WO2007129604A1 - 炭化水素系燃料の燃焼装置および炭化水素系燃料の燃焼装置を熱発生源として具備する装置 - Google Patents
炭化水素系燃料の燃焼装置および炭化水素系燃料の燃焼装置を熱発生源として具備する装置 Download PDFInfo
- Publication number
- WO2007129604A1 WO2007129604A1 PCT/JP2007/059159 JP2007059159W WO2007129604A1 WO 2007129604 A1 WO2007129604 A1 WO 2007129604A1 JP 2007059159 W JP2007059159 W JP 2007059159W WO 2007129604 A1 WO2007129604 A1 WO 2007129604A1
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- WO
- WIPO (PCT)
- Prior art keywords
- flame
- combustion furnace
- combustion
- oxygen
- containing gas
- Prior art date
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C3/00—Combustion apparatus characterised by the shape of the combustion chamber
- F23C3/002—Combustion apparatus characterised by the shape of the combustion chamber the chamber having an elongated tubular form, e.g. for a radiant tube
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C3/00—Combustion apparatus characterised by the shape of the combustion chamber
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01G—HORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
- A01G9/00—Cultivation in receptacles, forcing-frames or greenhouses; Edging for beds, lawn or the like
- A01G9/24—Devices or systems for heating, ventilating, regulating temperature, illuminating, or watering, in greenhouses, forcing-frames, or the like
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C99/00—Subject-matter not provided for in other groups of this subclass
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D11/00—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
- F23D11/24—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space by pressurisation of the fuel before a nozzle through which it is sprayed by a substantial pressure reduction into a space
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D17/00—Burners for combustion conjointly or alternatively of gaseous or liquid or pulverulent fuel
- F23D17/002—Burners for combustion conjointly or alternatively of gaseous or liquid or pulverulent fuel gaseous or liquid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23M—CASINGS, LININGS, WALLS OR DOORS SPECIALLY ADAPTED FOR COMBUSTION CHAMBERS, e.g. FIREBRIDGES; DEVICES FOR DEFLECTING AIR, FLAMES OR COMBUSTION PRODUCTS IN COMBUSTION CHAMBERS; SAFETY ARRANGEMENTS SPECIALLY ADAPTED FOR COMBUSTION APPARATUS; DETAILS OF COMBUSTION CHAMBERS, NOT OTHERWISE PROVIDED FOR
- F23M9/00—Baffles or deflectors for air or combustion products; Flame shields
- F23M9/06—Baffles or deflectors for air or combustion products; Flame shields in fire-boxes
Definitions
- Hydrocarbon fuel combustion apparatus and apparatus comprising a hydrocarbon fuel combustion apparatus as a heat generation source
- the present invention relates to a hydrocarbon fuel combustion apparatus and a hydrocarbon fuel combustion apparatus as a heat generation source. More specifically, the present invention relates to a hydrocarbon fuel combustion device that enables effective use of fuel by completely burning hydrocarbon fuel and a device that includes a hydrocarbon fuel combustion device as a heat generation source.
- the injection nozzle of the gun type burner 102 is disposed in a large-diameter combustion furnace 104.
- the combustion furnace 104 is heated to a high temperature by the combustion gas filled in the combustion furnace 104, and the high-temperature combustion exhaust gas is passed through the pipe of the heat exchanger 107, and the combustion furnace 104 and the heat exchanger 107 are passed through.
- Hot air that has been subjected to heat exchange by blowing air from the blower fan 105 is sent into the house 103.
- the heat-exhausted exhaust gas in the combustion furnace 104 is exhausted outside the house by the chimney 106 (see Reference 1).
- Patent Document 1 JP 2002-34355 A
- the combustion furnace has a large diameter in order to increase the heat exchange rate, but in the case of a gun type burner, when liquid fuel is ejected in a mist form from the nozzle and burned, Since a considerable part of the liquid fuel does not burn but adheres to the inner surface of the combustion furnace and becomes incompletely combusted, toxic gases such as carbon monoxide and volatilized unburned substances move out of the house. It will be exhausted, and harmful substances will be released to the outside air, which will adversely affect the environment. Moreover, if such exhaust gas is discharged into the house, it may be harmful to the growth of plants, harm the health of people working in the house, or cause a carbon monoxide poisoning accident.
