US20120100497A1 - Burner using plasma - Google Patents
Burner using plasma Download PDFInfo
- Publication number
- US20120100497A1 US20120100497A1 US13/380,701 US201013380701A US2012100497A1 US 20120100497 A1 US20120100497 A1 US 20120100497A1 US 201013380701 A US201013380701 A US 201013380701A US 2012100497 A1 US2012100497 A1 US 2012100497A1
- Authority
- US
- United States
- Prior art keywords
- combustion
- mixture fuel
- supply pipe
- tank
- direct current
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/05—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste oils
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D91/00—Burners specially adapted for specific applications, not otherwise provided for
-
- 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
- F23D11/10—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour
- F23D11/16—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour in which an emulsion of water and fuel is sprayed
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/34—Burners specially adapted for use with means for pressurising the gaseous fuel or the combustion air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/38—Torches, e.g. for brazing or heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
- F23L7/002—Supplying water
- F23L7/005—Evaporated water; Steam
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05H—PLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
- H05H1/00—Generating plasma; Handling plasma
- H05H1/24—Generating plasma
- H05H1/48—Generating plasma using an arc
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2204/00—Supplementary heating arrangements
- F23G2204/20—Supplementary heating arrangements using electric energy
- F23G2204/201—Plasma
Definitions
- the present invention relates to a burner using plasma in which a mixture fuel can be used as a combustion fuel, thus heating a boiler or the something with a cheaper fuel, with the mixture fuel being made by mixing water and industrial waste oil at a proper ratio.
- the present invention is basically directed to using a burner using plasma characterized in that a combustion tank helping spray a mixture fuel via a nozzle and combust the same is designated as a positive electrode (+), and a rod installed at one side of the same is designated as a negative electrode ( ⁇ ), thus receiving a DC (Direct Current) electricity of a DC electricity supply part, and a steam supply pipe is installed, so a mixture fuel supply pipe surrounding a combustion tank in a coil shape can be heated or preheated in such a way to heat an inner wall of the combustion tank by means of a high temperature plasma flame of above 800° C.
- a combustion tank helping spray a mixture fuel via a nozzle and combust the same is designated as a positive electrode (+)
- ⁇ negative electrode
- a fuel in a combustion chamber with the aid of a flame generation of a high temperature steam plasma torch from a steam supply pipe, and a fuel can be supplied at a pressure above 50 atm by a high pressure pump as a nozzle of a mixture fuel supply pipe is ignited, so the mixture can be more effectively combusted as compared to a simply spray combustion which uses a nozzle in a combustion chamber of a combustion tank owing to a high pressure and a high temperature of above 800° C., and a more continuous, safer combustion might be achieved at a lower cost in the event that a plasma torch part is used together.
- the oil burner generally used at a boiler or the something is designed to use a relatively expensive fuel oil and to spray via a nozzle in a mist form, thus combusting the fuel; however the maintenance of the boiler is costly which leads to a higher economic burden to a user.
- an industrial water oil is being suggested as a fuel; however the production of the industrial waste oil is very limited, thus limiting its actual application. Since diverse contaminations are contained in the waste oil, without a high temperature combustion, a harmful gas generated during an incomplete combustion could contaminate air. When it is needed to properly process such harmful gas, a high temperature heat decomposition process is needed at each step, and the industrial waste oil is needed to be processed in a mixing chamber which decomposes the oil into O 2 , H and OH-group, and the serious contamination substances contained in the waste oil can be stabilized using hydrogen fluoride, hydrogen chloride, CO 2 , etc; however the decomposition process system of such serious contamination substances require very expensive further facilities and high operation costs, which substantially retards the applications.
- a burner using plasma characterized in that a combustion tank in which a mixture fuel supply pipe is wound in a coil shape around an outer surface of a cylindrical combustion tank with its both sides open, is designated as a positive electrode part, and a rod installed at an outer side of the same is designated as a negative electrode, thus receiving a direct current electricity from a direct current supply part, and a plasma torch part is configured in such a way that a steam supply pipe designed to receive steam from a steam generation part is installed between the combustion tank and the negative part, thus generating a high temperature steam plasma flame in the combustion chamber.
- the flame in the combustion chamber of the combustion tank which is a high temperature steam plasma torch flame of above 800° C.
- the mixture fuel supplied at a high pressure of above 50 atm from the high pressure pump can be well sprayed in a mist state and can be well combusted with the aid of a high pressure at the nozzle and a high temperature above 800° C., which leads to a complete combustion.
- the burner using plasma according to the present invention is characterized in that a combustion tank 1 configured in such a way that a mixture fuel supply pipe 3 is wound in a coil shape on an outer surface of a combustion tank 1 , is designated as a positive electrode part 7 , and a rod engaged at an outer side of the same is designated as a negative electrode part 8 , so a direct current electricity is supplied from a direct current electricity supply part 6 , and a steam supply pipe 13 serving to receive steam from the steam generation part 12 is disposed between the combustion tank 1 and the negative electrode part 8 , thus forming a plasma torch part 9 , so a flame of a high temperature steam plasma torch is generated in the combustion chamber 11 of the combustion tank 1 .
- a high temperature plasma flame can be generated at a high temperature of above 800° C., and since the inner wall of the combustion tank is heated and consequently preheated, the mixture fuel can be supplied at a high pressure of above 50 atm, and the water is decomposed into hydrogen and oxygen in the mixture fuel supply pipe 3 , and the waste oil is decomposed into carbon components.
- a high heat is generated and is burnt on the basis of complete combustion.
- the mixture fuel combustion in the combustion tank 1 helps to perform a preheating combustion and to adjust the combustion state with the aid of the operation of the plasma torch part 9 , thus always achieving complete combustion, and the water in the mixture fuel is decomposed into hydrogen and oxygen, and the waste oil therein is decomposed into carbon components, so the air contamination due to the waste oil can be significantly filtered and prevented, thus achieving an economically advantageous effect.
- FIG. 1 is a cross sectional view illustrating the entire construction of a burner using plasma according to the present invention
- FIG. 2 is a cross sectional view illustrating a combustion tank according to the present invention
- FIG. 3 is a side view illustrating parts of an argon gas exhaust pipe and a negative electrode part according to the present invention.
- FIG. 4 is a side view illustrating part of a steam supply pipe according to the present invention.
- combustion tank 3 mixture fuel supply pipe 6: direct current electricity supply part 7: positive electrode part 8: negative electrode part 11: combustion chamber 12: steam generation part 13: steam supply pipe
- FIG. 1 is a cross sectional view illustrating the entire construction of a burner using plasma according to the present invention
- FIG. 2 is a cross sectional view illustrating a combustion tank according to the present invention
- FIG. 3 is a side view illustrating parts of an argon gas exhaust pipe and a negative electrode part according to the present invention
- FIG. 4 is a side view illustrating part of a steam supply pipe according to the present invention.
- the present invention is characterized in that heat is collected via a combustion tank 1 formed by winding a mixture fuel supply pipe 3 in a coil shape on an outer surface of the combustion tank 1 as a mixture fuel made by well mixing, with a mixer, water and waste oils is supplied by a high pressure pump 10 to an outer surface of a cylindrical tank 10 with its both sides open.
- the inner end of the mixture fuel supply pipe 3 is connected to a nozzle 4 installed in the combustion chamber 11 , and the mixture fuel is supplied via the nozzle 4 to the mixture fuel supply pipe 3 at a high pressure of above 50 atm with the aid of the high pressure pump 10 , so the mixture fuel is sprayed into the combustion chamber 11 via the spray holes of the nozzle 4 in a mist form, thus achieving a high temperature combustion.
