WO2015015447A1 - Process utilizing synergistic mixture of fuels to produce energy and reduce emissions in boilers - Google Patents
Process utilizing synergistic mixture of fuels to produce energy and reduce emissions in boilers Download PDFInfo
- Publication number
- WO2015015447A1 WO2015015447A1 PCT/IB2014/063565 IB2014063565W WO2015015447A1 WO 2015015447 A1 WO2015015447 A1 WO 2015015447A1 IB 2014063565 W IB2014063565 W IB 2014063565W WO 2015015447 A1 WO2015015447 A1 WO 2015015447A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- emissions
- magnegas
- combustion chamber
- process according
- combustion
- 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
- F23C6/00—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
- F23C6/04—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection
- F23C6/042—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection with fuel supply in stages
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/002—Removal of contaminants
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/02—Dust removal
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/04—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
- C10K3/06—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by mixing with gases
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/12—Liquefied petroleum gas
-
- 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
- F23C6/00—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
- F23C6/04—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection
- F23C6/045—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection with staged combustion in a single enclosure
- F23C6/047—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection with staged combustion in a single enclosure with fuel supply in stages
-
- 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
- F23C9/00—Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber
- F23C9/06—Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber for completing combustion
-
- 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
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
- F23G7/065—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
-
- 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
- F23C2900/00—Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
- F23C2900/9901—Combustion process using hydrogen, hydrogen peroxide water or brown gas as fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2400/00—Pretreatment and supply of gaseous fuel
- F23K2400/10—Pretreatment
Definitions
- the present invention relates to a clean burning dual fuel combination in a secondary combustion process resulting in greater heat output and lower emissions, and a process for the production thereof.
- Solid fuels (coal, wood or bio char) or liquid fuels (oil, LPG or natural gas) are used extensively to produce heat in boilers.
- the boiler emits heat and the heat is used to produce steam for a wide range of applications.
- the object of this invention seeks to address some or all of the above issues by providing a dual fuel which is able to produce high levels of heat output with substantially lower CO and C02 emissions.
- Magnegas is a clean burning fuel as described and formed by the process in US 6,663,752. This fuel is comprised of 65% hydrogen with a calorific value of 28 Mega joules per cubic Metre (MJ/m3) and a pressure of 18,000 kPa per bottle.
- Electromagnecules are stable clusters of individual atoms such as H (Hydrogen), C (Carbon) and O (Oxygen), parts of molecules called dimers (such as OH and CH), and ordinary molecules (such as CO and H-H-O) bonded together by internal attractive forces due to the electric and magnetic polarizations of the orbits of peripheral atomic electrons.
- H Hydrogen
- C Carbon
- O Oxygen
- dimers such as OH and CH
- ordinary molecules such as CO and H-H-O
- Magnegas acts as a catalyst. Molecular valence bonds are broken and the Magnegas converts or drawing atoms from the molecules in the primary fuel emissions into electromagnegular clusters. These molecules include those in the emissions targets such as CO and C02.
- Magnegas is a hydrogen based fuel sourced from Magnegas Corporation in Tarpon Springs, Florida, USA. This was the form of Magnegas used in all tests conducted in Australia. Unless otherwise specified, any reference to Magnegas in this document refers to Magnegas (Methanol). Ethylene glycol and oil based Magnegas are fuels with a higher calorific value (than Methanol). Magnegas (glycol) was used in the tests conducted in the USA. Where Magnegas (Glycol) is used, this is specified.
- Testo Analyzer data The emissions are recorded in flue gases using a testo 350 Analyzer.
- the equipment records the data from the flue gases into the Analyzer. Recorded Testo data is transferred into a computer software program. Data from flow meters are also recorded and merged with testo data to show flow rates and flue measurements using Excel spreadsheets.
- Serra flow meters purpose built to test different gases are linked to a totalizer box to change mixing rates.
- Data logging devices collect pulses from the totalizer and this data is downloaded onto a computer.
- Trendreader software collects the data from the data logger used in the boiler. Data was then analyzed on a spreadsheet program.
- emissions from the primary combustion process are captured, cooled (in order to avoid premature combustion before reaching the combustion chamber), compressed, mixed with Magnegas, and then re-combusted in a secondary combustion chamber at a temperature of at least 140 degrees Celsius.
- the most effective temperature range is between 140 and 220 degrees Celsius.
- a chart of the data showing the most effective temperatures for Magnegas heating in combustion process is shown in Figure 1 .
- a Testo report is not provided as the machine was unavailable for this test.