- the outer surfaces of the combustion furnace and the heat exchanger are heat-exchanged by blowing air from a fan, but the combustion gas is released from the chimney into the outside air at a high temperature.
- the heat exchange rate is very low and the fuel consumption is very bad.
- some sauna heating devices have a structure in which the exhaust pipe has a meandering structure so as to completely burn and improve heat exchange efficiency.
- a burner that can be used in this apparatus The size of the flame injection nozzle is limited to a small one, and the temperature inside the furnace is estimated to be around 400 ° C at best.
- black smoke is generated when the size of the flame injection nozzle is forcibly increased, and the complete combustion state cannot be maintained.
- a hydrocarbon-based fuel combustion apparatus includes a flame injector that is supplied with a fuel source fuel and has a flame injection nozzle attached to the front end.
- a blower that sends out oxygen-containing gas composed of oxygen or oxygen-containing gas, and a blower pipe that surrounds the flame injector from the blower and extends forward concentrically with the axial direction of the flame injection nozzle.
- a carbonization furnace provided with a cylindrical combustion furnace in which a flame is injected from the flame injection nozzle, one end is connected to the burner, and an exhaust port is provided at the other end or in the vicinity of the other end.
- the blower sends out the oxygen-containing gas only into the combustion furnace through the blower pipe, and the flame injector injects the flame only into the combustion furnace, and the blower From send
- the oxygen-containing gas thus discharged is exhausted only from the exhaust port, and the length of the combustion furnace is such that the position of the front end of the flame is inside the combustion furnace from the position of the exhaust port, and the length of the front end of the flame
- a sufficient distance to provide a predetermined distance between the position and the position of the exhaust port, and the inner diameter of the combustion furnace is a value not less than a minimum value in a range not in contact with the flame and a value in the vicinity thereof,
- the area from the flame tip to the exhaust port in the combustion furnace The flow path of the oxygen-containing gas is narrowly limited at one or more locations in the region.
- the combustion furnace has a narrow space. Because the hydrocarbon-based fuel will burn, the following four effects can be obtained and the above-mentioned problems can be solved. That is, first, when a liquid fuel is sprayed in a mist form from a nozzle with a gun-type burner and burned, a considerable part of the liquid fuel does not burn but adheres to the inner surface of the combustion furnace. Because of the high temperature in the immediate vicinity, the adhering liquid fuel will immediately vaporize and ignite and burn on the spot.
- the oxygen-containing gas delivered from the burner passes through a position far from the flame and is discharged outside the furnace without being used for combustion.
- oxygen in the oxygen-containing gas that passes near the flame is burned and consumed rapidly, so the oxygen concentration in the vicinity of the flame may be low.
- the oxygen-containing body sent out from the burner Since all of them pass through the immediate vicinity of the flame, the oxygen concentration in the vicinity of the flame is kept higher than in the case of a conventional large-diameter combustion furnace, and the use efficiency of oxygen for combustion is remarkably improved.
- the combustion furnace is a narrow space, the temperature inside the combustion furnace easily becomes high and complete combustion is further promoted.
- the oxygen-containing gas flow path is narrowly restricted at one or more locations in the combustion furnace from one end of the flame to the exhaust port.
- the flow of the flowing oxygen-containing gas is suppressed and the atmospheric pressure inside the combustion furnace is increased, and the four effects detailed in [0009] are further promoted, and the temperature in the furnace is higher than 800 ° C.
- Combustion is also possible, so that even if the size of the burner flame injection nozzle is increased, the complete combustion state and the high-temperature preheated air combustion state can be maintained.
- toxic gases such as volatilized and unburned substances, the generation of Nx can be suppressed.