- a heat insulation cover 2 is covered on an outer side of the mixture fuel supply pipe 3 for the mixture fuel supply pipe 3 to fully receive the combustion heat of the combustion chamber 11 and the heat of a high temperature steam plasma, and a combustion air tank 5 is installed in such a way to cover the entire outer portions of the nozzle 4 for an external air to be inputted from the pump 10 ′ at an outer side of the nozzle 4 , thus air cooling the nozzle 4 , and the combustion air is forced to circulate in the combustion chamber 11 , so enough amount of air injection and combustion flame circulate in the interior of the combustion chamber 11 and is discharged to the outside.
- the combustion tank 1 is designated as a positive electrode part 7 , with the combustion tank 1 electrically conducting a positive electricity(+) from the direct current electricity supply part 6 so as to form the combustion tank 1 with a plasma torch part, and the rod electrically conducting a negative electricity ( ⁇ ) from the direct current electricity supply part 6 is designated as a negative electrode part 8 , thus forming a plasma torch part 9 .
- a steam supply pipe 13 serving to receive a high temperature steam from the steam generation part 12 is secured between the side wall of the combustion tank 1 and the plasma torch part 9 , thus supplying a direct current electricity, and in the mode of activation, a steam in a form of mist and a steam plasma flame are generated in the plasma torch part 9 over the combustion chamber 11 , thus generating a high temperature plasma flame of above 800° C.
- An argon gas exhaust pipe 15 is connected to the negative electrode part 8 formed of a rod, in order to prevent a corrosion and transformation of the rod of the negative electrode part 8 for thereby receiving an argon gas from the argon gas supply part 14 .
- reference numeral 16 represents an igniter.
- the operation of the burner using plasma according to the present invention is as follows.
- a high temperature steam of the steam generator 12 is provided in a form of mist via the steam supply pipe 13 , so a high temperature steam plasma flame is generated at the plasma torch part 9 .
- the plasma flame of above 800° C. heats the inner wall of the combustion tank 1 on which the mixture fuel supply pipe 3 is wound, thus performing a preheating process of the spray combustion of the nozzle 4 .
- the water contained in the mixture fuel is decomposed into hydrogen and oxygen by means of the preheating of the mixture fuel supply pipe 3 wound on the outer surface of the combustion tank 1 , and the waste oil is decomposed into very small carbon components, thus generating a high temperature when passing through the nozzle 4 , and the mixture fuel of the mixture fuel supply pipe 3 is supplied in a state of a high pressure above 50 atm increased by means of the high pressure pump 10 , so the mixture fuel can be completely combusted with the aid of a high pressure above 50 atm and a high temperature of above 800° C. in the combustion chamber 11 .
- enough preheating is performed by means of the plasma flame generation in the combustion tank 1 , and when the mixture fuel is sprayed in a form of mist via the spray holes of the nozzle 4 , and the spray combustion is performed, the direct current electricity supply of the direct current electricity supply part 6 is stopped, thus stopping the generation of plasma flame, and the mixture fuel is continuously supplied at a high pressure above 50 atm to the combustion chamber 11 via the nozzle 4 by means of the high pressure pump 10 , thus performing a continuously high temperature combustion.
- an external combustion air circulates via the combustion air tank 5 installed outside the nozzle 4 by means of the pump 10 ′, and the nozzle 4 is continuously cooked, so the safety combustion of the nozzle 4 is achieved, and the external combustion air injected into the combustion chamber 11 by means of the pump 10 ′ circulates in the combustion chamber 11 along with the combustion flame with the aid of the construction that the passage of the combustion air tank 5 is formed in a screw shape, thus continuously contact-heating the inner wall of the combustion tank 1 .
- the mixture fuel of the mixture fuel supply pipe 3 continues to burn at a high temperature in the combustion chamber 11 along with the preheating.
- the heating to a higher temperature by means of the mixture fuel spray combustion by the nozzle 4 and the generation of a high temperature plasma flame can be adjusted by adjusting the supply of the direct current electricity of the direct current supply part 9 , so a safe, easy use of the burner using plasma can be achieved.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Plasma & Fusion (AREA)
- Environmental & Geological Engineering (AREA)
- Spectroscopy & Molecular Physics (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Spray-Type Burners (AREA)
Abstract
The present invention relates to a burner using plasma, which uses a mixture fuel in which water and industrial waste oil are mixed at an appropriate ratio. A combustion tank has a positive electrode (+), a rod installed at one side of the combustion tank has a negative electrode (−), and direct current electricity is supplied to the combustion tank and to the rod from a direct current electricity supply unit. A steam supply pipe of a steam generator is installed together with a plasma torch unit which is coupled to the combustion tank, such that high-temperature steam is discharged from the steam supply pipe together with the plasma torch generated by the plasma torch unit. Thus, the high-temperature plasma torch generates a high-temperature plasma flame of 800° C. or higher to heat a combustion chamber at the inner wall of the combustion tank. A mixture fuel supply pipe is wound into a coil on the outer surface of the combustion chamber, such that the mixture fuel supply pipe is preheated by high-temperature heat. The mixture fuel in the mixture fuel supply pipe is supplied at an air pressure of 50 through a high pressure pump, and water in the mixture fuel is decomposed into hydrogen and oxygen and waste oil in the mixture fuel is decomposed into carbons. The mixture fuel is injected or sprayed through a nozzle at a high temperature to effectively and completely burn the mixture fuel. The plasma torch unit operates by means of the direct current electricity supplied by the direct current electricity supply unit if needed, to adjust the temperature of the combustion chamber of the combustion tank, thereby enabling the smooth use of the burner.
Description
- The present invention relates to a burner using plasma in which a mixture fuel can be used as a combustion fuel, thus heating a boiler or the something with a cheaper fuel, with the mixture fuel being made by mixing water and industrial waste oil at a proper ratio.
- The present invention is basically directed to using a burner using plasma characterized in that a combustion tank helping spray a mixture fuel via a nozzle and combust the same is designated as a positive electrode (+), and a rod installed at one side of the same is designated as a negative electrode (−), thus receiving a DC (Direct Current) electricity of a DC electricity supply part, and a steam supply pipe is installed, so a mixture fuel supply pipe surrounding a combustion tank in a coil shape can be heated or preheated in such a way to heat an inner wall of the combustion tank by means of a high temperature plasma flame of above 800° C. in a combustion chamber with the aid of a flame generation of a high temperature steam plasma torch from a steam supply pipe, and a fuel can be supplied at a pressure above 50 atm by a high pressure pump as a nozzle of a mixture fuel supply pipe is ignited, so the mixture can be more effectively combusted as compared to a simply spray combustion which uses a nozzle in a combustion chamber of a combustion tank owing to a high pressure and a high temperature of above 800° C., and a more continuous, safer combustion might be achieved at a lower cost in the event that a plasma torch part is used together.
- The oil burner generally used at a boiler or the something is designed to use a relatively expensive fuel oil and to spray via a nozzle in a mist form, thus combusting the fuel; however the maintenance of the boiler is costly which leads to a higher economic burden to a user.