- Further graphs showing the most effective temperatures and emissions for Magnegas (Glycol) are shown in Figure 1 A. At temperatures below 140 degrees Celsius, combustion is less effective and higher levels of CO are formed.
- Magnegas in combination with the emissions, from these traditional fuels as a dual fuel under the above conditions results in high levels of energy output and substantially lower emissions than that achieved for traditional fuels.
- This dual fuel is not a simple mixture of fuels.
- Magnegas is mixed with the emissions so that it bonds to the emissions to form a structured dual fuel combination with unexpected effects.
- Coal feedstock is added to the primary combustion chamber (in this example, the boiler) at a rate of approx. 125 kg per hour.
- Oxygen is used to provide combustion in the primary combustion chamber. Flue emissions are in the range of approximately 140 to 300 degrees Celsius. Emissions from the primary combustion chamber is used when Magnegas is added creating a fuel for the secondary combustion chamber. Waste heat is captured and sent to a heat exchange system (in this example, a clean cycle generator). This can produce up to approx. 125 KWh of electricity which may be used in the electricity grid.
- the emissions from the boiler are cooled using a heat exchange to a temperature in the range of approx. 125 degrees Celsius to 150 degrees Celsius.
- the emissions are then condensed in the pipe and compressed before being transferred via a further pipe to the post combustion chamber.
- Magnegas is added to the emissions/feedstock.
- a mixing valve is used to control the rate of flow of the feedstock into the post combustion chamber.
- the ignition of the fuel and the emissions occurs in the post combustion chamber.
- This chamber is shaped to allow for expansion of the fuel during combustion.
- the chamber comprises an enlarged cylinder with an input opening for injection of feedstock at one end and an output opening at the other end for the release of heat and remaining emissions.
- Table 1 compares Coal emission produced from the primary boiler combustion system (traditional coal fired boiler emissions) to emissions from the Post Combustion process of the present invention.
- European Communities Council Directive 1 999/30 EC relating to limit values for sulphur dioxide, nitrogen dioxide and oxides of nitrogen in ambient air.
- the max amount of NO 2 is 200 mg/m3 ⁇ 98.7 ppm.
- Copper or stainless steel pipe from the primary combustion chamber to the post combustion chamber is 1 .6mm in thickness 100mm in diameter. Because the pipe is relatively thin it allows the emissions that are hot, to be cooled in the heat exchange down from between 120c and 140c. Cooling is required in order to avoid extreme heat in the pipes and early reaction before reaching the combustion chamber.
- the copper pipe coming down from the Primary combustion chamber is directed into a heat exchange process containing water.
- the pipe is built into a heat exchange chamber, which cools the pipes as the emissions flows through the pipes.
- the copper pipe is sealed, no water mixes with the emissions.
- the copper pipe then leads into the compressor station.
- the compressor station is a 7 inch x 3 inch diameter fan that moves 410m3 per hour of air.
- the Copper pipe is reduced from 100mm down to 50mm(50%reduction) before reaching the 2.5 inch emissions control valve which controls the speed of emissions flowing through the pipe and controls how much we send into the final post combustion chamber.
- the pipe from the tap to the post combustion chamber is 75mm and an inlet is provided through which Magnegas is added to the emissions.
- the rate of flow of Magnegas into the pipe is 85 standard litres per minute at a pressure of 180 kpa.
- the post combustion chamber is a purpose built machine made from refractory Fosico cement.
- the chamber is made with a diffuser action, which helps to swirl the mixture and mixes it.
- the chamber is larger in the middle than in the end, this expands in the middle then it contracts after combustion, which then gives it thrust.
- the measurements of the post combustion chamber are 75mm inlet into a cone of 100mm
- the chemical by-products comprise CO particulates carbon CO, NOx, SOx, heavy metals 02, and N02.
- Magnegas is then mixed with Coal flue emissions , then it is ignited.
- the exhaust gases are C02 7% 02 1 1 %, NOx 40 parts per million.
- the NOx and 02 will be the controls. No blending of air into the system, otherwise increases in CO, occurs.
- the Post-combustion chamber - 75mm grows out to 100mm then it forms a cone then a reverse cone on the backside back down to 75mm out.
- the reverse makes the chamber a 1 :5 ratio 100 diameter to 500 long it allows for the gas to expand and then burn.
- the reaction time tube has got to be cooled the bond built in the magnecules is not structured the new Magnegas fuel (H4) may not need as much cooling. No Nitrates.
- Emissions from the chemical reaction process is CO, particulates (carbon), NOx, SOx, all sorts of heavy metals C02, 02 N02 and NO, Hydrogen and CO are added and that is ignited. Results recorded are: C02 7%, 02 1 1 %, NOx 46 ppm, and an increase in 02 which is released and supports the combustion process. Carbon provides heat energy rather than forming CO. Particulates are lowered.
