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 PDF

Info

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
Application number
CA002512491A
Other languages
French (fr)
Other versions
CA2512491C (en
Inventor
Karim Zahedi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of CA2512491A1 publication Critical patent/CA2512491A1/en
Application granted granted Critical
Publication of CA2512491C publication Critical patent/CA2512491C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/01Pretreatment of the gases prior to electrostatic precipitation
    • B03C3/014Addition of water; Heat exchange, e.g. by condensation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/017Combinations 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.

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.
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.
CA002512491A 2004-10-25 2005-07-19 Apparatus and method using an electrified filter bed for removal of pollutants from a flue gas stream Expired - Fee Related CA2512491C (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Family Cites Families (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1130214A (en) * 1914-04-24 1915-03-02 Semet Solvay Co Art of removing tar from gas.
US2209798A (en) * 1936-09-12 1940-07-30 Union Oil Co Electrostatic fractionator
US2696892A (en) * 1951-06-08 1954-12-14 California Portland Cement Co Gas humidifying and electrical precipitation system
US3818682A (en) * 1972-09-25 1974-06-25 Owens Illinois Inc Flue gas temperature control system
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
US4308036A (en) 1979-08-23 1981-12-29 Efb Inc. Filter apparatus and method for collecting fly ash and fine dust
US4374652A (en) 1979-08-23 1983-02-22 Efb Inc. Filter apparatus and method for collecting fly ash and fine dust
US4338112A (en) 1981-03-19 1982-07-06 Owens-Corning Fiberglas Corporation Method for controlling particulate emissions from a glass furnace
US4338113A (en) 1981-03-19 1982-07-06 Owens-Corning Fiberglas Corporation Method for controlling particulate emissions
US4505723A (en) 1981-10-20 1985-03-19 Efb Inc. Filter apparatus
US4542000A (en) 1984-01-30 1985-09-17 Efb, Inc. Method for treating gas streams
US4668489A (en) * 1984-01-30 1987-05-26 Efb Inc. Method for treating gas streams
JPS60227844A (en) * 1984-04-27 1985-11-13 Mitsubishi Heavy Ind Ltd Treating equipment of stack gas
US4582521A (en) 1984-06-11 1986-04-15 Owens-Corning Fiberglas Corporation Melting furnace and method of use
US4675029A (en) * 1984-11-21 1987-06-23 Geoenergy International, Corp. Apparatus and method for treating the emission products of a wood burning stove
EP0274037A1 (en) 1986-12-10 1988-07-13 BBC Brown Boveri AG Process and device for the separation of particles
CA2001990C (en) 1989-11-01 1999-08-17 Gordon M. Cameron Electrostatic gas cleaning
US5290334A (en) 1992-09-21 1994-03-01 Edmeston Ab Apparatus for batch preheating and pollution abatement in glass manufacture
US5342427A (en) 1992-12-29 1994-08-30 Edmeston Ab Apparatus for cullet preheating and polluting emission reduction in the glass manufacturing process
US5607487A (en) 1993-03-17 1997-03-04 Taylor; Leland T. Bottom feed - updraft gasification system
US5458663A (en) * 1993-11-29 1995-10-17 Basf Corporation Apparatus for removing emissions by condensation and precipitation
US5665142A (en) * 1994-04-12 1997-09-09 Wilhelm Environmental Technologies, Inc. Flue gas conditioning system and method using native SO2 feedstock
US5505825A (en) 1994-09-20 1996-04-09 Foster Miller Inc. Electrically conductive sorption system and method
US5681375A (en) * 1996-07-16 1997-10-28 Wilhelm Environmental Technologies, Inc. Boiler flue gas conditioning system using dilute sulfuric acid injection
US5922290A (en) 1997-08-04 1999-07-13 Owens Corning Fiberglas Technology, Inc. Regenerative thermal oxidation system for treating asphalt vapors
US5980610A (en) * 1997-09-25 1999-11-09 The United States Of America As Represented By The United States Department Of Energy Apparatus and method for improving electrostatic precipitator performance by plasma reactor conversion of SO2 to SO3
JP3246427B2 (en) * 1997-12-22 2002-01-15 船井電機株式会社 Electronic dust collector and air conditioner with electronic dust collector

Cited By (1)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
CA2512491A1 (en) Apparatus and method using an electrified filter bed for removal of pollutants from a flue gas stream
KR100847058B1 (en) Purifying system for contaminated ground
KR101823961B1 (en) Drying system of sludge by reheating method using steam circulation
CN109127700B (en) Remediation equipment for organic contaminated soil
EP0839070B1 (en) Method for purifying exhaust from wood manufacturing processes
CN206073094U (en) A kind of VOC waste gas total system
JP5048573B2 (en) Sludge treatment method and treatment system
JPH11137950A (en) Treatment of waste gas of hot drying process and more particularly sludge drying process of sewer sludge drying device and equipment for execution this method
CA2163305A1 (en) Method for drying a substance, in particular wood shavings
CN108939821A (en) A kind of zeolite runner Adsorption Concentration device
NL8020118A (en) METHOD FOR EXTRACTING HEAT FROM MANURE, SEWER AND OTHER WET WASTE FROM COMBUSTION.
EA039823B1 (en) Apparatus and method for continuously drying bulk goods, in particular wood chips and/or wood fibers, comprising a solid fired hot gas generator
KR101059516B1 (en) Polluted soil purification system using fusion process of microwave and high temperature heating element
JP4979911B2 (en) Heat purification equipment for contaminated soil
KR101154826B1 (en) Sewage sludge processing equipment using direct buring deo-dorization device
EP0508546A1 (en) Drying apparatus
KR980000551A (en) Heating / drying of organic material and method and apparatus for treating waste gas generated therefrom
JP2005024160A (en) Dehumidifying drier and dehumidifying drying method
US8881424B2 (en) Drying installation
CN210584379U (en) VOCs processing apparatus
FI991566A (en) Procedure and apparatus for reducing greenhouse gas emissions
KR20060088799A (en) Waste incineration system having exhaust gas re-combustion chamber
KR102456662B1 (en) Packaged air pollution purification system
RU2622604C1 (en) Way of pasteous materials drying
JPH08311809A (en) Asphalt mixture manufacturing device

Legal Events

Date Code Title Description
EEER Examination request
MKLA Lapsed