CA2512491A1 - Apparatus and method using an electrified filter bed for removal of pollutants from a flue gas stream - Google Patents
Apparatus and method using an electrified filter bed for removal of pollutants from a flue gas stream Download PDFInfo
- Publication number
- CA2512491A1 CA2512491A1 CA002512491A CA2512491A CA2512491A1 CA 2512491 A1 CA2512491 A1 CA 2512491A1 CA 002512491 A CA002512491 A CA 002512491A CA 2512491 A CA2512491 A CA 2512491A CA 2512491 A1 CA2512491 A1 CA 2512491A1
- Authority
- CA
- Canada
- Prior art keywords
- flue gas
- filter bed
- gas stream
- pollutants
- bed unit
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/01—Pretreatment of the gases prior to electrostatic precipitation
- B03C3/014—Addition of water; Heat exchange, e.g. by condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/017—Combinations of electrostatic separation with other processes, not otherwise provided for
Landscapes
- Treating Waste Gases (AREA)
Abstract
Pollutants in a flue gas stream from a dryer of products, such as wood chips, are removed by a pollution abatement system that includes an electrified filter bed unit for removing solid particulates. To prevent deteriorated operation of the electrified filter bed unit due to condensation of volatile organic compounds, the flue gas stream is heated, prior to admission to the electrified filter bed unit, to a temperature sufficient to convert condensable liquid aerosols to a gaseous state. The electrified filter bed unit then removes solid particulate selectively without collecting condensable organics.
After the flue gas stream has passed through the electrified filter bed unit, gaseous pollutants can be removed by an oxidation process, for example.
After the flue gas stream has passed through the electrified filter bed unit, gaseous pollutants can be removed by an oxidation process, for example.
Claims (10)
1. Apparatus for drying particulate material and controlling emission of pollutants in flue gas, comprising a dryer using a hot gas stream, a pollution abatement system, and means for passing the flue gas through said pollution abatement system, wherein the flue gas contains particulate pollutants, gaseous pollutants, and condensable liquid aerosols, and wherein the pollution abatement system includes an electrified filter bed unit, and a heater, the flue gas being passed from the dryer through the heater and the electrified filter bed unit in that order, wherein the heater raises the temperature of the flue gas passed therethrough to a level sufficient to render liquid aerosols gaseous and to prevent condensation of the aerosols in the electrified filter bed unit, and the electrified filter bed unit removes particulates from the flue gas passed therethrough, without removing gaseous pollutants.
2. Apparatus according to claim 1, further comprising an incineration unit that receives flue gas passed from the electrified filter bed unit and that oxidizes gaseous pollutants in the flue gas.
3. Apparatus according to claim 1, wherein the heater is an air-to-air heat exchanger.
4. Apparatus according to claim 1, wherein the heater is an air/liquid heat exchanger.
5. Apparatus according to claim 1, wherein the heater is a direct hot gas mixing chamber.
6. A method of removing pollutants in a flue gas stream from a dryer of particulate materials, wherein the flue gas stream contains solid particulate pollutants, gaseous pollutants, and condensable liquid aerosol pollutants, said method comprising:
passing the flue gas stream through an electrified filter bed unit to remove the solid particulate pollutants from the flue gas stream; and prior to passing the flue gas stream through the electrified filter bed unit, heating the flue gas stream to a temperature sufficient to convert the condensable liquid aerosol pollutants to a gaseous phase and to maintain that phase as the flue gas stream is passed through the electrified filter bed unit, so that operation of the electrified filter bed unit is not impaired by condensation of the liquid aerosol pollutants in the electrified filter bed.
passing the flue gas stream through an electrified filter bed unit to remove the solid particulate pollutants from the flue gas stream; and prior to passing the flue gas stream through the electrified filter bed unit, heating the flue gas stream to a temperature sufficient to convert the condensable liquid aerosol pollutants to a gaseous phase and to maintain that phase as the flue gas stream is passed through the electrified filter bed unit, so that operation of the electrified filter bed unit is not impaired by condensation of the liquid aerosol pollutants in the electrified filter bed.
7. A method according to claim 6, wherein the flue gas stream is passed from the electrified filter bed unit to an incinerator to destroy gaseous pollutants.
8. A method according to claim 6, wherein the material dried comprises wood chips and the pollutants in the flue gas stream include volatile organic compounds that are driven off of the wood chips during the drying.
9. A method according to claim 8, wherein the wood chips are from southern and/or yellow pine.
10. A method according to claim 6, wherein the drying is performed in a dryer using hot gas supplied to the dryer in a temperature range of about 700°F to 1000°F, the flue gas stream is emitted from the dryer at a temperature range of about 200°F to 250°F, and prior to passing the flue gas stream through the electrified filter bed unit, the temperature of the flue gas stream is raised by about 50°F to 100°F.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/971,009 US6974494B1 (en) | 2004-10-25 | 2004-10-25 | Apparatus and method using an electrified filter bed for removal of pollutants from a flue gas stream |
US10/971,009 | 2004-10-25 |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2512491A1 true CA2512491A1 (en) | 2006-04-25 |
CA2512491C CA2512491C (en) | 2009-12-01 |
Family
ID=35452497
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002512491A Expired - Fee Related CA2512491C (en) | 2004-10-25 | 2005-07-19 | Apparatus and method using an electrified filter bed for removal of pollutants from a flue gas stream |
Country Status (2)
Country | Link |
---|---|
US (1) | US6974494B1 (en) |
CA (1) | CA2512491C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103055675A (en) * | 2013-01-18 | 2013-04-24 | 大恩(天津)环境技术研发有限公司 | Industrial smoke comprehensive treatment system and method based on advanced oxidation |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1747055A4 (en) * | 2004-04-09 | 2007-08-15 | Turbosonic Inc | Pollution control in wood products dryer |
EP1888204A4 (en) * | 2005-05-12 | 2012-02-29 | Turbosonic Inc | Pollution control in wood products dryer operation |
US7318288B2 (en) * | 2006-03-17 | 2008-01-15 | Karim Zahedi | Apparatus and method using an electrified filter bed for removal of pollutants from a flue gas stream |
ES2738525T3 (en) | 2007-03-21 | 2020-01-23 | Ash Tech Ind L L C | General purpose materials that incorporate a matrix of microparticles |
US20090239429A1 (en) | 2007-03-21 | 2009-09-24 | Kipp Michael D | Sound Attenuation Building Material And System |
US8445101B2 (en) | 2007-03-21 | 2013-05-21 | Ashtech Industries, Llc | Sound attenuation building material and system |
US8624908B1 (en) | 2008-06-27 | 2014-01-07 | Rovi Guides, Inc. | Systems and methods of transitioning from buffering video to recording video |
US8591677B2 (en) | 2008-11-04 | 2013-11-26 | Ashtech Industries, Llc | Utility materials incorporating a microparticle matrix formed with a setting agent |
SE0950639A1 (en) * | 2009-09-07 | 2011-03-08 | Andritz Tech & Asset Man Gmbh | Wood material drying plant with rotary dryer |
WO2012129656A1 (en) | 2011-03-28 | 2012-10-04 | Turbosonic Inc. | Erosion-resistant conductive composite material collecting electrode for wesp |
US11027289B2 (en) | 2011-12-09 | 2021-06-08 | Durr Systems Inc. | Wet electrostatic precipitator system components |
EP3589891A1 (en) | 2017-03-03 | 2020-01-08 | Douglas Technical Limited | Apparatus and method for continuously drying bulk goods, in particular wood chips and/or wood fibers comprising a solid fired hot gas generator |
UA125909C2 (en) * | 2017-06-06 | 2022-07-06 | Даґлас Текнікал Лімітед | Apparatus and method for continuously drying bulk goods |
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US4078503A (en) * | 1976-07-19 | 1978-03-14 | Nichols Engineering & Research Corporation | Method and apparatus for treating off-gas from a furnace for burning organic material in an oxygen deficient atmosphere |
US4144359A (en) | 1977-11-22 | 1979-03-13 | Efb Inc. | Apparatus and method for controlling pollutant emissions and for enhancing the manufacture of asphaltic roofing |
US4306885A (en) * | 1978-02-27 | 1981-12-22 | Apollo Technologies, Inc. | Method of conditioning flue gas |
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US4374652A (en) | 1979-08-23 | 1983-02-22 | Efb Inc. | Filter apparatus and method for collecting fly ash and fine dust |
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-
2004
- 2004-10-25 US US10/971,009 patent/US6974494B1/en not_active Expired - Fee Related
-
2005
- 2005-07-19 CA CA002512491A patent/CA2512491C/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103055675A (en) * | 2013-01-18 | 2013-04-24 | 大恩(天津)环境技术研发有限公司 | Industrial smoke comprehensive treatment system and method based on advanced oxidation |
Also Published As
Publication number | Publication date |
---|---|
CA2512491C (en) | 2009-12-01 |
US6974494B1 (en) | 2005-12-13 |
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Legal Events
Date | Code | Title | Description |
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EEER | Examination request | ||
MKLA | Lapsed |