- To overcome the above problems, an industrial water oil is being suggested as a fuel; however the production of the industrial waste oil is very limited, thus limiting its actual application. Since diverse contaminations are contained in the waste oil, without a high temperature combustion, a harmful gas generated during an incomplete combustion could contaminate air. When it is needed to properly process such harmful gas, a high temperature heat decomposition process is needed at each step, and the industrial waste oil is needed to be processed in a mixing chamber which decomposes the oil into O2, H and OH-group, and the serious contamination substances contained in the waste oil can be stabilized using hydrogen fluoride, hydrogen chloride, CO2, etc; however the decomposition process system of such serious contamination substances require very expensive further facilities and high operation costs, which substantially retards the applications.
- There is another conventional art characterized in that water and waste oil are mixed at a proper ratio, and the mixture fuel of water and the waste oil is sprayed via a nozzle in a mist form in a combustion chamber and is combusted in the same, and a long mixture fuel supply pipe, adapted as a means for enhancing a combustion efficiency during a spray combustion of a mixture fuel, is installed in a separate preheating chamber in a coil shape, thus enhancing a fuel spray via a nozzle in a mist form, and a combustion efficiency; however the above conventional art has some limits in that it is almost impossible to increase the mixture fuel supply pipe formed in a coil shape to a proper temperature (above 800° C.) with only the heating apparatus which is designed to exclusively heat the preheating chamber, so the spray combustion of the mixture fuel with the aid of the nozzle becomes unstable, which results in a lower combustion efficiency in the boiler owing to an incomplete combustion.
- Accordingly, it is an object of the present invention to provide a burner using plasma which overcomes the problems encountered in the conventional art and makes it possible to achieve a more efficient ignition combustion and a complete combustion by using a mixture fuel formed of water and a waste oil.
- It is an object of the present invention to provide a burner using plasma which makes it possible to supply a mixture oil at a high pressure of above 50 atm using a high pressure pump in such a way that a mixture fuel supply pipe surrounding a combustion tank in a coil shape preheats the mixture fuel before it is sprayed in a mist form from a combustion chamber of a combustion tank to a nozzle and is combusted therein, the process of which achieves a high temperature combustion is performed in the combustion chamber, and since a combustion heat of the combustion chamber is well received by an inner wall of the combustion tank, thus helping complete combust the mixture fuel in the combustion chamber by continuously heating the mixture fuel supply pipe, and the direct current electricity is supplied from the direct current electricity supply part in such a way that a positive electrode part conducted with a positive voltage (+) of the direct current electricity supply part is provided in the combustion tank, and a rod conducted with a negative voltage (−) is configured in one side of the same, and a steam supply pipe is secured between the positive and negative electrode parts, thus producing a flame of a high steam plasma torch in the combustion chamber of the combustion tank, so the interior of the combustion chamber of above 800° C., which is a proper combustion temperature of the mixture fuel, can serve to perform a heating and preheating process, which leads to a more efficient combustion of the mixture fuel formed of water and a waste oil.
- It is further another object of the present invention to provide a burner using plasma which makes it possible to achieve a simple construction burner, and to significantly decrease an economical cost in terms of a combustion in a boiler or the something since the present invention provides a burner using plasma in which a mixture fuel made from water and an industrial waste oil can be completely combusted.
- To achieve the above objects, there is provided a burner using plasma characterized in that a combustion tank in which a mixture fuel supply pipe is wound in a coil shape around an outer surface of a cylindrical combustion tank with its both sides open, is designated as a positive electrode part, and a rod installed at an outer side of the same is designated as a negative electrode, thus receiving a direct current electricity from a direct current supply part, and a plasma torch part is configured in such a way that a steam supply pipe designed to receive steam from a steam generation part is installed between the combustion tank and the negative part, thus generating a high temperature steam plasma flame in the combustion chamber. The flame in the combustion chamber of the combustion tank, which is a high temperature steam plasma torch flame of above 800° C. proper to heat the mixture fuel, attributes to heat and consequently preheat the inner wall of the combustion tank for a short time with the aid of a circulation heating, so the mixture fuel supplied at a high pressure of above 50 atm from the high pressure pump can be well sprayed in a mist state and can be well combusted with the aid of a high pressure at the nozzle and a high temperature above 800° C., which leads to a complete combustion.
- As described above, the burner using plasma according to the present invention is characterized in that a combustion tank 1 configured in such a way that a mixture
fuel supply pipe 3 is wound in a coil shape on an outer surface of a combustion tank 1, is designated as a positive electrode part 7, and a rod engaged at an outer side of the same is designated as anegative electrode part 8, so a direct current electricity is supplied from a direct currentelectricity supply part 6, and asteam supply pipe 13 serving to receive steam from thesteam generation part 12 is disposed between the combustion tank 1 and thenegative electrode part 8, thus forming aplasma torch part 9, so a flame of a high temperature steam plasma torch is generated in thecombustion chamber 11 of the combustion tank 1. In the mode of the activation, a high temperature plasma flame can be generated at a high temperature of above 800° C., and since the inner wall of the combustion tank is heated and consequently preheated, the mixture fuel can be supplied at a high pressure of above 50 atm, and the water is decomposed into hydrogen and oxygen in the mixturefuel supply pipe 3, and the waste oil is decomposed into carbon components. When such components pass through the nozzle 4, a high heat is generated and is burnt on the basis of complete combustion. - The mixture fuel combustion in the combustion tank 1 helps to perform a preheating combustion and to adjust the combustion state with the aid of the operation of the
plasma torch part 9, thus always achieving complete combustion, and the water in the mixture fuel is decomposed into hydrogen and oxygen, and the waste oil therein is decomposed into carbon components, so the air contamination due to the waste oil can be significantly filtered and prevented, thus achieving an economically advantageous effect. - The present invention will become better understood with reference to the accompanying drawings which are given only by way of illustration and thus are not limitative of the present invention, wherein;
-
FIG. 1 is a cross sectional view illustrating the entire construction of a burner using plasma according to the present invention; -
FIG. 2 is a cross sectional view illustrating a combustion tank according to the present invention; -
FIG. 3 is a side view illustrating parts of an argon gas exhaust pipe and a negative electrode part according to the present invention; and -
FIG. 4 is a side view illustrating part of a steam supply pipe according to the present invention. -
* Descriptions of the reference numerals in the drawings* 1: combustion tank 3: mixture fuel supply pipe 6: direct current electricity supply part 7: positive electrode part 8: negative electrode part 11: combustion chamber 12: steam generation part 13: steam supply pipe - The preferred embodiments of the present invention will be described with reference to the accompanying drawings.
- It is noted that the same reference numerals are assumed to indicate the same elements or parts. During the descriptions of the present invention, the related known functions or constructions are omitted not to make the gist of the preset invention indefinite.