- a hydrocarbon-based fuel combustion apparatus includes at least a partial region in a region from the flame tip to the exhaust port in the combustion furnace.
- the flow direction of the oxygen-containing gas in is configured to be substantially opposite to the reverse direction of the oxygen-containing gas by the blower.
- the fuel is combusted when ejected in a mist form from the nozzle and burned.
- the hydrocarbon fuel adhering to the inner surface of the combustion furnace without burning is completely burned, and it is possible to suppress not only toxic gases such as carbon monoxide and volatilized unburned substances but also NOx. .
- the hydrocarbon fuel is a mixture of one or a plurality of hydrocarbon fuels selected from crude oil, heavy oil, kerosene, light oil, jet fuel, gasoline, naphtha, LPG, and LNG. Although it is used as a fuel, it can produce a remarkable effect especially when kerosene or light oil is used.
- a hot air boiler for a greenhouse as an apparatus including the hydrocarbon-based fuel combustion apparatus having the above configuration as a heat generation source, and the combustion gas exhausted from the combustion furnace is used as hot air. By using it together, the amount of fuel used can be greatly reduced. The invention's effect
- the inner diameter of the combustion furnace is a value not less than a minimum value in a range not in contact with the flame by the burner and a value in the vicinity thereof, and the inside of the combustion furnace
- the internal pressure of the combustion furnace is increased.
- the combustion temperature in the inside is 800 ° C or higher, realizing a combustion state similar to the combustion state called high-temperature preheated air combustion, carbon monoxide, volatilized unburned substances, etc. by complete combustion even when the oxygen concentration is low It is possible to suppress the generation of harmful substances such as Nx as well as toxic gases.
- the flow direction of the oxygen-containing gas in at least a partial region in the region from the flame front end to the exhaust port in the combustion furnace is substantially opposite to the oxygen-containing gas delivery direction by the blower.
- the internal pressure in the combustion furnace is increased more effectively, and a combustion state similar to the combustion state called high-temperature preheated air combustion is realized, and complete combustion is possible even when the oxygen concentration is low. .
- the hydrocarbon fuel combustion apparatus according to the present invention is provided as a hot air boiler, the combustion gas in which the generation of toxic substances is suppressed is discharged into the greenhouse as hot air.
- the heat exchange rate is increased and the fuel consumption is remarkably improved.
- FIG. 1 is a side view for illustrating an example of a hydrocarbon fuel combustion apparatus to which the present invention is applied.
- FIG. 2 is a side view for explaining another example of a hydrocarbon fuel combustion apparatus to which the present invention is applied.
- FIG. 3 is an explanatory side view illustrating another example of the exhaust port installation mechanism in claim 1 of a hydrocarbon fuel combustion apparatus to which the present invention is applied.
- FIG. 4 is an explanatory side view showing another example of the exhaust port installation mechanism in claim 2 of the hydrocarbon fuel combustion apparatus to which the present invention is applied.
- FIG. 5 is an explanatory side view illustrating an example of a hot air boiler provided with the combustion device in FIG. 1.
- FIG. 6 is a side view illustrating another example of a hot air boiler equipped with the combustion device in FIG.
- FIG. 1 is an explanatory diagram illustrating an example of a hydrocarbon fuel combustion apparatus to which the present invention is applied.
- FIG. 2 is an explanatory diagram for illustrating another example of a hydrocarbon fuel combustion apparatus to which the present invention is applied.
- the combustion apparatus 1 shown here includes a cylindrical combustion furnace 2 having a total length of 1500 mm and an inner diameter of 250 mm, It is composed of a gun type burner 4 connected to one end 3 of the combustion furnace 2.
- the burner 4 is supplied with fuel (for example, kerosene fuel) from a fuel source, and has a flame injector 5 having a flame injection nozzle 20 mounted at the front end thereof, and an oxygen-containing gas composed of oxygen or a gas containing oxygen.
- a blower 6 to be sent out and a blower pipe 7 surrounding the flame injector 5 from the blower 6 and extending forward concentrically with the axial direction of the flame injection nozzle 20 are configured.
