US20070251435A1 - Fuel and emissions reduction power plant design using Oxygen for combustion and flue gas recirculation to minimize Carbon Dioxide and NOx emissions - Google Patents
Fuel and emissions reduction power plant design using Oxygen for combustion and flue gas recirculation to minimize Carbon Dioxide and NOx emissions Download PDFInfo
- Publication number
- US20070251435A1 US20070251435A1 US11/789,478 US78947807A US2007251435A1 US 20070251435 A1 US20070251435 A1 US 20070251435A1 US 78947807 A US78947807 A US 78947807A US 2007251435 A1 US2007251435 A1 US 2007251435A1
- Authority
- US
- United States
- Prior art keywords
- fuel
- oxygen
- combustion
- carbon dioxide
- nox
- 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
- 239000000446 fuel Substances 0.000 title claims abstract description 17
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 15
- 239000001301 oxygen Substances 0.000 title claims abstract description 15
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 15
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 8
- 239000003546 flue gas Substances 0.000 title claims abstract description 8
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 4
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 4
- 238000002485 combustion reaction Methods 0.000 title claims description 15
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title abstract description 5
- 239000000567 combustion gas Substances 0.000 title 1
- 238000000034 method Methods 0.000 claims abstract description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 7
- 239000012298 atmosphere Substances 0.000 claims abstract description 5
- 238000012986 modification Methods 0.000 claims abstract 2
- 230000004048 modification Effects 0.000 claims abstract 2
- 239000007789 gas Substances 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 5
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 238000012546 transfer Methods 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 239000005431 greenhouse gas Substances 0.000 claims 1
- 239000012299 nitrogen atmosphere Substances 0.000 claims 1
- 239000011369 resultant mixture Substances 0.000 claims 1
- 230000004936 stimulating effect Effects 0.000 claims 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 16
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 2
- 238000010792 warming Methods 0.000 abstract 2
- 230000002950 deficient Effects 0.000 abstract 1
- 230000008030 elimination Effects 0.000 abstract 1
- 238000003379 elimination reaction Methods 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- 230000001105 regulatory effect Effects 0.000 description 3
- 238000005755 formation reaction Methods 0.000 description 2
- 230000003071 parasitic effect Effects 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical class [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 1
- 238000012790 confirmation Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
Images
Classifications
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- 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
-
- 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
- F23L7/007—Supplying oxygen or oxygen-enriched air
-
- 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
- F23C2900/09002—Specific devices inducing or forcing flue gas recirculation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2215/00—Preventing emissions
- F23J2215/50—Carbon dioxide
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Definitions
- Some furnaces or boiler designs install an air to air heat exchanger and pass this flue gas thru one side of it and outside air is drawn thru the cross tubing to preheat the new batch of combustion air which will supply the Oxygen necessary for the fuel/Oxygen heating cycle to continue.
- the primary difference with this patent proposal is to return a regulated portion of the hot flue gas to the combustion air inlet where new fuel and commercially concentrated Oxygen are inputted thru separate pipes and burned, bringing the mixture up to the needed temperature to transfer more heat energy in to the steam or process generating system.
- the attached drawing identifies the typical components of a power boiler system and the uses of new or modified components to effect the improved emissions saving system.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Abstract
Power/process boiler modifications to use direct Oxygen input to burn the Carbon based fuel in a Nitrogen deficient atmosphere created by flue gas recirculation. This will result in a substantial reduction in fuel consumption and less Carbon Dioxide plus a near elimination of NOx in the flue exhaust released to the atmosphere. Both substances contribute to the Greenhouse effect and Global Warming and widespread use of his concept would help to reduce Global Warming and also reduce the usage and depletion of Carbon based fuels.
Description
- This application claims the benefit of PPA Ser. No. 60/796,124. confirmation NO. 2274 filed Apr. 27, 2006 by the present inventor.
- Not applicable
- Conventional and existing fuel fired boilers and process heating devices typically use atmospheric air as the source of Oxygen necessary for the combustion. Approximately 19 percent of the atmospheric air is elemental Oxygen and the major portion of the rest is elemental Nitrogen. The part of the atmospheric air we really need for the combustion process is the Oxygen. The rest of the air is basically parasitic in that it goes along for the ride with the heating process and requires a considerable portion of the heat output from the fuel combustion to raise the Nitrogen to the same temperature as the rest of the gases in the boiler.
- After the combined hot gases have imported a portion of their energy to the steam or other process, the gases exit the boiler and enter the flue or chimney where it is generally released to the atmosphere. Thus a substantial portion of the fuel combustion energy is thrown away after converting perhaps 50 percent of its energy to making steam.
- Some furnaces or boiler designs install an air to air heat exchanger and pass this flue gas thru one side of it and outside air is drawn thru the cross tubing to preheat the new batch of combustion air which will supply the Oxygen necessary for the fuel/Oxygen heating cycle to continue.
- The use of pure oxygen is not a new process and is sometimes used to reduce the amount of Carbon fuel used and to reduce the formations of Nitrous Oxides, but this modified process will use direct recirculation of the flue gases instead of using a gas to gas heat exchanger to preheat the Oxygen/Nitrogen combustion air. The regulated quantity of the recirculated flue gases that are returned to the boiler inlet will provide the additional mass of heated gases necessary to transfer their heat energy to the boiler/heater tubes or drum where the steam or other heated fluids are generated and subsequently put to use in electrical power generation or other manufacturing process.
- The primary difference with this patent proposal is to return a regulated portion of the hot flue gas to the combustion air inlet where new fuel and commercially concentrated Oxygen are inputted thru separate pipes and burned, bringing the mixture up to the needed temperature to transfer more heat energy in to the steam or process generating system.
- Enhanced combustion efficiency and reduction in NOx and Carbon Dioxide emissions thru a combined process of direct Oxygen feed for the combustion of the Carbon based fuel in place of the conventional atmospheric air supplied as the source of Oxygen, recirculation of the boiler or other heat/power generation device flue or discharge gases to provide a reheat capability volume and eliminate the introduction of atmospheric air which contains nearly 78 percent Nitrogen.
- The presence of the large amount of Nitrogen that comes with air breathing furnaces combined with the high temperatures of the boiler or other heating device normally results in the formation of NOx compounds which are undesirable emissions which are typically regulated to a low level. The quantity of Nitrogen in the conventionally fed atmospheric air is also parasitic to the combustion process in that it must also be heated up to the boiler temperature where it also releases a portion of its heat energy to the steam generating process but is then discharged from the boiler where much of it is released to the atmosphere and that heat is lost. Direct recirculation of this flue gas would reduce the quantity of Carbon fuel/Oxygen needed for the combustion process and to preheat the incoming new fuel and Oxygen.
- When the furnace is initially started up, the combustion chamber and gas flow area would be charged with an inert gas so as to preclude the presence of substantial amounts of Nitrogen.
- The attached drawing identifies the typical components of a power boiler system and the uses of new or modified components to effect the improved emissions saving system.
Claims (2)
1. Original design or modifications to existing power systems to incorporate this patent application will have the following benefits:
Direct Oxygen feed to provide the combustion of the Carbon based fuel will result in a higher flame temperature than using atmospheric air for the source of Oxygen. For a given quantity of fuel, the necessary BTU output can be achieved with a reduced quantity of fuel. This higher temperature will further heat the bypassed flue gases to bring the resultant mixture to the desired temperature needed to transfer heat energy to the production of steam or other process heating. The reduced quantity of Carbon based fuel will also result in the release of considerably less Carbon Dioxide, an undesirable Greenhouse gas.