- the process for this test was: add coal to the Primary combustion chamber and burnt it, this was repeated over and over and shows on the graph the times we opened the flue to add more coal or to stoke the primary combustion furnace, or we checked the flue.
- the example of this can be seen on the seconds run line between 230 and 460 seconds. Another example is at 678 to 792 seconds the same event occurred. This occurred regularly throughout the test and is the oxygen blue line.
- the C02 (red line) and the NOX (purple line) decreased and resumed non-activity levels.
- the CO moauve line
- Thrust - The post combustion chamber makes an air blowing noise similar to the thrust motor and produces heat.
- the flame, which exhausts out of the chamber is only visible in low light due to the high levels of Hydrogen in the feedstock.
- the end of the flame is actually which is clear extends approx. 1 metre from the end of the chamber.
- Tests were conducted in the early evening so the flame could be viewed, filmed and recorded.
- a graph showing the flow rate in the combustion chamber is shown in Figure 4. Details of the results of recordings for NOx and CO are shown in Figure 5. Details of the results of recordings for 02 and C02 in the flue are shown in Figure 6 (02 increasing and C02 declining).
- testo data is in second intervals and the flow meter data for the
- Magnegas is in minutes. Further graphs with the data linked together is shown in Figure 17.
- the above test results are for Magnegas blended (mixed) with LPG as a dual fuel. Under the conditions when the temperature reaches 580 degrees Celsius in the boiler. Magnegas runs at 2.25 litre per minute and LPG runs at 1 litre per minute. A lower temperature of 470 degrees is reached when we mix 2.9 litres per minute of Magnegas with .65 litres per minute of LPG. A surprisingly high temperature output was achieved with this dual fuel combination.
- the chamber is made from steel or copper pipe on the intake side of the chamber.
- the combustion cylinder in this case is manufactured from refactory, a cement based product used in the boiler industry.
- the chamber has a cylindrical shape, with an inlet end and outlet end.
- the chamber is tapered at the outlet end.
- the chamber is tapered at both ends.
- the chamber has an inlet and preferably, the inlet into the chamber is at about a 30 degree angle. This directs flow to the larger proportion of the chamber where combustion occurs. This angle ensures that all emissions are forced into the centre of the chamber for combustion. Without the angle in the secondary combustion chamber, cooler air is trapped which circulates before the combustion flame. This lowers the temperature in the flame and chamber. This reduces the effectiveness of splitting of C02 and other emissions.
- the emissions from the primary combustion chamber are captured, cooled, and compressed.
- Magnegas is injected and mixed with the emissions in the mixing chamber before being sent to the secondary combustion chamber to ensure appropriate bonding of Magnegas to the emissions prior to secondary combustion. This needs to occur at least one metre before being fed into the secondary combustion chamber. Preferably, this is at approximately one metre before being fed into the secondary combustion chamber.
- the inlet is flared so as to provide a diffuser action and to help swirl the mixture.
- a circular motion occurs in the chamber during combustion.
- the chamber when ignited, pushes out the emissions.
- a thrust noise generated from the escaping combustion.
- Some of the combustion occurs otside the chamber.
- the hydrogen flame being partly invisible froms part of the combustion.
- Particulates and small carbon flakes from the primary combustion process are ignited in the secondary combustion process. These embers fall both inside and outside the secondary combustion chamber.
- FIG. 22 A Drawing showing an outline of a preferred form of the secondary combustion dual fuel system is shown in Figure 22. This drawing includes the design of the secondary combustion chamber.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020167005582A KR20160096584A (en) | 2013-07-30 | 2014-07-30 | Process utilizing synergistic mixture of fuels to produce energy and reduce emissions in boilers |
AU2014297994A AU2014297994A1 (en) | 2013-07-30 | 2014-07-30 | Process utilizing synergistic mixture of fuels to produce energy and reduce emissions in boilers |
US14/909,433 US20160195264A1 (en) | 2013-07-30 | 2014-07-30 | Process utilizing synergistic mixture of fuels to produce energy and reduce emissions in boilers |
EP14832844.6A EP3027968A4 (en) | 2013-07-30 | 2014-07-30 | Process utilizing synergistic mixture of fuels to produce energy and reduce emissions in boilers |
CN201480054106.8A CN106537034A (en) | 2013-07-30 | 2014-07-30 | Process utilizing synergistic mixture of fuels to produce energy and reduce emissions in boilers |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2013902833A AU2013902833A0 (en) | 2013-07-30 | Process utilizing dual fuels to produce energy and reduce emissions in boilers | |
AU2013902833 | 2013-07-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2015015447A1 true WO2015015447A1 (en) | 2015-02-05 |
Family
ID=52431093
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/IB2014/063565 WO2015015447A1 (en) | 2013-07-30 | 2014-07-30 | Process utilizing synergistic mixture of fuels to produce energy and reduce emissions in boilers |
Country Status (6)
Country | Link |
---|---|
US (1) | US20160195264A1 (en) |
EP (1) | EP3027968A4 (en) |
KR (1) | KR20160096584A (en) |
CN (1) | CN106537034A (en) |
AU (1) | AU2014297994A1 (en) |
WO (1) | WO2015015447A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018129596A1 (en) | 2017-01-16 | 2018-07-19 | Energy2Cleanair Holdings Pty Ltd As Trustee For Energy2Cleanair Unit Trust | Post-combustion device and method |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2987873A (en) * | 1955-05-13 | 1961-06-13 | Phillips Petroleum Co | Method and apparatus for using ammonia to increase the air specific impulse of a two-stage compressor turbojet engine |
US6663752B2 (en) * | 2001-10-03 | 2003-12-16 | Hadronic Press, Inc. | Clean burning liquid fuel produced via a self-sustaining processing of liquid feedstock |
US20100287942A1 (en) * | 2009-05-14 | 2010-11-18 | General Electric Company | Dry Low NOx Combustion System with Pre-Mixed Direct-Injection Secondary Fuel Nozzle |
US20120011854A1 (en) * | 2010-07-13 | 2012-01-19 | Abdul Rafey Khan | Flame tolerant secondary fuel nozzle |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
PT97742B (en) * | 1990-11-05 | 1999-03-31 | Gunnerman Rudolf W | PROCESS FOR COMBUSTION OF AN AQUEOUS COMBUSTIBLE IN AN INTERNAL COMBUSTION ENGINE |
KR950019076A (en) * | 1993-12-28 | 1995-07-22 | 가나이 쯔도무 | Combustion Method and Combustion Device |
US20090136406A1 (en) * | 2007-11-27 | 2009-05-28 | John Zink Company, L.L.C | Flameless thermal oxidation method |
JP5330838B2 (en) * | 2009-01-19 | 2013-10-30 | 新日鉄住金エンジニアリング株式会社 | Combustion burner for combustible gas generated from waste gasification |
US20120125759A1 (en) * | 2010-11-18 | 2012-05-24 | Flsmidth A/S | Vertical Calcined Petroleum Coke Incinerator |
-
2014
- 2014-07-30 CN CN201480054106.8A patent/CN106537034A/en active Pending
- 2014-07-30 US US14/909,433 patent/US20160195264A1/en not_active Abandoned
- 2014-07-30 KR KR1020167005582A patent/KR20160096584A/en not_active Application Discontinuation
- 2014-07-30 AU AU2014297994A patent/AU2014297994A1/en not_active Abandoned
- 2014-07-30 EP EP14832844.6A patent/EP3027968A4/en not_active Withdrawn
- 2014-07-30 WO PCT/IB2014/063565 patent/WO2015015447A1/en active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2987873A (en) * | 1955-05-13 | 1961-06-13 | Phillips Petroleum Co | Method and apparatus for using ammonia to increase the air specific impulse of a two-stage compressor turbojet engine |
US6663752B2 (en) * | 2001-10-03 | 2003-12-16 | Hadronic Press, Inc. | Clean burning liquid fuel produced via a self-sustaining processing of liquid feedstock |
US20100287942A1 (en) * | 2009-05-14 | 2010-11-18 | General Electric Company | Dry Low NOx Combustion System with Pre-Mixed Direct-Injection Secondary Fuel Nozzle |
US20120011854A1 (en) * | 2010-07-13 | 2012-01-19 | Abdul Rafey Khan | Flame tolerant secondary fuel nozzle |
Non-Patent Citations (1)
Title |
---|
See also references of EP3027968A4 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018129596A1 (en) | 2017-01-16 | 2018-07-19 | Energy2Cleanair Holdings Pty Ltd As Trustee For Energy2Cleanair Unit Trust | Post-combustion device and method |
Also Published As
Publication number | Publication date |
---|---|
US20160195264A1 (en) | 2016-07-07 |
CN106537034A (en) | 2017-03-22 |
EP3027968A1 (en) | 2016-06-08 |
AU2014297994A1 (en) | 2016-03-17 |
EP3027968A4 (en) | 2017-07-12 |
KR20160096584A (en) | 2016-08-16 |
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