- the combustion furnace 2 is connected in a state of protruding toward the other end 8 of the combustion furnace 2 on the concentric axis, and the other end 8 of the combustion furnace 2 has an inner diameter of 100 mm and has an exhaust port 21 at the upper side.
- the exhaust pipe 9 having
- the flow path of the oxygen-containing gas is narrowly limited in a region from the tip of the flame injected from the flame injection nozzle 20 installed in the combustion furnace 2 to the other end of the combustion furnace 2.
- a projection 10 for projecting is provided along the inner peripheral surface of the combustion furnace 2.
- the flow path of the oxygen-containing gas in the region from the front end of the flame injected from the flame injection nozzle 20 installed in the combustion furnace 2 to the exhaust port 21 is the protrusion 10 and
- the exhaust pipe 9 connected to the other end of the combustion furnace 2 is narrowly limited.
- only the flame injector 4 and the blower pipe 7 of the burner 4 are installed in the combustion furnace 2 at one end 3 of the combustion furnace 2 having an inner diameter of 300 mm, and the flame injection
- the flame injection nozzle of the combustor is connected in a state of projecting toward the open end of the combustion furnace 2 on the concentric axis of the combustion furnace 2, and an exhaust pipe having an inner diameter of 200 mm is connected to the other end 8 of the combustion furnace 2.
- 9 is connected, and the exhaust pipe 9 is bent 180 degrees so that the flow direction of the oxygen-containing gas flowing through the interior of the exhaust pipe 9 and the oxygen-containing gas flowing through the combustion furnace 2 are opposite to each other.
- the exhaust pipe 9 is bent 180 degrees so that the flow directions of the oxygen-containing gas and the oxygen-containing gas flowing in the reverse direction are reversed. Further, in the region from the tip of the flame injected from the flame injection nozzle 20 installed in the combustion furnace 2 to the other end 8 of the combustion furnace 2 and in the region of the exhaust pipe 9, Because the gas flow path is narrowly restricted The projecting portion 10 is projected along the inner peripheral surface of the combustion furnace 2 and the inner peripheral surface of the exhaust pipe 9.
- the flow path of the oxygen-containing gas is the other end of the combustion furnace 2 in the region from the front end of the flame injected from the flame injection nozzle installed in the combustion furnace 2 to the exhaust port 21.
- the exhaust pipe 9 and the projection 10 connected to 8 are narrowly limited, and the flow of the oxygen-containing gas in at least a partial region up to the exhaust tip force of the flame in the combustion furnace is determined by the blower.
- the direction is substantially opposite to the direction of delivery of the oxygen-containing gas.
- the blower 6 of the burner 4 sends out oxygen-containing gas (air) only through the blower pipe 7 into the combustion furnace 2 and the flame injector 5 is used as the combustion furnace 2.
- the flame is injected only into the inside, and the combustion gas due to the oxygen-containing gas and the flame is discharged from the exhaust port 21 of the exhaust pipe 9 connected to the other end 8 of the combustion furnace 2.
- the flame injector and the blower pipe 7 of the burner 4 are installed in the combustion furnace 2 at one end of the combustion furnace 2, and the flame injector
- the flame injection nozzle is connected on the concentric axis of the combustion furnace 2 so as to protrude toward the other end 8 of the combustion furnace 2, and the other end 8 is sealed and in the vicinity of the other end 8.
- the exhaust port 21 is opened on the outer wall surface of the combustion furnace 2, and the exhaust port 21 of the combustion furnace 2 from the front end of the flame injected from the flame injection nozzle 20 installed in the combustion furnace 2.
- the protrusion 10 for narrowly limiting the flow path of the oxygen-containing gas may be configured to protrude along the inner peripheral surface of the combustion furnace 2.
- the oxygen-containing gas is exhausted from the exhaust port 21 to the outer wall surface of the combustion furnace 2 in the vicinity of the other end 8, and is injected from the flame injection nozzle installed in the combustion furnace 2.