-
FIG. 1 is a cross sectional view illustrating the entire construction of a burner using plasma according to the present invention,FIG. 2 is a cross sectional view illustrating a combustion tank according to the present invention,FIG. 3 is a side view illustrating parts of an argon gas exhaust pipe and a negative electrode part according to the present invention, andFIG. 4 is a side view illustrating part of a steam supply pipe according to the present invention. - The present invention is characterized in that heat is collected via a combustion tank 1 formed by winding a mixture
fuel supply pipe 3 in a coil shape on an outer surface of the combustion tank 1 as a mixture fuel made by well mixing, with a mixer, water and waste oils is supplied by ahigh pressure pump 10 to an outer surface of acylindrical tank 10 with its both sides open. The inner end of the mixturefuel supply pipe 3 is connected to a nozzle 4 installed in thecombustion chamber 11, and the mixture fuel is supplied via the nozzle 4 to the mixturefuel supply pipe 3 at a high pressure of above 50 atm with the aid of thehigh pressure pump 10, so the mixture fuel is sprayed into thecombustion chamber 11 via the spray holes of the nozzle 4 in a mist form, thus achieving a high temperature combustion. - A
heat insulation cover 2 is covered on an outer side of the mixturefuel supply pipe 3 for the mixturefuel supply pipe 3 to fully receive the combustion heat of thecombustion chamber 11 and the heat of a high temperature steam plasma, and a combustion air tank 5 is installed in such a way to cover the entire outer portions of the nozzle 4 for an external air to be inputted from thepump 10′ at an outer side of the nozzle 4, thus air cooling the nozzle 4, and the combustion air is forced to circulate in thecombustion chamber 11, so enough amount of air injection and combustion flame circulate in the interior of thecombustion chamber 11 and is discharged to the outside. - The combustion tank 1 is designated as a positive electrode part 7, with the combustion tank 1 electrically conducting a positive electricity(+) from the direct current
electricity supply part 6 so as to form the combustion tank 1 with a plasma torch part, and the rod electrically conducting a negative electricity (−) from the direct currentelectricity supply part 6 is designated as anegative electrode part 8, thus forming aplasma torch part 9. - A
steam supply pipe 13 serving to receive a high temperature steam from thesteam generation part 12 is secured between the side wall of the combustion tank 1 and theplasma torch part 9, thus supplying a direct current electricity, and in the mode of activation, a steam in a form of mist and a steam plasma flame are generated in theplasma torch part 9 over thecombustion chamber 11, thus generating a high temperature plasma flame of above 800° C. - An argon
gas exhaust pipe 15 is connected to thenegative electrode part 8 formed of a rod, in order to prevent a corrosion and transformation of the rod of thenegative electrode part 8 for thereby receiving an argon gas from the argongas supply part 14. In the drawings, reference numeral 16 represents an igniter. - The operation of the burner using plasma according to the present invention is as follows. As the direct current electricity from the direct
current supply part 6 is concurrently supplied to the positive electrode part 7 of the combustion tank 1 and thenegative electrode part 8 of the rod, and a high temperature steam of thesteam generator 12 is provided in a form of mist via thesteam supply pipe 13, so a high temperature steam plasma flame is generated at theplasma torch part 9. At this time, since the plasma flame of above 800° C. heats the inner wall of the combustion tank 1 on which the mixturefuel supply pipe 3 is wound, thus performing a preheating process of the spray combustion of the nozzle 4. - The water contained in the mixture fuel is decomposed into hydrogen and oxygen by means of the preheating of the mixture
fuel supply pipe 3 wound on the outer surface of the combustion tank 1, and the waste oil is decomposed into very small carbon components, thus generating a high temperature when passing through the nozzle 4, and the mixture fuel of the mixturefuel supply pipe 3 is supplied in a state of a high pressure above 50 atm increased by means of thehigh pressure pump 10, so the mixture fuel can be completely combusted with the aid of a high pressure above 50 atm and a high temperature of above 800° C. in thecombustion chamber 11. - In the present invention, enough preheating is performed by means of the plasma flame generation in the combustion tank 1, and when the mixture fuel is sprayed in a form of mist via the spray holes of the nozzle 4, and the spray combustion is performed, the direct current electricity supply of the direct current
electricity supply part 6 is stopped, thus stopping the generation of plasma flame, and the mixture fuel is continuously supplied at a high pressure above 50 atm to thecombustion chamber 11 via the nozzle 4 by means of thehigh pressure pump 10, thus performing a continuously high temperature combustion. - During the combustion of the present invention, an external combustion air circulates via the combustion air tank 5 installed outside the nozzle 4 by means of the
pump 10′, and the nozzle 4 is continuously cooked, so the safety combustion of the nozzle 4 is achieved, and the external combustion air injected into thecombustion chamber 11 by means of thepump 10′ circulates in thecombustion chamber 11 along with the combustion flame with the aid of the construction that the passage of the combustion air tank 5 is formed in a screw shape, thus continuously contact-heating the inner wall of the combustion tank 1. During the combustion by means of the nozzle 4, the mixture fuel of the mixturefuel supply pipe 3 continues to burn at a high temperature in thecombustion chamber 11 along with the preheating. When the temperature of thecombustion chamber 11 of the combustion tank 1 decreases, and consequently the combustion is less performed, the heating to a higher temperature by means of the mixture fuel spray combustion by the nozzle 4 and the generation of a high temperature plasma flame can be adjusted by adjusting the supply of the direct current electricity of the directcurrent supply part 9, so a safe, easy use of the burner using plasma can be achieved. - The same reference numerals in the drawings indicate the same elements operating with the same functions.
- The above descriptions of the present invention are not limited to the above disclosed embodiments and accompanying drawings, and it is obvious to those who skilled in the art that various substitutions, changes and modifications are possible without departing from the concepts of the present invention.
Claims (1)
1. A burner using plasma, comprising:
a cylindrical combustion tank operating as a positive electrode part, the combusting tank being installed by winding in a coil shape a mixture fuel supply pipe on an outer surface of the cylindrical combustion tank with its both sides open;
a rod operating as a negative electrode part the rod being installed at an outer one side of the same, wherein a direct current electricity is received from a direct current electricity supply part; and
a plasma torch part configured by installing a steam supply pipe between the combustion tank and the negative electrode part, thus receiving the steam of a steam generation part, whereby to generate a high temperature plasma flame in the combustion tank.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR10-2009-0056123 | 2009-06-23 | ||
KR1020090056123A KR101025035B1 (en) | 2009-06-23 | 2009-06-23 | The burner for using plasma |
PCT/KR2010/004032 WO2010151026A2 (en) | 2009-06-23 | 2010-06-22 | Burner using plasma |
Publications (1)
Publication Number | Publication Date |
---|---|
US20120100497A1 true US20120100497A1 (en) | 2012-04-26 |
Family
ID=43387025
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US13/380,701 Abandoned US20120100497A1 (en) | 2009-06-23 | 2010-06-22 | Burner using plasma |
Country Status (8)
Country | Link |
---|---|
US (1) | US20120100497A1 (en) |
JP (1) | JP2012531572A (en) |
KR (1) | KR101025035B1 (en) |
CN (1) | CN102449397A (en) |
AU (1) | AU2010263419B2 (en) |
RU (1) | RU2493486C1 (en) |
SG (1) | SG176536A1 (en) |
WO (1) | WO2010151026A2 (en) |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103090381A (en) * | 2013-01-30 | 2013-05-08 | 广州市和宝生物能源技术有限公司 | Burner |
US20130273480A1 (en) * | 2012-04-17 | 2013-10-17 | Alter Nrg Corp | Start-up torch |
US20150271907A1 (en) * | 2004-09-03 | 2015-09-24 | Jack Hunt | Plasma Generator |
US9192415B1 (en) | 2008-02-06 | 2015-11-24 | Nuvasive, Inc. | Systems and methods for holding and implanting bone anchors |
US9198698B1 (en) | 2011-02-10 | 2015-12-01 | Nuvasive, Inc. | Minimally invasive spinal fixation system and related methods |
US9486256B1 (en) | 2013-03-15 | 2016-11-08 | Nuvasive, Inc. | Rod reduction assemblies and related methods |
US20180051874A1 (en) * | 2016-08-18 | 2018-02-22 | Clearsign Combustion Corporation | Cooled ceramic electrode supports |
US9974577B1 (en) | 2015-05-21 | 2018-05-22 | Nuvasive, Inc. | Methods and instruments for performing leveraged reduction during single position spine surgery |
CN108854895A (en) * | 2018-06-15 | 2018-11-23 | 宋波 | Follow-on water reaction unit |
CN109974010A (en) * | 2019-03-26 | 2019-07-05 | 化州市联合民生轮业有限公司 | A kind of family life solid refuse processing unit |
US10398481B2 (en) | 2016-10-03 | 2019-09-03 | Nuvasive, Inc. | Spinal fixation system |
CN112619334A (en) * | 2020-10-22 | 2021-04-09 | 无锡英普朗科技有限公司 | High-temperature plasma reaction device |
US11051861B2 (en) | 2018-06-13 | 2021-07-06 | Nuvasive, Inc. | Rod reduction assemblies and related methods |
CN113217196A (en) * | 2021-03-03 | 2021-08-06 | 中国人民解放军空军工程大学 | Self-air-entraining sliding arc plasma jet igniter of concave cavity flame stabilizer and ignition method |
CN116906930A (en) * | 2023-07-28 | 2023-10-20 | 广东大唐国际雷州发电有限责任公司 | Low-load operation reliable ignition system for coal-fired generator set boiler |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102818282B (en) * | 2012-08-24 | 2014-12-03 | 北京博希格动力技术有限公司 | Micro-oil pure-oxygen enhanced plasma ignition method and igniter |
WO2017139906A1 (en) | 2016-02-17 | 2017-08-24 | 王守国 | Plasma heater |
CN105605591B (en) * | 2016-03-04 | 2018-08-21 | 杭州左纳实业有限公司 | The processing method of organic wastewater burner and organic wastewater |
CN106304601A (en) * | 2016-09-29 | 2017-01-04 | 成都真火科技有限公司 | A kind of flame passes flow-generator |
KR101969832B1 (en) * | 2017-10-23 | 2019-04-17 | 주식회사 세지테크 | Boiler using micro plasma steam for eco-friendly burning of low grade fuel oil |
CN108800125A (en) * | 2018-02-07 | 2018-11-13 | 潘志华 | A kind of artificial intelligence water decomposition burner |
CN108215237B (en) * | 2018-02-26 | 2023-04-28 | 蒋丰亮 | Material extrusion and profiling device for PE large-caliber fiber reinforced pipeline |
CN108266729A (en) * | 2018-03-08 | 2018-07-10 | 广州荣誉国际电工有限公司 | A kind of burner and method for improving thermal chemical reaction rate and enthalpy |
CN108253417A (en) * | 2018-03-08 | 2018-07-06 | 广州荣誉国际电工有限公司 | It is a kind of to use artificial hot plasma flame and the united catalytic burner of oxyhydrogen flame and method |
CN108253418B (en) * | 2018-03-08 | 2024-03-15 | 广州荣誉国际电工有限公司 | Energy-saving burner |
WO2020059974A1 (en) * | 2018-09-21 | 2020-03-26 | 주식회사 세지테크 | Plasma steam burner system for eco-friendly combustion |
CN112082153B (en) * | 2020-09-11 | 2021-08-31 | 李宝伟 | Plasma state hydrogen-oxygen atom generator and control method thereof |
Citations (46)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1877523A (en) * | 1930-02-25 | 1932-09-13 | Gordon Bernard | Apparatus for treating the exhaust gases of internal combustion engines |
US2467450A (en) * | 1945-08-21 | 1949-04-19 | Aeroil Prod | Vaporizing coil type oil burner |
US2804918A (en) * | 1954-02-04 | 1957-09-03 | Hupp Corp | Retort burner and blowtorch incorporating the same |
US2863499A (en) * | 1955-12-01 | 1958-12-09 | George W Jackson | Fuel burners |
US3055144A (en) * | 1959-03-02 | 1962-09-25 | Gen Implement Corp | Vaporizer for preventing frost damage to agricultural crops |
US3289728A (en) * | 1965-04-30 | 1966-12-06 | Frank F Moench | Fuel burner |
US3439993A (en) * | 1967-08-25 | 1969-04-22 | Isaac Neufeldt | Vapourizing burner for pressurized liquid fuels |
US3854032A (en) * | 1973-12-26 | 1974-12-10 | J Cooper | Superheated electric arc steam generator |
US4213501A (en) * | 1976-11-13 | 1980-07-22 | Messer Griesheim Gmbh | Process and device for evaporating large quantities of low boiling liquefied gases |
US4443180A (en) * | 1981-05-11 | 1984-04-17 | Honeywell Inc. | Variable firing rate oil burner using aeration throttling |
US4596918A (en) * | 1984-02-17 | 1986-06-24 | Centre De Recherches Metallurgiques Centrum Voor Research In De Metallurgie | Electric arc plasma torch |
US4606761A (en) * | 1983-11-29 | 1986-08-19 | Union Steel Corp. (of So. Africa) Ltd. | Reduction of metal compounds |
US4772775A (en) * | 1987-03-23 | 1988-09-20 | Leach Sam L | Electric arc plasma steam generation |
US4980092A (en) * | 1988-04-22 | 1990-12-25 | Aerospatiale Societe Nationale Industrielle | Method for the destruction of chemically stable waste |
US5030273A (en) * | 1989-09-18 | 1991-07-09 | Plasma Energy Corporation | Furnace-plasma arc torch-supervisory control system for recovery of free aluminum from aluminum dross |