2. The process of initially charging the boiler/heater combustion chamber with a non-Nitrogen atmosphere will preclude the formation of significant quantities of NOx compounds. NOx gases are an undesirable Greenhouse stimulating gas. Power producers and manufacturers are generally charged or monitored by the EPA to limit their release to the atmosphere.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US11/789,478 US20070251435A1 (en) | 2006-04-27 | 2007-04-25 | Fuel and emissions reduction power plant design using Oxygen for combustion and flue gas recirculation to minimize Carbon Dioxide and NOx emissions |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US79612406P | 2006-04-27 | 2006-04-27 | |
| US11/789,478 US20070251435A1 (en) | 2006-04-27 | 2007-04-25 | Fuel and emissions reduction power plant design using Oxygen for combustion and flue gas recirculation to minimize Carbon Dioxide and NOx emissions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20070251435A1 true US20070251435A1 (en) | 2007-11-01 |
Family
ID=38647122
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US11/789,478 Abandoned US20070251435A1 (en) | 2006-04-27 | 2007-04-25 | Fuel and emissions reduction power plant design using Oxygen for combustion and flue gas recirculation to minimize Carbon Dioxide and NOx emissions |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US20070251435A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090193809A1 (en) * | 2008-02-04 | 2009-08-06 | Mark Stewart Schroder | Method and system to facilitate combined cycle working fluid modification and combustion thereof |
| US20150013300A1 (en) * | 2013-06-03 | 2015-01-15 | Washington University | Method and apparatus for capturing carbon dioxide during combustion of carbon containing fuel |
| CN112377892A (en) * | 2020-12-01 | 2021-02-19 | 上海工业锅炉研究所有限公司 | Flue gas emission system of single-drum four-return biomass burning corner tube boiler |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6200128B1 (en) * | 1997-06-09 | 2001-03-13 | Praxair Technology, Inc. | Method and apparatus for recovering sensible heat from a hot exhaust gas |
| US6401633B2 (en) * | 1998-04-06 | 2002-06-11 | Minergy Corporation | Closed cycle waste combustion |
| US6532881B2 (en) * | 1999-06-10 | 2003-03-18 | L'air Liquide - Societe' Anonyme A' Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation De Procedes Georges Claude | Method for operating a boiler using oxygen-enriched oxidants |
| US6935251B2 (en) * | 2002-02-15 | 2005-08-30 | American Air Liquide, Inc. | Steam-generating combustion system and method for emission control using oxygen enhancement |
-
2007
- 2007-04-25 US US11/789,478 patent/US20070251435A1/en not_active Abandoned
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6200128B1 (en) * | 1997-06-09 | 2001-03-13 | Praxair Technology, Inc. | Method and apparatus for recovering sensible heat from a hot exhaust gas |
| US6401633B2 (en) * | 1998-04-06 | 2002-06-11 | Minergy Corporation | Closed cycle waste combustion |
| US6532881B2 (en) * | 1999-06-10 | 2003-03-18 | L'air Liquide - Societe' Anonyme A' Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation De Procedes Georges Claude | Method for operating a boiler using oxygen-enriched oxidants |
| US6935251B2 (en) * | 2002-02-15 | 2005-08-30 | American Air Liquide, Inc. | Steam-generating combustion system and method for emission control using oxygen enhancement |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090193809A1 (en) * | 2008-02-04 | 2009-08-06 | Mark Stewart Schroder | Method and system to facilitate combined cycle working fluid modification and combustion thereof |
| US20150013300A1 (en) * | 2013-06-03 | 2015-01-15 | Washington University | Method and apparatus for capturing carbon dioxide during combustion of carbon containing fuel |
| US9939153B2 (en) * | 2013-06-03 | 2018-04-10 | Washington University | Method and apparatus for capturing carbon dioxide during combustion of carbon containing fuel |
| US10767861B2 (en) | 2013-06-03 | 2020-09-08 | Washington University | Method and apparatus for capturing carbon dioxide during combustion of carbon containing fuel |
| CN112377892A (en) * | 2020-12-01 | 2021-02-19 | 上海工业锅炉研究所有限公司 | Flue gas emission system of single-drum four-return biomass burning corner tube boiler |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |