WO1998047604B1 - Heat recovery and pollution abatement device - Google Patents
Heat recovery and pollution abatement deviceInfo
- Publication number
- WO1998047604B1 WO1998047604B1 PCT/CA1998/000363 CA9800363W WO9847604B1 WO 1998047604 B1 WO1998047604 B1 WO 1998047604B1 CA 9800363 W CA9800363 W CA 9800363W WO 9847604 B1 WO9847604 B1 WO 9847604B1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- air
- gas
- flue gas
- mist
- treated
- 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.)
- Ceased
Links
Abstract
A heat recovery and pollution abatement process with stackless operation for removing the products of combustion from hot boiler flue gas (45) comprising the steps of passing said hot boiler flue gas through a cloud of steam or mist (46), cooling the hot moist flue gas and recovering the heat therefrom (47), passing the partly cooled hot moist flue gas through a second cloud of mist comprised of cold water to total saturation (48), collecting the resulting stream of acid water, forcing the treated flue gas, mixing the treated flue gas with outside air, directing the forced treated air to atmosphere, shutting off the process in the absence of boiler flue gas.
Claims
1. A heat recovery and pollution abatement process with stackless operation for removing the products of combustion from hot boiler flue gas comprising flowing the hot boiler flue gas in a first direction, directing a cloud of steam or mist in the opposite direction causing a pressure differential between the two flows, increasing the relative humidity of the flue gas above 80% relative humidity but below saturation, cooling the hot moist flue gas and recovering heat therefrom, flowing the partly cooled flue gas in the first direction, directing a second cloud of mist using water only in the opposite direction, totally saturating the flue gas, condensing the fluids and collecting the resulting stream of acid water, forcing the treated flue gas, mixing the treated flue gas with outside air, directing the forced treated air to atmosphere, shutting off the process in the absence of boiler flue gas.
2. The heat recovery and pollution abatement process with stackless operation for removing the products of combustion from hot boiler flue gas of claim 1 in which the cloud of steam or mist is comprised of droplets 5 to
10 microns in diameter.
3. The heat recovery and pollution abatement process with stackless operation for removing the products of combustion from hot boiler flue gas of claim 2 in which the relative humidity of the flue gas is increased to 90 to
95% relative humidity but below saturation.
4. The heat recovery and pollution abatement process with stackless operation for removing the products of combustion from hot boiler flue gas of claim 1 in which the hot boiler flue gas is mixed with ozone prior to
-27-
passing said hot boiler flue gas and ozone through the cloud of steam or mist.
5. A pollution abatement process for removing contaminants from process air or gas, collecting the resultant stream of water containing contaminants, forcing the treated air or gas to atmosphere or recycling the treated air or gas as process air or gas, comprising flowing the treated air or gas in a first direction, directing a cloud of steam or mist in the opposite direction causing a pressure differential between the two flows, increasing the relative humidity of the process air or gas above 80% relative humidity but below saturation, cooiing the hot moist process air or gas and recovering heat therefrom, flowing the partly cooled process air or gas in the first direction, directing a second cloud of mist using water only in the opposite direction, totally saturating the process air or gas, collecting the resultant stream of water containing contaminants, forcing the treated air or gas to atmosphere or recycling the treated air or gas as process air or gas.
6. A pollution abatement process for removing contaminants from process air or gas of claim 5 in which the contaminants from process air or gas are mixed with ozone prior to passing said process air or gas and ozone through the cloud of steam or mist.
7. A process for cleaning indoor polluted ambient air, mixing said cleaned indoor ambient air with outside air for recirculation inside a building, comprising flowing the indoor polluted ambient air in a first direction, directing a cloud of steam or mist in the opposite direction causing a pressure differential between the two flows, increasing the relative humidity of the indoor polluted ambient air above 80% relative humidity but below saturation,
-28-
cooling the hot moist indoor polluted ambient air and recovering heat therefrom, flowing the partly cooled indoor polluted ambient air in the first direction, directing a second cloud of mist using water only in the opposite direction, totally saturating the indoor polluted ambient air, collecting the resultant stream of water containing pollutants, forcing a portion of the treated air to atmosphere and recirculating a portion of the treated air within the building.
8. The process for cleaning indoor polluted ambient air of claim 7 in which the cloud of steam or mist is comprised of droplets 5 to 10 microns in diameter.
9. The process for cleaning indoor polluted ambient air of claim 8 in which the relative humidity of the indoor polluted ambient air is increased to 90 to 95% relative humidity but below saturation.
10. The process for cleaning indoor polluted ambient air of claim 9 including the step of recovering heat from the moist indoor ambient air during the step or steps of cooling the moist indoor ambient air.