US5206879A (en) * | 1990-08-03 | 1993-04-27 | Tioxide Group Services Limited | Destruction process |
US5296670A (en) * | 1992-12-31 | 1994-03-22 | Osram Sylvania Inc. | DC plasma arc generator with erosion control and method of operation |
DE4235214A1 (en) * | 1992-10-20 | 1994-04-21 | Kba Immer Gmbh & Co Kg | Processing contaminated pre-cleaned oil in plasma reactor - with pre-cleaning by extn. with mixt. of polar solvent and non-polar solvent, sepg. heavy phase, and removing volatiles by distn.. |
US5319176A (en) * | 1991-01-24 | 1994-06-07 | Ritchie G. Studer | Plasma arc decomposition of hazardous wastes into vitrified solids and non-hazardous gasses |
US5420391A (en) * | 1994-06-20 | 1995-05-30 | Metcon Services Ltd. | Plasma torch with axial injection of feedstock |
US5546701A (en) * | 1994-09-20 | 1996-08-20 | Hydrogen Burner Technology, Inc. | Underoxidized burner utilizing improved injectors |
US5611947A (en) * | 1994-09-07 | 1997-03-18 | Alliant Techsystems, Inc. | Induction steam plasma torch for generating a steam plasma for treating a feed slurry |
US5866753A (en) * | 1992-03-04 | 1999-02-02 | Commonwealth Scientific | Material processing |
US5943970A (en) * | 1993-08-10 | 1999-08-31 | Gonopolsky; Adam Mikhailovich | Method and equipment for thermal destruction of wastes |
US6155182A (en) * | 1997-09-04 | 2000-12-05 | Tsangaris; Andreas | Plant for gasification of waste |
US6187206B1 (en) * | 1995-12-20 | 2001-02-13 | Alcan International | Thermal plasma reactor and wastewater treatment method |
US20010051322A1 (en) * | 1999-07-30 | 2001-12-13 | Heck Kenneth J. | Ignitor assembly for a fossil fuel-fired power generation system |
JP2002022135A (en) * | 2000-07-10 | 2002-01-23 | Mitsubishi Heavy Ind Ltd | Method and equipment for waste-oil combustion |
US6372156B1 (en) * | 1999-08-19 | 2002-04-16 | Bechtel Bwxt Idaho, Llc | Methods of chemically converting first materials to second materials utilizing hybrid-plasma systems |
US20030000823A1 (en) * | 2001-06-15 | 2003-01-02 | Uhm Han Sup | Emission control for perfluorocompound gases by microwave plasma torch |
US6617538B1 (en) * | 2000-03-31 | 2003-09-09 | Imad Mahawili | Rotating arc plasma jet and method of use for chemical synthesis and chemical by-products abatements |
US20050139593A1 (en) * | 2001-12-01 | 2005-06-30 | Mtu Aero Engines Gmbh | Method for purifying gas using plasma discharge |
US20060103318A1 (en) * | 2004-11-17 | 2006-05-18 | Bechtel Bwxt Idaho, Llc | Chemical reactor and method for chemically converting a first material into a second material |
US7140309B2 (en) * | 2003-09-22 | 2006-11-28 | New Energy Corporation | Method of clean burning and system for same |
US20060289397A1 (en) * | 2005-05-16 | 2006-12-28 | Imad Mahawili | Arc plasma jet and method of use for chemical scrubbing system |
US20070187372A1 (en) * | 2006-02-10 | 2007-08-16 | Alexander Rabinovich | High enthalpy low power plasma reformer |
US20080286169A1 (en) * | 2004-02-18 | 2008-11-20 | Commissariat A L'energie Atomique | Device and Method for Destroying Liquid, Powder or Gaseous Waste Using an Inductively Coupled Plasma |
US20080283153A1 (en) * | 2007-05-09 | 2008-11-20 | Air Products And Chemicals, Inc. | Furnace atmosphere activation method and apparatus |
US20080299019A1 (en) * | 2007-05-29 | 2008-12-04 | Dighe Shyam V | System and process for upgrading heavy hydrocarbons |
US20090031703A1 (en) * | 2007-07-30 | 2009-02-05 | Korea Institute Of Machinery & Materials | Plasma burner and diesel particulate filter trap |
US20090246094A1 (en) * | 2006-06-23 | 2009-10-01 | Young Bae Park | Waste gas purification apparatus |
US7658155B2 (en) * | 2005-06-29 | 2010-02-09 | Advanced Plasma Power Limited | Waste treatment process and apparatus |
US8070863B2 (en) * | 2006-05-05 | 2011-12-06 | Plasco Energy Group Inc. | Gas conditioning system |
US8373087B2 (en) * | 2005-04-28 | 2013-02-12 | E.E.R. Enviromental Energy Resources (Israel) Ltd. | Plasma torch for use in a waste processing chamber |
US8438983B2 (en) * | 2005-06-29 | 2013-05-14 | Advanced Plasma Power Limited | Waste treatment process and apparatus |
US20130126445A1 (en) * | 2009-11-30 | 2013-05-23 | Florent Lemont | Method and device for treating wastes by means of injection into an immersed plasma |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU20243A1 (en) * | 1930-03-31 | 1931-04-30 | Н.Н. Богоявленский | Oil Burner |
JPS56911A (en) * | 1979-06-15 | 1981-01-08 | Denroku Suzuki | Plasma arc type oil burner |
SU1211517A1 (en) * | 1984-03-20 | 1986-02-15 | Purmal Modris Ya | Arrangement for fuel combustion |
JPH06265109A (en) * | 1993-03-15 | 1994-09-20 | Nippon Steel Corp | Burner for plasma auxiliary combustion furnace |
JP2002013705A (en) * | 2000-06-28 | 2002-01-18 | Yoshikatsu Hayashi | Device for burning mixture of water and oil |
JP2005299440A (en) * | 2004-04-08 | 2005-10-27 | Jfe Engineering Kk | Gas engine device |
JP4301094B2 (en) * | 2004-06-25 | 2009-07-22 | トヨタ自動車株式会社 | Fuel or reducing agent addition apparatus and method, and plasma torch |
JP3928969B2 (en) * | 2004-08-20 | 2007-06-13 | 花本建設株式会社 | Oil-water mixture combustion equipment |
KR100822048B1 (en) * | 2006-06-07 | 2008-04-15 | 주식회사 글로벌스탠다드테크놀로지 | Apparatus using plasma torch to treat the hazadous waste gas |
KR200424378Y1 (en) | 2006-06-07 | 2006-08-22 | 주식회사 글로벌스탠다드테크놀로지 | Apparatus using plasma torch to treat the hazadous waste gas |
JP4659097B2 (en) * | 2006-08-01 | 2011-03-30 | コリア・インスティテュート・オブ・マシナリー・アンド・マテリアルズ | Plasma reactor and system for reducing particulate matter in exhaust gas using the same |
KR100679869B1 (en) | 2006-10-27 | 2007-02-07 | 한국기계연구원 | Pm reduction equipment of dpf system using plasma reactor |
JP3127046U (en) * | 2006-09-07 | 2006-11-16 | 周 耀南 | Plasma gas burner |
KR100844976B1 (en) * | 2007-07-18 | 2008-07-09 | 한국에너지기술연구원 | Combustion apparatus combining plasma/gas burner and melting method using the apparatus |
KR100866327B1 (en) * | 2007-07-30 | 2008-10-31 | 한국기계연구원 | Plasma burner and diesel particulate filter trap |
KR100913606B1 (en) | 2007-12-18 | 2009-08-26 | 한국기계연구원 | Plasma burner and diesel particulate filter trap |
-
2009
- 2009-06-23 KR KR1020090056123A patent/KR101025035B1/en active IP Right Grant
-
2010
- 2010-06-22 SG SG2011088960A patent/SG176536A1/en unknown
- 2010-06-22 AU AU2010263419A patent/AU2010263419B2/en not_active Ceased
- 2010-06-22 US US13/380,701 patent/US20120100497A1/en not_active Abandoned
- 2010-06-22 CN CN2010800235558A patent/CN102449397A/en active Pending
- 2010-06-22 JP JP2012517377A patent/JP2012531572A/en active Pending
- 2010-06-22 RU RU2012100003/06A patent/RU2493486C1/en not_active IP Right Cessation
- 2010-06-22 WO PCT/KR2010/004032 patent/WO2010151026A2/en active Application Filing
Patent Citations (58)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1877523A (en) * | 1930-02-25 | 1932-09-13 | Gordon Bernard | Apparatus for treating the exhaust gases of internal combustion engines |
US2467450A (en) * | 1945-08-21 | 1949-04-19 | Aeroil Prod | Vaporizing coil type oil burner |
US2804918A (en) * | 1954-02-04 | 1957-09-03 | Hupp Corp | Retort burner and blowtorch incorporating the same |
US2863499A (en) * | 1955-12-01 | 1958-12-09 | George W Jackson | Fuel burners |
US3055144A (en) * | 1959-03-02 | 1962-09-25 | Gen Implement Corp | Vaporizer for preventing frost damage to agricultural crops |
US3289728A (en) * | 1965-04-30 | 1966-12-06 | Frank F Moench | Fuel burner |
US3439993A (en) * | 1967-08-25 | 1969-04-22 | Isaac Neufeldt | Vapourizing burner for pressurized liquid fuels |
US3854032A (en) * | 1973-12-26 | 1974-12-10 | J Cooper | Superheated electric arc steam generator |
US4213501A (en) * | 1976-11-13 | 1980-07-22 | Messer Griesheim Gmbh | Process and device for evaporating large quantities of low boiling liquefied gases |
US4443180A (en) * | 1981-05-11 | 1984-04-17 | Honeywell Inc. | Variable firing rate oil burner using aeration throttling |
US4606761A (en) * | 1983-11-29 | 1986-08-19 | Union Steel Corp. (of So. Africa) Ltd. | Reduction of metal compounds |
US4596918A (en) * | 1984-02-17 | 1986-06-24 | Centre De Recherches Metallurgiques Centrum Voor Research In De Metallurgie | Electric arc plasma torch |
US4772775A (en) * | 1987-03-23 | 1988-09-20 | Leach Sam L | Electric arc plasma steam generation |
EP0359872A1 (en) * | 1987-03-23 | 1990-03-28 | Sam L. Leach | Steam generator |
US4980092A (en) * | 1988-04-22 | 1990-12-25 | Aerospatiale Societe Nationale Industrielle | Method for the destruction of chemically stable waste |
US5030273A (en) * | 1989-09-18 | 1991-07-09 | Plasma Energy Corporation | Furnace-plasma arc torch-supervisory control system for recovery of free aluminum from aluminum dross |
US5206879A (en) * | 1990-08-03 | 1993-04-27 | Tioxide Group Services Limited | Destruction process |
US5319176A (en) * | 1991-01-24 | 1994-06-07 | Ritchie G. Studer | Plasma arc decomposition of hazardous wastes into vitrified solids and non-hazardous gasses |
US5866753A (en) * | 1992-03-04 | 1999-02-02 | Commonwealth Scientific | Material processing |
DE4235214A1 (en) * | 1992-10-20 | 1994-04-21 | Kba Immer Gmbh & Co Kg | Processing contaminated pre-cleaned oil in plasma reactor - with pre-cleaning by extn. with mixt. of polar solvent and non-polar solvent, sepg. heavy phase, and removing volatiles by distn.. |
US5296670A (en) * | 1992-12-31 | 1994-03-22 | Osram Sylvania Inc. | DC plasma arc generator with erosion control and method of operation |
US5943970A (en) * | 1993-08-10 | 1999-08-31 | Gonopolsky; Adam Mikhailovich | Method and equipment for thermal destruction of wastes |
US5420391B1 (en) * | 1994-06-20 | 1998-06-09 | Metcon Services Ltd | Plasma torch with axial injection of feedstock |
US5420391A (en) * | 1994-06-20 | 1995-05-30 | Metcon Services Ltd. | Plasma torch with axial injection of feedstock |
US5611947A (en) * | 1994-09-07 | 1997-03-18 | Alliant Techsystems, Inc. | Induction steam plasma torch for generating a steam plasma for treating a feed slurry |
US5546701A (en) * | 1994-09-20 | 1996-08-20 | Hydrogen Burner Technology, Inc. | Underoxidized burner utilizing improved injectors |
US6187206B1 (en) * | 1995-12-20 | 2001-02-13 | Alcan International | Thermal plasma reactor and wastewater treatment method |
US6155182A (en) * | 1997-09-04 | 2000-12-05 | Tsangaris; Andreas | Plant for gasification of waste |
US20010051322A1 (en) * | 1999-07-30 | 2001-12-13 | Heck Kenneth J. | Ignitor assembly for a fossil fuel-fired power generation system |
US6372156B1 (en) * | 1999-08-19 | 2002-04-16 | Bechtel Bwxt Idaho, Llc | Methods of chemically converting first materials to second materials utilizing hybrid-plasma systems |
US6617538B1 (en) * | 2000-03-31 | 2003-09-09 | Imad Mahawili | Rotating arc plasma jet and method of use for chemical synthesis and chemical by-products abatements |
JP2002022135A (en) * | 2000-07-10 | 2002-01-23 | Mitsubishi Heavy Ind Ltd | Method and equipment for waste-oil combustion |
US20030000823A1 (en) * | 2001-06-15 | 2003-01-02 | Uhm Han Sup | Emission control for perfluorocompound gases by microwave plasma torch |
US7217903B2 (en) * | 2001-12-01 | 2007-05-15 | Mtu Aero Engines Gmbh | Method for purifying gas using plasma discharge |
US20050139593A1 (en) * | 2001-12-01 | 2005-06-30 | Mtu Aero Engines Gmbh | Method for purifying gas using plasma discharge |
US7140309B2 (en) * | 2003-09-22 | 2006-11-28 | New Energy Corporation | Method of clean burning and system for same |
US20080286169A1 (en) * | 2004-02-18 | 2008-11-20 | Commissariat A L'energie Atomique | Device and Method for Destroying Liquid, Powder or Gaseous Waste Using an Inductively Coupled Plasma |
US20060103318A1 (en) * | 2004-11-17 | 2006-05-18 | Bechtel Bwxt Idaho, Llc | Chemical reactor and method for chemically converting a first material into a second material |
US7354561B2 (en) * | 2004-11-17 | 2008-04-08 | Battelle Energy Alliance, Llc | Chemical reactor and method for chemically converting a first material into a second material |
US8287814B2 (en) * | 2004-11-17 | 2012-10-16 | Battelle Energy Alliance, Llc | Chemical reactor for converting a first material into a second material |
US20110236272A1 (en) * | 2004-11-17 | 2011-09-29 | Kong Peter C | Chemical reactor for converting a first material into a second material |
US8373087B2 (en) * | 2005-04-28 | 2013-02-12 | E.E.R. Enviromental Energy Resources (Israel) Ltd. | Plasma torch for use in a waste processing chamber |
US20060289397A1 (en) * | 2005-05-16 | 2006-12-28 | Imad Mahawili | Arc plasma jet and method of use for chemical scrubbing system |
US7658155B2 (en) * | 2005-06-29 | 2010-02-09 | Advanced Plasma Power Limited | Waste treatment process and apparatus |
US8438983B2 (en) * | 2005-06-29 | 2013-05-14 | Advanced Plasma Power Limited | Waste treatment process and apparatus |
US20070187372A1 (en) * | 2006-02-10 | 2007-08-16 | Alexander Rabinovich | High enthalpy low power plasma reformer |
US8070863B2 (en) * | 2006-05-05 | 2011-12-06 | Plasco Energy Group Inc. | Gas conditioning system |
US20090246094A1 (en) * | 2006-06-23 | 2009-10-01 | Young Bae Park | Waste gas purification apparatus |
US8197765B2 (en) * | 2006-06-23 | 2012-06-12 | Young Bae Park | Waste gas purification apparatus |
US8268094B2 (en) * | 2007-05-09 | 2012-09-18 | Air Products And Chemicals, Inc. | Furnace atmosphere activation method and apparatus |
US20080283153A1 (en) * | 2007-05-09 | 2008-11-20 | Air Products And Chemicals, Inc. | Furnace atmosphere activation method and apparatus |
US20100215554A1 (en) * | 2007-05-29 | 2010-08-26 | Dighe Shyam V | System and process for upgrading heavy hydrocarbons |
US7632394B2 (en) * | 2007-05-29 | 2009-12-15 | Westinghouse Plasma Corporation | System and process for upgrading heavy hydrocarbons |
US8052946B2 (en) * | 2007-05-29 | 2011-11-08 | Westinghouse Plasma Corporation | System and process for upgrading heavy hydrocarbons |
US20080299019A1 (en) * | 2007-05-29 | 2008-12-04 | Dighe Shyam V | System and process for upgrading heavy hydrocarbons |
US8257455B2 (en) * | 2007-07-30 | 2012-09-04 | Korea Institute Of Machinery & Materials | Plasma burner and diesel particulate filter trap |
US20090031703A1 (en) * | 2007-07-30 | 2009-02-05 | Korea Institute Of Machinery & Materials | Plasma burner and diesel particulate filter trap |
US20130126445A1 (en) * | 2009-11-30 | 2013-05-23 | Florent Lemont | Method and device for treating wastes by means of injection into an immersed plasma |
Cited By (30)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20150271907A1 (en) * | 2004-09-03 | 2015-09-24 | Jack Hunt | Plasma Generator |
US10004544B2 (en) | 2008-02-06 | 2018-06-26 | Nuvasive, Inc. | Systems and methods for introducing a bone anchor |
US11311320B2 (en) | 2008-02-06 | 2022-04-26 | Nuvasive, Inc. | Systems and methods for introducing a bone anchor |
US9492208B1 (en) | 2008-02-06 | 2016-11-15 | Nuvasive, Inc. | Systems and methods for holding and implanting bone anchors |
US9757166B1 (en) | 2008-02-06 | 2017-09-12 | Nuvasive, Inc. | Systems and methods for holding and implanting bone anchors |
US10426526B2 (en) | 2008-02-06 | 2019-10-01 | Nuvasive, Inc. | Systems and methods for introducing a bone anchor |
US9192415B1 (en) | 2008-02-06 | 2015-11-24 | Nuvasive, Inc. | Systems and methods for holding and implanting bone anchors |
US10426527B2 (en) | 2011-02-10 | 2019-10-01 | Nuvasive, Inc. | Minimally invasive spinal fixation system and related methods |
US9198698B1 (en) | 2011-02-10 | 2015-12-01 | Nuvasive, Inc. | Minimally invasive spinal fixation system and related methods |
US11406429B2 (en) | 2011-02-10 | 2022-08-09 | Nuvasive, Inc. | Minimally invasive spinal fixation system and related methods |
US11723698B2 (en) | 2011-02-10 | 2023-08-15 | Nuvasive, Inc. | Minimally invasive spinal fixation system and related methods |
US9649140B1 (en) | 2011-02-10 | 2017-05-16 | Nuvasive, Inc. | Minimally invasive spinal fixation system and related methods |
US9574770B2 (en) * | 2012-04-17 | 2017-02-21 | Alter Nrg Corp. | Start-up torch |
US20130273480A1 (en) * | 2012-04-17 | 2013-10-17 | Alter Nrg Corp | Start-up torch |
CN103090381A (en) * | 2013-01-30 | 2013-05-08 | 广州市和宝生物能源技术有限公司 | Burner |
US9486256B1 (en) | 2013-03-15 | 2016-11-08 | Nuvasive, Inc. | Rod reduction assemblies and related methods |
US11771477B2 (en) | 2015-05-21 | 2023-10-03 | Nuvasive, Inc. | Methods and instruments for performing leveraged reduction during single position spine surgery |
US10682166B2 (en) | 2015-05-21 | 2020-06-16 | Nuvasive, Inc. | Methods and instruments for performing leveraged reduction during single position spine surgery |
US9974577B1 (en) | 2015-05-21 | 2018-05-22 | Nuvasive, Inc. | Methods and instruments for performing leveraged reduction during single position spine surgery |
US20180051874A1 (en) * | 2016-08-18 | 2018-02-22 | Clearsign Combustion Corporation | Cooled ceramic electrode supports |
US10619845B2 (en) * | 2016-08-18 | 2020-04-14 | Clearsign Combustion Corporation | Cooled ceramic electrode supports |
US11766281B2 (en) | 2016-10-03 | 2023-09-26 | Nuvasive, Inc. | Spinal fixation system |
US10398481B2 (en) | 2016-10-03 | 2019-09-03 | Nuvasive, Inc. | Spinal fixation system |
US11197697B2 (en) | 2016-10-03 | 2021-12-14 | Nuvasive, Inc. | Spinal fixation system |
US11051861B2 (en) | 2018-06-13 | 2021-07-06 | Nuvasive, Inc. | Rod reduction assemblies and related methods |
CN108854895A (en) * | 2018-06-15 | 2018-11-23 | 宋波 | Follow-on water reaction unit |
CN109974010A (en) * | 2019-03-26 | 2019-07-05 | 化州市联合民生轮业有限公司 | A kind of family life solid refuse processing unit |
CN112619334A (en) * | 2020-10-22 | 2021-04-09 | 无锡英普朗科技有限公司 | High-temperature plasma reaction device |
CN113217196A (en) * | 2021-03-03 | 2021-08-06 | 中国人民解放军空军工程大学 | Self-air-entraining sliding arc plasma jet igniter of concave cavity flame stabilizer and ignition method |
CN116906930A (en) * | 2023-07-28 | 2023-10-20 | 广东大唐国际雷州发电有限责任公司 | Low-load operation reliable ignition system for coal-fired generator set boiler |
Also Published As
Publication number | Publication date |
---|---|
KR20100137875A (en) | 2010-12-31 |
JP2012531572A (en) | 2012-12-10 |
RU2493486C1 (en) | 2013-09-20 |
WO2010151026A2 (en) | 2010-12-29 |
RU2012100003A (en) | 2013-07-20 |
AU2010263419B2 (en) | 2013-05-30 |
CN102449397A (en) | 2012-05-09 |
SG176536A1 (en) | 2012-01-30 |
KR101025035B1 (en) | 2011-03-25 |
AU2010263419A1 (en) | 2012-02-09 |
WO2010151026A3 (en) | 2011-03-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20120100497A1 (en) | Burner using plasma | |
KR101424992B1 (en) | Burner Device | |
KR100951848B1 (en) | Combustion apparatus for fan heater and boiler | |
KR101405166B1 (en) | Hybrid scrubber system | |
KR20140131323A (en) | Multistage method for producing hydrogen-containing gaseous fuel and thermal gas-generator setup of its implementation (g.g. arakelyan method) | |
JP2997912B2 (en) | Compound processing equipment | |
KR101939924B1 (en) | A hybrid homogenous-catalytic combustion system | |
JP3127046U (en) | Plasma gas burner | |
JP3878284B2 (en) | Cremation method and apparatus | |
KR101562496B1 (en) | Pressure atomizing type of hybrid flame oil burner | |
JP2002022135A (en) | Method and equipment for waste-oil combustion | |
JPH1121572A (en) | Process and apparatus for combusting fossil fuel | |
JPH10253017A (en) | Hydrogen gas combustion apparatus and burner for heating combustion used therefor | |
JP2018169067A (en) | Gas Burner | |
JP5507720B1 (en) | Automatic ignition type oil burner | |
JP3791792B2 (en) | Exhaust gas treatment equipment | |
KR101530548B1 (en) | Premixed combustion device using heat recirculation | |
RU2769172C1 (en) | Steam plasma burner device with in-cycle gasification of fuel | |
KR101238407B1 (en) | Combustion apparatus using supercritical water | |
JP5476184B2 (en) | Waste glycerin fuel processing apparatus and method | |
KR101731570B1 (en) | Eco-friendly power generation system | |
RU2352869C1 (en) | Steam-gas mixture generator | |
KR20220035643A (en) | Energy producing system using emulsion and operating method thereof | |
TWI326754B (en) | ||
JP2000329308A (en) | Fuel combustion method, burner and ash treating device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |