[go: up one dir, main page]

WO2003068369A1 - Method, apparatus and singlet oxygen generator for cleaning gases - Google Patents

Method, apparatus and singlet oxygen generator for cleaning gases Download PDF

Info

Publication number
WO2003068369A1
WO2003068369A1 PCT/FI2003/000108 FI0300108W WO03068369A1 WO 2003068369 A1 WO2003068369 A1 WO 2003068369A1 FI 0300108 W FI0300108 W FI 0300108W WO 03068369 A1 WO03068369 A1 WO 03068369A1
Authority
WO
WIPO (PCT)
Prior art keywords
singlet oxygen
gas
oxygen generator
particles
set forth
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
Application number
PCT/FI2003/000108
Other languages
French (fr)
Inventor
Hannu L. Suominen
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.)
BCDE Group Waste Management Ltd Oy
Original Assignee
BCDE Group Waste Management Ltd Oy
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 BCDE Group Waste Management Ltd Oy filed Critical BCDE Group Waste Management Ltd Oy
Priority to AU2003205796A priority Critical patent/AU2003205796A1/en
Publication of WO2003068369A1 publication Critical patent/WO2003068369A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02Preparation of oxygen
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • 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
    • B03C3/019Post-treatment of gases
    • 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
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/38Particle charging or ionising stations, e.g. using electric discharge, radioactive radiation or flames

Definitions

  • the invention relates to a method and apparatus for cleaning harmful gases.
  • a particular application for the method and apparatus is the cleaning of exhaust gases from a waste disposal plant or an incineration plant.
  • the invention relates also to a singlet oxygen generator, which is capable of producing singlet oxygen in a gas flow for oxidizing harmful gaseous substances present therein.
  • the singlet oxygen generator finds a particular application in a method and apparatus of the invention for cleaning the gases of a waste disposal plant or an incineration plant.
  • Waste disposal and incineration plants produce exhaust gases, which contain both particles and gaseous harmful substances.
  • the particles can be e.g. microbial germs or other very small organic or inorganic particles. Harmful gaseous substances may include e.g. ammonia, methane, or hydrogen sulphide.
  • Harmful gaseous substances may include e.g. ammonia, methane, or hydrogen sulphide.
  • the removal of both particles and harmful gases from a gas mixture to be cleaned is particularly problematic. Especially, the elimination of small particles ( ⁇ 0,3 ⁇ m) from air is difficult with conventional air cleaners. Filters become blocked quickly, particularly in the process of cleaning moist air and the cleaning and replacement thereof requires a lot of work.
  • a second object of the invention is to provide a singlet oxygen generator, which is suitable for the oxidation of gaseous substances and which finds a particular application in the method and apparatus of the invention for cleaning the gases of a waste disposal or incineration plant.
  • the singlet oxygen generator has its characterizing features set forth in the appended claim 4.
  • FIG. 1 shows schematically an apparatus of the invention for implementing a method of the invention
  • Fig. 2 shows a singlet oxygen generator of the invention in a longitudinal section.
  • the gases of a waste disposal plant to be cleaned are first supplied to a particle separator 1, wherein the gas flows in a spirally whirling motion from bottom upwards. Inside the flow is a high-voltage electrode 5, the ion beams issuing from its tips charging particles present in the gas flow. The charged particles are collected by means of an electric field on energized collector surfaces 6, from which the particles are flushed with water sprayed from pipes 7 and the water is removed to receivers and/or further treatment processes, which do not constitute an object of this invention.
  • the gas flow, from which the particles have been eliminated, is delivered by a fan 4 along a duct to a gas cleaner 3, 7, which in the present case comprises a combination gas scrubber and particle separator, whose operation is otherwise similar to that of the particle separator 1 as described above, with the exception that the wash liquid sprayed from the pipes 7 can be provided with solvents and neutralizers needed for the scrubbing of gases to be removed in each particular application.
  • a jet of water alone is often sufficient for the removal of oxidized gases from a flow of exhaust gas.
  • the harmful gases, and particularly foul-smelling gases to be removed, are more readily scrubbed from an exhaust gas flow by oxidizing the same according to the invention with a singlet oxygen generator 2. What is essential in the invention is that the oxygenation is not performed until the gas has been cleaned to a substantially particle-free state.
  • the singlet oxygen generator 2 shown schematically in fig. 1, will now be described more closely with reference to fig. 2.
  • the generator 2 comprises a tube 13 of glass, inside which is an electrically conducting electrode 11, comprising e.g. a bar of acid-proof stainless steel. Outside the tube 13 is a spiral electrode 12. Between the tips of the electrodes 11, 12 is coupled a high-voltage supply 10. Its potential is typically within the range of 1-10 kV. Potential is preferably adjustable for controlling the production of singlet oxygen. Frequency is typically within the range of 10-100 kHz, and frequency can also be adjustable for optimizing the generator operation or controlling its output.
  • a substantially larger-diameter jacket tube 14 provides a flow channel for housing the spiral electrode 12.
  • E represents the energy of an electric field associated with a corona discharge.
  • the optimal operation and output of the singlet oxygen generator 2 can also be adjusted by controlling the speed of the fan 8.
  • the flow channel for a gas to be cleaned is provided with a mixer 20 for providing a turbulent flow and with sampling sensors 16 and 17 for a gas analyzer 21 upstream and downstream of a singlet oxygen supply point, respectively.
  • a control unit 15 controls the singlet oxygen generator's operation (voltage and/or frequency and/or air flow). Samples are picked up from the gas analyzer's 21 sampling points 16, 17 for the comparison of analytical data.
  • the discharge pipes of the combination particle separator and gas scrubber 3 and the particle separator 1 are provided with a viewing glass 18 and a debris screen 19, which denies admission of larger pieces of debris into a gas scrubbing solution, as well as with an outlet gate 22 for removing large pieces of debris.
  • the electrodes 5 and 6 have therebetween an active direct-voltage field with no alternating-current component.
  • the result of this is that the ion beams of the electrode 5 do not yet develop ozone at this stage, as the gas flow contains plenty of particles.
  • the generator 2 used for controlled production of singlet oxygen, but no more than the amount needed for the oxidation of gaseous compounds, and thus, for deodorizing the same.
  • the exhaust gas does not contain ozone, either.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention relates to a method and apparatus for cleaning gases. The invention relates also to a singlet oxygen generator, which finds a particular application in cleaning the gases of a waste disposal plant. At a first stage, a gas is subjected to the removal of particles by flowing the gas through a particle separator (1) capable of ionizing particles. At a second stage, the gas, which has been cleaned to a substantially particle-free state, is subjected to the removal of harmful gaseous substances by oxidation, such that the flow is supplied with singlet oxygen by means of a singlet oxygen generator (2).

Description

Method, apparatus and singlet oxygen generator for cleaning gases
The invention relates to a method and apparatus for cleaning harmful gases. A particular application for the method and apparatus is the cleaning of exhaust gases from a waste disposal plant or an incineration plant. The invention relates also to a singlet oxygen generator, which is capable of producing singlet oxygen in a gas flow for oxidizing harmful gaseous substances present therein. The singlet oxygen generator finds a particular application in a method and apparatus of the invention for cleaning the gases of a waste disposal plant or an incineration plant.
Waste disposal and incineration plants produce exhaust gases, which contain both particles and gaseous harmful substances. The particles can be e.g. microbial germs or other very small organic or inorganic particles. Harmful gaseous substances may include e.g. ammonia, methane, or hydrogen sulphide. The removal of both particles and harmful gases from a gas mixture to be cleaned is particularly problematic. Especially, the elimination of small particles (< 0,3 μm) from air is difficult with conventional air cleaners. Filters become blocked quickly, particularly in the process of cleaning moist air and the cleaning and replacement thereof requires a lot of work. It is prior known to clean gases by means of gas scrubbers, but, for example, methane, hydrogen sulphide, and ammonia are often present in such large amounts that powerful and expensive gas scrubbers are required, and a sufficient degree of cleaning is still not achieved.
It is an object of the invention to provide an improved method and apparatus, enabling an effective removal of both particles and harmful gases from gases to be cleaned.
This object of the invention is achieved by a method of the invention, the characterizing features of which are set forth in the appended claim 1. This object is also achieved by means of an apparatus of the invention, the characterizing features of which are set forth in the appended claim 3.
A second object of the invention is to provide a singlet oxygen generator, which is suitable for the oxidation of gaseous substances and which finds a particular application in the method and apparatus of the invention for cleaning the gases of a waste disposal or incineration plant. The singlet oxygen generator has its characterizing features set forth in the appended claim 4.
The invention will now be described in more detail by way of exemplary embodiments with reference to the accompanying drawings, in which
Fig. 1 shows schematically an apparatus of the invention for implementing a method of the invention; and
Fig. 2 shows a singlet oxygen generator of the invention in a longitudinal section.
In reference to fig. 1, the gases of a waste disposal plant to be cleaned are first supplied to a particle separator 1, wherein the gas flows in a spirally whirling motion from bottom upwards. Inside the flow is a high-voltage electrode 5, the ion beams issuing from its tips charging particles present in the gas flow. The charged particles are collected by means of an electric field on energized collector surfaces 6, from which the particles are flushed with water sprayed from pipes 7 and the water is removed to receivers and/or further treatment processes, which do not constitute an object of this invention.
The gas flow, from which the particles have been eliminated, is delivered by a fan 4 along a duct to a gas cleaner 3, 7, which in the present case comprises a combination gas scrubber and particle separator, whose operation is otherwise similar to that of the particle separator 1 as described above, with the exception that the wash liquid sprayed from the pipes 7 can be provided with solvents and neutralizers needed for the scrubbing of gases to be removed in each particular application. However, a jet of water alone is often sufficient for the removal of oxidized gases from a flow of exhaust gas.
The harmful gases, and particularly foul-smelling gases to be removed, are more readily scrubbed from an exhaust gas flow by oxidizing the same according to the invention with a singlet oxygen generator 2. What is essential in the invention is that the oxygenation is not performed until the gas has been cleaned to a substantially particle-free state.
