas with it and forms resonance, and sends energy to high-speed jet, so that high rapid fire
Flow liquid state fuel particle constantly becomes smaller until fission pipe is discharged in it under the action of high pressure gas;
(3) liquid fuel is discharged after fission pipe extruding fission through outlet, and gas and liquid, gas are separated into outlet
It can be directly used as fuel.
Further, the liquid fuel uses methanol.
Further, the methanol purity is greater than 92%.
Compared with prior art, the advantageous effect of present invention is that:
The present invention provides liquid fuel extruding fission systems and fission method that one kind can freeze, are fired liquid by high pressure gas
Material is sprayed into fission pipe by high speed atomisation manifold formula, is managed constantly collision and the collision of each high speed atomisation stream in fission, is formed
After gaseous fuel, is exported and used by outlet;By resonance box, realize that liquid fires in resonance box mesohigh gas and fission pipe
Resonance of the material gasification to the process of fission pipe impact, reinforces the gasification of liquid fuel;Outlet uses T-type pipe, gaseous fuel flow
The big droplet of middle entrainment falls into liquid outlet through gravity and is recycled;By being atomized endothermic process, for air-cooler and cold
But collet cold air source, air-cooler improve liquid fuel and gas in gas and oil separating plant by regulation pipe regulating air volume
Separative efficiency, while reducing the gasification of liquid fuel in Fuel Tanking Unit, guarantee the stability of system;Liquid fuel tank realizes
The recycling of boiling point outlet fuel, while realizing the stable storage of liquid fuel;Fuel Tanking Unit setting breather valve ensure that
Stablize in Fuel Tanking Unit.Whole system is not necessarily to applied force, external heat, and liquid fuel can be made to stable gaseous fuel, should
Gaseous fuel is more conducive to store and transport under the assistance of high pressure gas, and provides air-cooler and cooling jacket cold wind source.
Detailed description of the invention
Fig. 1 is the liquid fuel extruding fission system schematic that one kind provided by the invention can freeze;
Fig. 2 is high-pressure nozzle schematic diagram;
Fig. 3 is air-cooler schematic diagram of internal structure;
Fig. 4 is regulation pipe and fixing sleeve cross-sectional view;
Fig. 5 is regulation pipe and the second fixing sleeve connection schematic diagram.
In figure, 1 is fission pipe, and 2 be first port, and 3 be second port;4 be high-pressure nozzle, and 5 be inlet tube, and 501 be gas
Body inlet tube, 502 be liquid inlet duct, and 6 be outlet, and 601 be gas outlet tube, and 602 be liquid outlet tube, and 7 be mixing chamber,
8 be spray chamber, and 9 be spray-hole, and 10 be resonance box, and 11 be constant pressure valve, and 12 be high pressure gas entrance, and 13 be cooling tube, and 14 be pneumatics
Machine, 15 be gas and oil separating plant, and 151 be waste gas outlet pipe, and 152 be fuel fluid outlet, and 16 be Fuel Tanking Unit, and 17 be gas-liquid point
From pipe, 18 be cooling jacket, and 19 be breather valve, and 20 be cool air hose, and 21 be shell, and 22 be regulation pipe, and 23 be the first air outlet, 24
It is sawtooth for the second air outlet, 25,26 be the first fixing sleeve, and 27 be the second fixing sleeve, and 28 be support rod, and 29 slots, 30 be bead,
31 be cold air outlet.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
As shown in Figs. 1-5, a kind of liquid fuel extruding fission system freezed, including fission boiling point and gasification base
It stands;
The fission boiling point includes fission pipe 1 and resonance box 10;The fission pipe 1 manages interior setting high-pressure nozzle 4, inlet tube
5 and outlet 6, the fission pipe 1 be respectively arranged with first port 2 and second port 3 at tube body both ends;The first port 2
It is fixedly connected with high-pressure nozzle 4, high-pressure nozzle includes mixing chamber 7 and nozzle, and mixing chamber 7 is connected to nozzle;The nozzle includes
Spray chamber 8 and spray-hole 9, spray chamber 8 are hemispherical, and spray chamber 8 is connected to by spray-hole 9 with fission pipe 1;High-pressure nozzle 4 is mixed
It closes 7 rear end of chamber and is connected to inlet tube 5, the inlet tube 5 includes gas inlet pipe 501 and liquid inlet duct 502, the liquid inlet
Force (forcing) pump 503 is provided on pipe 501;The second port 3 is fixedly connected with outlet 6, and outlet 6 is T-type pipe, and transverse tube is gas
Body outlet 601, the vertical tube below transverse tube is liquid outlet tube 602, and gas outlet tube 601 is connected with liquid outlet tube 602,
It is provided with flow-rate adjustment pump 603 on the gas outlet tube 601, is provided with recovery pump 604 on the liquid outlet tube 602;Institute
It states resonance box 10 to be nested in outside fission pipe 1, constant pressure valve 11 and high pressure gas entrance 12 and cold is provided on 10 cabinet of resonance box
But pipe 13 fill pressure-air in 10 cabinet of resonance box, and high pressure gas entrance 12 is for being passed through high pressure gas;The cooling tube 13 runs through
10 cabinet of resonance box, cooling tube 13 are passed through normal temperature air, and cooling tube 13 exports cool air hose 20 and exports Cryogenic air;The gasification base
It stands including liquid fuel tank and air compressor machine 14, the liquid fuel tank includes gas and oil separating plant 15 and Fuel Tanking Unit 16;It is described
Gas and oil separating plant 15 is for liquid in withdrawal liquid outlet 602;The liquid of the 15 connection outlet pipe 6 of gas and oil separating plant
Outlet 602 is provided with waste gas outlet pipe 151 on the upside of gas and oil separating plant 15, and downside is provided with fuel fluid outlet 152, institute
Gas and oil separating plant 15 is stated to be connected to by fuel fluid outlet 152 with Fuel Tanking Unit 16;The Fuel Tanking Unit 16 is for storing liquid
State fuel;Boiling point liquid inlet duct 502 is connected on the downside of the Fuel Tanking Unit 16;The air compressor machine 14 is empty for providing compression
Gas, the air compressor machine 14 connect boiling point gas inlet pipe 501;The air-cooler includes shell 21 and regulation pipe 22;It is described
Cool air hose 22 runs through air-cooler, and cool air hose 20 offers the first air outlet 23 through air-cooler part;The regulation pipe 22 is arranged
On cool air hose 20, the regulation pipe 22 offers the second air outlet 24;Described 22 one end of regulation pipe is provided with sawtooth 25;It is described
22 both ends of regulation pipe are arranged with the first fixing sleeve 26 and the second fixing sleeve 27, and first fixing sleeve 26 and the second fixing sleeve 27 are logical
Support rod 28 is crossed to be fixed in air-cooler;Second fixing sleeve, the 27 lower half circumference offers slot 29, and the regulation pipe 22 is arranged
There is 25 one end of sawtooth to be set in the second fixing sleeve 27, bead 30, institute are provided between the sawtooth 25 and the second fixing sleeve 27
It states bead 30 and engages connection with sawtooth 25,27 end of the second fixing sleeve and regulation pipe 22 are provided between 25 one end end of sawtooth
Away from less than 30 diameter of bead.The high-pressure nozzle 4 is tightly connected with first port 2;The outlet 6 is sealed with second port 3
Connection;The resonance box 10 is tightly connected with fission pipe 1;Cooling tube 13 in resonance box 10 both ends outer wall respectively with resonance box 10
It is tightly connected.1 tube length of fission pipe and diameter ratio are 40:2-40:6.The liquid outlet tube 602 of the outlet 6 away from
It is 1-4mm with a distance from fission pipe 1.Second air outlet, 24 area is not less than 23 area of the first air outlet.The shell 21
Offer cold air outlet 31.
A kind of liquid fuel extruding fission method, comprising the following steps:
(1) gas inlet pipe of liquid fuel extruding fission device is passed through pressure-air, and liquid inlet duct is passed through liquid fuel;Altogether
Vibration case high pressure gas entrance is passed through high pressure gas;Adjustment liquid fuel inlet port pressure is 0.1MPa, and flow velocity is 500 mls/hour;High pressure
Air inlet pressure 2-6MPa, flow velocity 4m/s-10m/s;
(2) liquid fuel and pressure-air are high through a plurality of high-speed jet of liquid fuel extruding fission device mesohigh spray head injection
Rapid fire stream direct projection fission pipe inboard wall of tube body continues and fission pipe inboard wall of tube body and the high-speed jet intersected with it high speed after reflection
Collision, fission pipe tube body is wrapped in outer high pressure gas with it and forms resonance, and sends energy to high-speed jet, so that high rapid fire
Flow liquid state fuel particle constantly becomes smaller until fission pipe is discharged in it under the action of high pressure gas;
(3) liquid fuel is discharged after fission pipe extruding fission through outlet, and gas and liquid, gas are separated into outlet
It can be directly used as fuel.
In the present embodiment, the liquid fuel uses methanol.The methanol purity is greater than 92%.
For the present embodiment when implementing, liquid fuel, which is pressed to form after liquid flow, enters high-pressure nozzle through liquid inlet duct 502
4, gas pressurized, which is formed after gas stream, enters high-pressure nozzle through gas inlet pipe 501, and liquid flow and gas stream are in high-pressure nozzle 4
It meets and forms a plurality of high-pressure jet injection fission 1 tube body of pipe through the ejection of high-pressure nozzle 4, high-pressure jet is in fission 1 tube body inner tube of pipe
Wall constantly collides reflection, and the also constantly mutually collision of each high-pressure jet, at the same time, the high pressure being distributed in outside fission 1 tube body of pipe
Air and fission 1 tube body of pipe generate resonance, (absorb energy and heat, overcome surface tension) liquid fuel during collision
Drop constantly ruptures and wears, promote Surface Renewal and increase its surface area, until stabilization, in the impetus of high pressure draught
It is discharged by outlet 6 down, the drop carried in high pressure draught falls under gravity into liquid outlet 602, residual gas warp
Gas vent 601 exports fuel gas, and fuel gas is that high pressure gas carries the minimum fuel droplet of partial size, and stable storage was using
Low energy consumption in journey, is not easy carbon distribution.Constantly heat is absorbed from surrounding in liquid fuel puffing process to be used for using the endothermic process
Air-cooler and cooling jacket cold air source.
Only presently preferred embodiments of the present invention is explained in detail above, but the present invention is not limited to above-described embodiment,
Within the knowledge of a person skilled in the art, it can also make without departing from the purpose of the present invention each
Kind variation, various change should all be included in the protection scope of the present invention.
Claims (9)
- The system 1. the liquid fuel extruding that one kind can freeze is fissioned, it is characterised in that: including fission boiling point and gasification base station;The fission boiling point includes fission pipe and resonance box;High-pressure nozzle, inlet tube are set in the fission pipe pipe and gone out Mouth pipe, the fission pipe are respectively arranged with first port and second port at tube body both ends;The first port is fixedly connected with High-pressure nozzle, high-pressure nozzle include mixing chamber and nozzle, and mixing chamber is connected to nozzle;The nozzle includes spray chamber and injection Hole, spray chamber are hemispherical, and spray chamber is connected to by spray-hole with fission pipe;High-pressure nozzle mixing cavity rear end is connected to inlet tube, The inlet tube includes gas inlet pipe and liquid inlet duct, is provided with force (forcing) pump on the liquid inlet duct;The second end Mouth is fixedly connected with outlet, and outlet is T-type pipe, and transverse tube is gas outlet tube, and the vertical tube below transverse tube is liquid outlet tube, Gas outlet tube is connected with liquid outlet tube, and flow-rate adjustment pump, the liquid outlet tube are provided on the gas outlet tube On be provided with recovery pump;The resonance box is nested in outside fission pipe, is provided with constant pressure valve and high pressure gas on the resonance box body Entrance and cooling tube fill pressure-air in the box body that resonates, and high pressure gas entrance is for being passed through high pressure gas;The cooling tube runs through Resonate box body, and cooling tube is passed through normal temperature air, and cooling tube exports cool air hose and exports Cryogenic air;The gasification base station includes liquid fuel tank and air compressor machine, and the liquid fuel tank includes that gas and oil separating plant and oil storage fill It sets;The gas and oil separating plant is for separating liquid fuel and gas in boiling point outlet;The gas and oil separating plant connects The liquid outlet tube of exit pipe, gas and oil separating plant upside are provided with waste gas outlet pipe, and downside is provided with fuel fluid outlet, The gas and oil separating plant is connected to by fuel fluid outlet with Fuel Tanking Unit;The Fuel Tanking Unit is for storing liquid fuel; Boiling point liquid inlet duct is connected on the downside of the Fuel Tanking Unit;It is described used for air compressor in offer compressed air, the air compressor machine Connect boiling point gas inlet pipe;The air-cooler includes shell and regulation pipe;The cool air hose runs through air-cooler, and cool air hose is opened up through air-cooler part There is the first air outlet;The regulation pipe is set on cool air hose, and the regulation pipe offers the second air outlet;The regulation pipe one End is provided with sawtooth;The regulation pipe both ends are arranged with the first fixing sleeve and the second fixing sleeve, first fixing sleeve and second Fixing sleeve is fixed in air-cooler by support rod;The second fixing sleeve lower half circumference offers slot, the regulation pipe setting There is sawtooth one end to be set in the second fixing sleeve, bead, the bead and saw are provided between the sawtooth and the second fixing sleeve Tooth engagement connection, second fixing sleeve end and regulation pipe are provided with sawtooth one end end spacing less than bead diameter.
- The system 2. the liquid fuel extruding that one kind according to claim 1 can freeze is fissioned, it is characterised in that: the high pressure Spray head and first port are tightly connected;The outlet and second port are tightly connected;The resonance box and the fission seal of tube connect It connects;Cooling tube both ends outer wall in resonance box is tightly connected with resonance box respectively.
- The system 3. the liquid fuel extruding that one kind according to claim 1 can freeze is fissioned, it is characterised in that: the fission Pipe tube length and diameter ratio are 40:2-40:6.
- The system 4. the liquid fuel extruding that one kind according to claim 1 can freeze is fissioned, it is characterised in that: the outlet The distance of the liquid outlet tube distance fission pipe of pipe is 1-4mm.
- The system 5. the liquid fuel extruding that one kind according to claim 1 can freeze is fissioned, it is characterised in that: described second Outlet air open area is not less than the first outlet air open area.
- The system 6. the liquid fuel extruding that one kind according to claim 1 can freeze is fissioned, it is characterised in that: the shell Offer cold air outlet.
- A kind of method 7. liquid fuel extruding is fissioned, which comprises the following steps:(1) gas inlet pipe of liquid fuel extruding fission device is passed through pressure-air, and liquid inlet duct is passed through liquid fuel;Altogether Vibration case high pressure gas entrance is passed through high pressure gas;Adjustment liquid fuel inlet port pressure is 0.1MPa, and flow velocity is 500 mls/hour;High pressure Air inlet pressure 2-6MPa, flow velocity 4m/s-10m/s;(2) liquid fuel and pressure-air are high through a plurality of high-speed jet of liquid fuel extruding fission device mesohigh spray head injection Rapid fire stream direct projection fission pipe inboard wall of tube body continues and fission pipe inboard wall of tube body and the high-speed jet intersected with it high speed after reflection Collision, fission pipe tube body is wrapped in outer high pressure gas with it and forms resonance, and sends energy to high-speed jet, so that high rapid fire Flow liquid state fuel particle constantly becomes smaller until fission pipe is discharged in it under the action of high pressure gas;(3) liquid fuel is discharged after fission pipe extruding fission through outlet, and gas and liquid, gas are separated into outlet It can be directly used as fuel.
- The method 8. a kind of liquid fuel extruding according to claim 7 is fissioned, it is characterised in that: the liquid fuel uses Methanol.
- The method 9. a kind of liquid fuel extruding according to claim 8 is fissioned, it is characterised in that: the methanol purity is greater than 92%。
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110624495A (en) * | 2019-11-04 | 2019-12-31 | 锦益创典(天津)科技有限责任公司 | Nitrosation continuous reaction device and method |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2158031Y (en) * | 1992-12-10 | 1994-03-02 | 南京航空航天大学 | Internal ultrasonic atomizing nozzle |
CN2246151Y (en) * | 1996-01-23 | 1997-01-29 | 杜献军 | Gas preparing and feeding pot |
JPH1182929A (en) * | 1997-09-02 | 1999-03-26 | Central Glass Co Ltd | Method for forming fuel spray in burner, and burner device |
RU2142604C1 (en) * | 1998-01-26 | 1999-12-10 | Петраков Александр Дмитриевич | Heat energy production process and resonant heat pump/generator unit |
JP2001107805A (en) * | 1999-08-05 | 2001-04-17 | Nippon Soken Inc | Fuel injection system of internal combustion engine |
EP1284235A1 (en) * | 2001-08-15 | 2003-02-19 | Sulzer Hexis AG | Process for reforming fuels, especially fuel oil |
CN101649226A (en) * | 2009-09-11 | 2010-02-17 | 北京震宇成套电气设备集团 | Method for preparing fuel gas by gasifying biomass materials and device thereof |
CN102162398A (en) * | 2010-02-12 | 2011-08-24 | 通用电气公司 | Method of controlling a combustor for a gas turbine |
CN103822207A (en) * | 2012-11-16 | 2014-05-28 | 航天长征化学工程股份有限公司 | Variable pressure and variable working condition oil burner |
US20170072377A1 (en) * | 2014-03-26 | 2017-03-16 | Clean Fuels B.V. | Method and apparatus for conversion of liquid fuels in a reactor, use of an apparatus for conversion of liquid fuels |
CN210229979U (en) * | 2019-03-28 | 2020-04-03 | 万荣金坦能源科技有限公司 | Cryogenic liquid fuel puffing fission system |
-
2019
- 2019-03-28 CN CN201910245388.4A patent/CN109847686B/en active Active
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2158031Y (en) * | 1992-12-10 | 1994-03-02 | 南京航空航天大学 | Internal ultrasonic atomizing nozzle |
CN2246151Y (en) * | 1996-01-23 | 1997-01-29 | 杜献军 | Gas preparing and feeding pot |
JPH1182929A (en) * | 1997-09-02 | 1999-03-26 | Central Glass Co Ltd | Method for forming fuel spray in burner, and burner device |
RU2142604C1 (en) * | 1998-01-26 | 1999-12-10 | Петраков Александр Дмитриевич | Heat energy production process and resonant heat pump/generator unit |
JP2001107805A (en) * | 1999-08-05 | 2001-04-17 | Nippon Soken Inc | Fuel injection system of internal combustion engine |
EP1284235A1 (en) * | 2001-08-15 | 2003-02-19 | Sulzer Hexis AG | Process for reforming fuels, especially fuel oil |
CN101649226A (en) * | 2009-09-11 | 2010-02-17 | 北京震宇成套电气设备集团 | Method for preparing fuel gas by gasifying biomass materials and device thereof |
CN102162398A (en) * | 2010-02-12 | 2011-08-24 | 通用电气公司 | Method of controlling a combustor for a gas turbine |
CN103822207A (en) * | 2012-11-16 | 2014-05-28 | 航天长征化学工程股份有限公司 | Variable pressure and variable working condition oil burner |
US20170072377A1 (en) * | 2014-03-26 | 2017-03-16 | Clean Fuels B.V. | Method and apparatus for conversion of liquid fuels in a reactor, use of an apparatus for conversion of liquid fuels |
CN210229979U (en) * | 2019-03-28 | 2020-04-03 | 万荣金坦能源科技有限公司 | Cryogenic liquid fuel puffing fission system |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110624495A (en) * | 2019-11-04 | 2019-12-31 | 锦益创典(天津)科技有限责任公司 | Nitrosation continuous reaction device and method |
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