- the flow path of the oxygen-containing gas is narrowly limited by the protrusion 10 and the exhaust port 21 in the region from the front end of the flame to the exhaust port 21.
- FIG. 3 mouth
- only one flame injector of the burner 4 and a blower pipe 7 are installed in the combustion furnace 2 at one end 3 of the combustion furnace 2, and the flame injection
- the flame injection nozzle of the chamber is connected in a state of projecting toward the other end 8 of the combustion furnace 2 on the concentric axis of the combustion furnace 2, and the open end of the other end 8 is connected to the oxygen from the periphery thereof.
- Content A structure may be provided in which a lid 22 is formed in which an exhaust port 21 through which the body is discharged is formed.
- the oxygen-containing gas is exhausted from the exhaust port 21 formed in the vicinity of the lid 22 installed at the opening end of the other end 8, and is installed in the combustion furnace 2.
- the flow path of the oxygen-containing gas is narrowly limited in the region from the tip of the flame injected from the flame injection nozzle to the exhaust port 21.
- only the flame injector 4 of the burner 4 and the blower pipe 7 are installed in the combustion furnace 2 at one end 3 of the combustion furnace 2, and the flame of the flame injector
- An injection nozzle is connected on the concentric axis of the combustion furnace 2 so as to protrude toward the other end 8 of the combustion furnace 2, and the front end force of the flame in the combustion furnace 2 is exhausted at the other end 8.
- the flow direction of the oxygen-containing gas in at least a part of the region up to is formed in a state where the oxygen-containing gas is bent at about 180 degrees so that the oxygen-containing gas is sent in a direction substantially opposite to the direction in which the flame-injector sends the oxygen-containing gas.
- the front end force of the flame injected from the flame injection nozzle 20 installed in the combustion furnace 2 is limited to a narrow flow path for the oxygen-containing gas in the region up to the other end 8 of the combustion furnace 2. Are projected along the inner peripheral surface of the combustion furnace 2. It is good also as a structure.
- the flow path of the oxygen-containing gas is narrowly limited by the protrusion 10 in the region from the front end of the flame injected from the flame injection nozzle installed in the combustion furnace 2 to the exhaust port 21.
- the flow direction of the oxygen-containing gas in at least a partial region from the flame tip to the exhaust port in the combustion furnace is substantially opposite to the oxygen-containing gas delivery direction by the blower. .
- the inner diameter of each of the combustion furnaces 2 shown above is a value not less than the minimum value in the range where it does not contact the flame A injected from the flame injection nozzle, and a value in the vicinity thereof.
- the outer diameter of the flame A varies depending on the size of the flame injection nozzle, for example, the inner diameter of the combustion furnace 2 is 150 mm to 250 mm when the size of the flame injection nozzle is changed from 0.5 gal / hour to 2.0 gallon Z time. Within range.
- the length of the combustion furnace 2 is such that the position of the tip of the flame A is the position 8 before the other end of the combustion furnace 2, specifically, the tip of the flame A is It is desirable that the length of one end 3 of the combustion furnace 2 be a position that is within a total length 2Z3.
- flame The total length of the combustion furnace 2 should be in the range of 600mm to 4000mm when the size of the gun nose is changed from 0.5 gallon / hour to 2.0 gallon / hour.
- the flow path of the oxygen-containing gas is narrowly limited, whereby the pressure inside the combustion furnace 2 is set.
- the furnace temperature is 800 ° C or higher
- a complete combustion state and a high-temperature preheated air combustion state can be maintained. Therefore, not only toxic gases such as carbon monoxide and volatilized unburned substances, but also the generation of NOx can be suppressed.
- the inside of the combustion furnace 2 The flow direction of the oxygen-containing gas in at least a partial region in the region from the front end of the flame to the exhaust port 21 is substantially opposite to the delivery direction of the oxygen-containing gas by the blower 6.
- the flow of the oxygen-containing gas flowing in the exhaust pipe 9 will be further suppressed, and it is further encouraged to increase the pressure inside the combustion furnace 2, and the furnace temperature is a high temperature state of 800 ° C or higher.
- FIG. 5 shows a hot-air boiler equipped with a hydrocarbon fuel combustion apparatus to which the present invention is applied.
- FIG. 6 is an explanatory view showing an example, and FIG. 6 is an explanatory view showing another example of a hot air boiler equipped with a hydrocarbon fuel combustion apparatus to which the present invention is applied.
- the hot air boiler 11 shown here includes the combustion device 1 shown in FIG. 1 or the combustion device storage case 12 in which the combustion device 1 shown in FIG. 2 is stored, and the upper end of the combustion device storage case 12
- the blower fan 13 is provided on the side of the combustion apparatus case 12 and the hot air outlet 14 is opened on the side of the combustion apparatus case 12.
- the air outside the combustion device storage case 12 is taken into the combustion device storage case 12 by the suction side of the blower fan 13.
- the taken-in air is a mixture of the combustion gas exhausted from the exhaust pipe 9 of the combustion apparatus 1 and the air heat-exchanged by contacting the outer surface of the combustion furnace 2 and the exhaust pipe 9 of the combustion apparatus 1. Warm air from the gas is sent out from the hot air outlet 14.
- a conventional hot air boiler uses a 4 gallon / hour injection nozzle
- a hot air boiler according to the present invention uses a 1.2 gallon / hour injection nozzle.
- the hot air boiler of this invention was performed by the same ventilation volume.
- the size of the flame injection nozzle of the conventional hot air boiler is 4 gallons / hour, and the size of the flame injection nozzle of the hot air boiler of the present invention is 1.2 gallons / hour.
- the air temperature is 3 ° C lower than conventional hot air boilers It just becomes. This is presumed that the boiler of the present invention has a high heat exchange rate by using all the combustion gas from the combustion furnace as hot air.
- the daily fuel consumption of the conventional hot air boiler is 182 liters, whereas the daily fuel consumption of the hot air boiler of the present invention is 92 liters. It became possible to reduce to about one-half.
- the burner nozzle size was 2.5 gallons / hour for both.
- the temperature in the conventional combustion furnace is 680 ° C, and the combustion gas has a high Nx concentration as well as toxic gases such as carbon monoxide and volatilized unburned substances. It could not be used as hot air and had to be exhausted outside the greenhouse by a chimney.
- the temperature in the combustion furnace of the present invention is 813 ° C, and no toxic gases such as carbon monoxide and volatilized unburned substances and NOx are detected in the combustion gas, and they are sent into the vinyl house as hot air. It became possible to do.
- the inner diameter of the combustion furnace is not less than the minimum value in the range where it does not come into contact with the flame by the burner, and a value in the vicinity thereof, and the flow of oxygen-containing gas in the region from the flame front to the open end in the combustion furnace
- fuel for example, kerosene fuel
- the combustion furnace at 800 ° C or higher can be completely burned, so that carbon monoxide and volatilized Generation of toxic gases such as combustion substances and NOx can be suppressed.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental Sciences (AREA)