11. The process for cleaning indoor polluted ambient air of claim 7 in which the indoor polluted ambient air is mixed with ozone prior to passing said indoor polluted ambient air and ozone through the cloud of steam or mist.
12. A process for cleaning outside air for contaminants prior to introduction of the treated outside air into a building comprising flowing the outside air in a first direction, directing a cloud of steam or mist in the opposite direction causing a pressure differential between the two flows, increasing the relative humidity of the outside air above 80% relative humidity but below saturation, cooling the moist outside air and recovering heat therefrom,
- -
flowing the partly cooled outside air in the first direction, directing a second cloud of mist using water only in the opposite direction, totally saturating the outside air, collecting the resultant stream of water containing contaminants, forcing the treated atmospheric air into the building.
13. A heat recovery and pollution abatement unit with stackless operation for removing the products of combustion from hot boiler flue gases comprising a first misting chamber, a first cooling coil, a second misting chamber, a second cooling or condensing coil, a fan chamber, a diffuser, and a treated flue gas outlet with dampers, the first and second misting chambers including high pressure fine mist misting devices directed countercurrent to the direction of hot boiler gases.
14. The heat recovery and pollution abatement unit with stackless operation for removing the products of combustion from hot boiler flue gases of claim 13 in which the first and second cooling devices are also used as heat recovery units.
15. The heat recovery and pollution abatement unit with stackless operation for removing the products of combustion from hot boiler flue gases of claim 12 having an ozone mixing chamber in advance of the heat recovery and pollution abatement unit.
16. A pollution abatement unit for removing contaminants from process air or gas comprising a first misting chamber, a first cooling coil, a second misting chamber, a second cooling or condensing coil, a fan chamber, and a treated air or gas outlet for venting to atmosphere or recycling the forced process air or gas, the first and second misting chambers including high pressure fine mist misting devices directed countercurrent to the direction of hot boiler gases.
17. The pollution abatement unit for removing contaminants from process air or gas of claim 16 having an ozone mixing chamber in advance of the heat recovery and pollution abatement unit.
-30-
18. An air cleaning unit for cleaning indoor polluted ambient air from a building comprising a first misting chamber, a first cooling coil, a second misting chamber, a second cooling or condensing coil, a fan chamber, and a heated air outlet connected to the building supply air system, the first and second misting chambers including high pressure fine mist misting devices directed countercurrent to the direction of hot boiler gases.
19. The air cleaning unit for cleaning indoor polluted ambient air from a building of claim 18 in which the first and second cooling coils also recover heat.
20. A unit for cleaning outside ambient air for contaminants prior to introduction of the treated outside ambient air into a building comprising a first misting chamber, a first cooling coil, a second misting chamber, a second cooling or condensing coil, a fan chamber, and a cleaned air outlet for connection to the building supply air system, the first and second misting chambers including high pressure fine mist misting devices directed countercurrent to the direction of hot boiler gases.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/402,608 US6344177B1 (en) | 1997-04-23 | 1998-04-22 | Heat recovery and pollution abatement device |
| AU70209/98A AU7020998A (en) | 1997-04-23 | 1998-04-22 | Heat recovery and pollution abatement device |
| CA002330138A CA2330138A1 (en) | 1997-04-23 | 1998-04-22 | Heat recovery and pollution abatement device |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US4417797P | 1997-04-23 | 1997-04-23 | |
| US60/044,177 | 1997-04-23 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| WO1998047604A2 WO1998047604A2 (en) | 1998-10-29 |
| WO1998047604A3 WO1998047604A3 (en) | 1999-01-28 |
| WO1998047604B1 true WO1998047604B1 (en) | 1999-03-04 |
Family
ID=21930916
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CA1998/000363 Ceased WO1998047604A2 (en) | 1997-04-23 | 1998-04-22 | Heat recovery and pollution abatement device |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US6344177B1 (en) |
| AU (1) | AU7020998A (en) |
| CA (1) | CA2330138A1 (en) |
| WO (1) | WO1998047604A2 (en) |
Families Citing this family (36)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6162409A (en) * | 1999-03-15 | 2000-12-19 | Arthur P. Skelley | Process for removing Nox and Sox from exhaust gas |
| US7438744B2 (en) * | 2004-05-14 | 2008-10-21 | Eco/Technologies, Llc | Method and system for sequestering carbon emissions from a combustor/boiler |
| JP4995084B2 (en) | 2004-08-06 | 2012-08-08 | アルストム テクノロジー リミテッド | Super-cleaning of combustion gases including CO2 removal |
| AU2004205336B2 (en) * | 2004-08-31 | 2006-08-24 | Kosta Kapitoures | Emission Control Systems |
| ITMI20042296A1 (en) * | 2004-11-29 | 2005-02-28 | Ecociprea S R L | PLANT AND METHOD FOR THE REMOVAL OF AT LEAST ONE POLLUTANT FROM A FLUID IN A GASEOUS STAGE |
| US8182577B2 (en) | 2007-10-22 | 2012-05-22 | Alstom Technology Ltd | Multi-stage CO2 removal system and method for processing a flue gas stream |
| US7862788B2 (en) | 2007-12-05 | 2011-01-04 | Alstom Technology Ltd | Promoter enhanced chilled ammonia based system and method for removal of CO2 from flue gas stream |
| US7891210B2 (en) * | 2008-01-24 | 2011-02-22 | Johnson Controls Technology Company | Adjustable motor base for an HVAC&R blower motor |
| US7846240B2 (en) | 2008-10-02 | 2010-12-07 | Alstom Technology Ltd | Chilled ammonia based CO2 capture system with water wash system |
| US8404027B2 (en) | 2008-11-04 | 2013-03-26 | Alstom Technology Ltd | Reabsorber for ammonia stripper offgas |
| US8292989B2 (en) | 2009-10-30 | 2012-10-23 | Alstom Technology Ltd | Gas stream processing |
| US8790605B2 (en) | 2009-09-15 | 2014-07-29 | Alstom Technology Ltd | Method for removal of carbon dioxide from a process gas |
| US8784761B2 (en) | 2009-11-20 | 2014-07-22 | Alstom Technology Ltd | Single absorber vessel to capture CO2 |
| US8084652B2 (en) * | 2009-09-18 | 2011-12-27 | Eco Power Solutions (Usa) Corp. | Converting CO2 to an alcohol |
| US8518156B2 (en) | 2009-09-21 | 2013-08-27 | Alstom Technology Ltd | Method and system for regenerating a solution used in a wash vessel |
| EP2322265A1 (en) | 2009-11-12 | 2011-05-18 | Alstom Technology Ltd | Flue gas treatment system |
| US8293200B2 (en) | 2009-12-17 | 2012-10-23 | Alstom Technology Ltd | Desulfurization of, and removal of carbon dioxide from, gas mixtures |
| WO2011149530A1 (en) * | 2010-05-25 | 2011-12-01 | Caldwell Tanks, Inc. | Misting array assembly of an abatement system |
| USD639902S1 (en) | 2010-05-25 | 2011-06-14 | Caldwell Tanks, Inc. | Sealing structure for blocking an opening |
| US8870166B2 (en) | 2010-05-25 | 2014-10-28 | Caldwell Tanks, Inc. | Misting array assembly of an abatement system |
| US7975990B1 (en) | 2010-05-25 | 2011-07-12 | Caldwell Tanks, Inc. | Misting array assembly having adjustable nozzles |
| USD645936S1 (en) | 2010-05-25 | 2011-09-27 | Caldwell Tanks, Inc. | Nozzle tubing having offset nozzles |
| USD645118S1 (en) | 2010-05-25 | 2011-09-13 | Caldwell Tanks, Inc. | Nozzle tubing having offset nozzles |
| USD638519S1 (en) | 2010-05-25 | 2011-05-24 | Caldwell Tanks, Inc. | Misting array frame structure |
| US8728209B2 (en) | 2010-09-13 | 2014-05-20 | Alstom Technology Ltd | Method and system for reducing energy requirements of a CO2 capture system |
| US8623307B2 (en) | 2010-09-14 | 2014-01-07 | Alstom Technology Ltd. | Process gas treatment system |
| US20130283796A1 (en) * | 2011-01-04 | 2013-10-31 | Eco Power Solutions (Usa) Corp. | APPLYING OZONE NOx CONTROL TO AN HRSG FOR A FOSSIL FUEL TURBINE APPLICATION |
| US8329128B2 (en) | 2011-02-01 | 2012-12-11 | Alstom Technology Ltd | Gas treatment process and system |
| US9028784B2 (en) | 2011-02-15 | 2015-05-12 | Alstom Technology Ltd | Process and system for cleaning a gas stream |
| US9162177B2 (en) | 2012-01-25 | 2015-10-20 | Alstom Technology Ltd | Ammonia capturing by CO2 product liquid in water wash liquid |
| US8864879B2 (en) | 2012-03-30 | 2014-10-21 | Jalal Askander | System for recovery of ammonia from lean solution in a chilled ammonia process utilizing residual flue gas |
| US9694317B2 (en) | 2012-05-03 | 2017-07-04 | Altira Technology Fund V L.P. | Multi-pollutant abatement device and method |
| US9447996B2 (en) | 2013-01-15 | 2016-09-20 | General Electric Technology Gmbh | Carbon dioxide removal system using absorption refrigeration |
| US8986640B1 (en) | 2014-01-07 | 2015-03-24 | Alstom Technology Ltd | System and method for recovering ammonia from a chilled ammonia process |
| US11311831B1 (en) * | 2015-01-28 | 2022-04-26 | Pui King Chan | Air purification method based on cloud physics |
| EP3279560B1 (en) * | 2015-03-31 | 2022-08-03 | Mitsubishi Heavy Industries, Ltd. | Boiler, steam-generating plant provided with same, and method for operating boiler |
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|---|---|---|---|---|
| US3618301A (en) * | 1969-03-11 | 1971-11-09 | Clermont Engineering Co Inc | Process and apparatus for removing air pollutants from oven-stack emissions |
| FR2079074A5 (en) * | 1970-02-27 | 1971-11-05 | Aoi Katashi | |
| DE2061715C3 (en) * | 1970-04-17 | 1975-03-13 | Katashi Kamakura Kanagawa Aoi (Japan) | Device for separating toxic components from exhaust gases |
| US3948608A (en) * | 1972-03-24 | 1976-04-06 | Weir Jr Alexander | Apparatus for treating stack gases |
| JPS5215265B2 (en) * | 1973-03-03 | 1977-04-27 | ||
| US4158702A (en) * | 1974-07-22 | 1979-06-19 | Joy Manufacturing Company | Gas cleansing means |
| DE2708919C2 (en) * | 1977-03-02 | 1982-05-27 | Dr. C. Otto & Comp. Gmbh, 4630 Bochum | Process for the purification of SO ↓ 2 ↓ -containing industrial exhaust gases |
| US4189309A (en) * | 1978-03-14 | 1980-02-19 | Hoekstra Irenus A | Desulfurization of flue gas |
| US4400355A (en) * | 1981-12-07 | 1983-08-23 | Donnelly Francis M | Apparatus for desulfurizing combustion gases |
| FR2586204A1 (en) * | 1985-08-16 | 1987-02-20 | Tissandier Paul | Improvements to devices and processes for the decontamination of flue gases resulting from the combustion or incineration of products |
| US4753784A (en) * | 1986-03-03 | 1988-06-28 | Neverman Duane C | Process to remove SOX and NOX from exhaust gases |
| US4849192A (en) * | 1987-04-08 | 1989-07-18 | Energy And Environmental Research Corp. | Methods for preventing formation of sulfuric acid and related products in combustion effluents |
| US5122352A (en) * | 1988-03-08 | 1992-06-16 | Johnson Arthur F | Heat exchanger and pollutant removal system |
| DE3921787A1 (en) * | 1989-07-01 | 1991-01-17 | Hoechst Ag | METHOD FOR SELECTIVE ABSORPTION OF CHLORINE AND / OR BROM FROM CO (ARROW DOWN), 2 (ARROW DOWN) CONTAINING EXHAUST GASES WITH THE AID OF WATER VAPOR |
| US5321946A (en) * | 1991-01-25 | 1994-06-21 | Abdelmalek Fawzy T | Method and system for a condensing boiler and flue gas cleaning by cooling and liquefaction |
| US5270025A (en) * | 1991-04-05 | 1993-12-14 | Energy & Environmental Research Corp. | Methods for controlling N2 O emissions and for the reduction of NO.sub.x emissions in combustion systems while controlling N2 O emissions |
| US5206002A (en) * | 1991-08-29 | 1993-04-27 | Cannon Boiler Works, Inc. | Process for removing nox and sox from exhaust gas |
| US5366708A (en) * | 1992-12-28 | 1994-11-22 | Monsanto Eviro-Chem Systems, Inc. | Process for catalytic reaction of gases |
| DE4308310A1 (en) * | 1993-03-16 | 1993-09-30 | Tilo Dipl Ing Dolata | Exhaust gas scrubber with heat recovery and plastic construction - performs water spray scrubbing in first and third stages, and passes exhaust gas through adsorption material while heat is removed by cooling coils in second stage |
| US5670122A (en) * | 1994-09-23 | 1997-09-23 | Energy And Environmental Research Corporation | Methods for removing air pollutants from combustion flue gas |
-
1998
- 1998-04-22 WO PCT/CA1998/000363 patent/WO1998047604A2/en not_active Ceased
- 1998-04-22 US US09/402,608 patent/US6344177B1/en not_active Expired - Lifetime
- 1998-04-22 AU AU70209/98A patent/AU7020998A/en not_active Abandoned
- 1998-04-22 CA CA002330138A patent/CA2330138A1/en not_active Abandoned
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