- Combustion Of Fluid Fuel (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2008514447A JP4385080B2 (ja) | 2006-05-01 | 2007-04-27 | 炭化水素系燃料の燃焼装置および炭化水素系燃料の燃焼装置を熱発生源として具備する装置 |
EP07742594A EP2017528A1 (en) | 2006-05-01 | 2007-04-27 | Combustor of hydrocarbon based fuel and device comprising combustor of hydrocarbon based fuel as heat generation source |
CN2007800158102A CN101432573B (zh) | 2006-05-01 | 2007-04-27 | 热风锅炉 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2006-127749 | 2006-05-01 | ||
JP2006127749 | 2006-05-01 |
Publications (1)
Publication Number | Publication Date |
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WO2007129604A1 true WO2007129604A1 (ja) | 2007-11-15 |
Family
ID=38667712
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/JP2007/059159 WO2007129604A1 (ja) | 2006-05-01 | 2007-04-27 | 炭化水素系燃料の燃焼装置および炭化水素系燃料の燃焼装置を熱発生源として具備する装置 |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP2017528A1 (ja) |
JP (1) | JP4385080B2 (ja) |
KR (1) | KR101071660B1 (ja) |
CN (1) | CN101432573B (ja) |
WO (1) | WO2007129604A1 (ja) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
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FR2977562B1 (fr) | 2011-07-06 | 2016-12-23 | Gaztransport Et Technigaz | Cuve etanche et thermiquement isolante integree dans une structure porteuse |
CN110146643A (zh) * | 2018-02-13 | 2019-08-20 | 中国石油化工股份有限公司 | 模拟烃类火的实验装置 |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS4732765Y1 (ja) * | 1968-11-09 | 1972-10-03 | ||
JPS49298Y1 (ja) * | 1969-06-11 | 1974-01-07 | ||
JPH03211307A (ja) * | 1990-01-16 | 1991-09-17 | Matsushita Electric Ind Co Ltd | 燃焼装置 |
JPH094816A (ja) * | 1995-06-16 | 1997-01-10 | Sanyo Electric Co Ltd | 燃料噴霧式燃焼装置 |
JPH11248255A (ja) * | 1998-03-02 | 1999-09-14 | Fulta Electric Machinery Co Ltd | 農事用のハウスヒーター |
JP2002034355A (ja) | 2000-07-21 | 2002-02-05 | Sansyu Sangyo Co Ltd | 施設園芸ハウス用温風暖房機 |
JP2003222314A (ja) * | 2002-01-30 | 2003-08-08 | Takahashi Kikan:Kk | バーナー |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5392233A (en) * | 1977-01-17 | 1978-08-12 | Ishikawajima Harima Heavy Ind | Heater for farming |
JPS59183631A (ja) * | 1983-03-31 | 1984-10-18 | サンレ−冷熱株式会社 | ハウス栽培に於けるco↓2施用方法 |
-
2007
- 2007-04-27 CN CN2007800158102A patent/CN101432573B/zh not_active Expired - Fee Related
- 2007-04-27 KR KR1020087029332A patent/KR101071660B1/ko not_active IP Right Cessation
- 2007-04-27 EP EP07742594A patent/EP2017528A1/en not_active Withdrawn
- 2007-04-27 JP JP2008514447A patent/JP4385080B2/ja not_active Expired - Fee Related
- 2007-04-27 WO PCT/JP2007/059159 patent/WO2007129604A1/ja active Application Filing
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4732765Y1 (ja) * | 1968-11-09 | 1972-10-03 | ||
JPS49298Y1 (ja) * | 1969-06-11 | 1974-01-07 | ||
JPH03211307A (ja) * | 1990-01-16 | 1991-09-17 | Matsushita Electric Ind Co Ltd | 燃焼装置 |
JPH094816A (ja) * | 1995-06-16 | 1997-01-10 | Sanyo Electric Co Ltd | 燃料噴霧式燃焼装置 |
JPH11248255A (ja) * | 1998-03-02 | 1999-09-14 | Fulta Electric Machinery Co Ltd | 農事用のハウスヒーター |
JP2002034355A (ja) | 2000-07-21 | 2002-02-05 | Sansyu Sangyo Co Ltd | 施設園芸ハウス用温風暖房機 |
JP2003222314A (ja) * | 2002-01-30 | 2003-08-08 | Takahashi Kikan:Kk | バーナー |
Also Published As
Publication number | Publication date |
---|---|
JP4385080B2 (ja) | 2009-12-16 |
EP2017528A1 (en) | 2009-01-21 |
JPWO2007129604A1 (ja) | 2009-09-17 |
CN101432573A (zh) | 2009-05-13 |
KR101071660B1 (ko) | 2011-10-11 |
CN101432573B (zh) | 2011-11-09 |
KR20090009284A (ko) | 2009-01-22 |
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