The singlet oxygen generator 2, shown schematically in fig. 1, will now be described more closely with reference to fig. 2. The generator 2 comprises a tube 13 of glass, inside which is an electrically conducting electrode 11, comprising e.g. a bar of acid-proof stainless steel. Outside the tube 13 is a spiral electrode 12. Between the tips of the electrodes 11, 12 is coupled a high-voltage supply 10. Its potential is typically within the range of 1-10 kV. Potential is preferably adjustable for controlling the production of singlet oxygen. Frequency is typically within the range of 10-100 kHz, and frequency can also be adjustable for optimizing the generator operation or controlling its output. A substantially larger-diameter jacket tube 14 provides a flow channel for housing the spiral electrode 12. A fan 8 can be used for blowing air through the flow channel constituted by the jacket tube 14. Consequently, a corona effect, created by the spiral electrode 12 around itself, breaks up oxygen molecules of a flowing gas to singlet oxygen O' according to the following formula: O2 + E => O'+O1 (wherein E represents the energy of an electric field associated with a corona discharge). The optimal operation and output of the singlet oxygen generator 2 can also be adjusted by controlling the speed of the fan 8.
As shown in fig. 1, the flow channel for a gas to be cleaned is provided with a mixer 20 for providing a turbulent flow and with sampling sensors 16 and 17 for a gas analyzer 21 upstream and downstream of a singlet oxygen supply point, respectively. A control unit 15 controls the singlet oxygen generator's operation (voltage and/or frequency and/or air flow). Samples are picked up from the gas analyzer's 21 sampling points 16, 17 for the comparison of analytical data. For example, methane is converted by means of singlet oxygen to carbon dioxide and water (CH4 + 40' => C02 + 2H20), and hence, by analyzing the amount of methane upstream and downstream of a singlet oxygen supply point, the yield of singlet oxygen can be controlled in such a way that the proportional reduction of methane remains within a certain range. The same applies also e.g. to the conversion of hydrogen sulphide to gypsum and water by means of singlet oxygen: (H2S + 40' => H2S04;H2SO4 + Ca(OH)2 => CaS04 + 2H20)
In fig. 1, the discharge pipes of the combination particle separator and gas scrubber 3 and the particle separator 1 are provided with a viewing glass 18 and a debris screen 19, which denies admission of larger pieces of debris into a gas scrubbing solution, as well as with an outlet gate 22 for removing large pieces of debris.
As for the operation of the ionizing particle separator 1, it is important that the electrodes 5 and 6 have therebetween an active direct-voltage field with no alternating-current component. The result of this is that the ion beams of the electrode 5 do not yet develop ozone at this stage, as the gas flow contains plenty of particles. Only at the next stage, as the particles have been removed, is the generator 2 used for controlled production of singlet oxygen, but no more than the amount needed for the oxidation of gaseous compounds, and thus, for deodorizing the same. Thus, the exhaust gas does not contain ozone, either.

Claims

Claims
1. A method for cleaning gases, characterized in that, at a first stage, a gas is subjected to the removal of particles by flowing the gas through a particle separator (1) capable of ionizing particles and, at a second stage, the gas is subjected to the removal of harmful gaseous substances by oxidation, such that the gas flow is supplied with singlet oxygen by means of a singlet oxygen generator (2).
2. A method as set forth in claim 1, characterized in that the gas flow is analyzed by means of a gas analyzer (21), having its sampling points (16, 17) upstream and downstream of a singlet oxygen supply point, and the singlet oxygen generator (2) is controlled on the basis of analytical data.
3. An apparatus for cleaning gases, characterized in that the apparatus comprises an ionizing particle separator (1) for ionizing particles in a gas to be cleaned and for collecting the same from a gas flow by means of an electric field, and a singlet oxygen generator (2) downstream of the particle separator (1) in the gas flowing direction, which is adapted to supply singlet oxygen into the gas flow to be cleaned, as well as a degassing unit (3, 7) for removing harmful gaseous substances in an oxidized and odourless state.
4. A singlet oxygen generator for oxidizing gaseous substances, characterized in that the singlet oxygen generator (2) comprises a tube (13) of an electrically non-conducting material, an electrically conducting electrode (11) present inside the tube (13) and a spiral electrode (12) present outside the tube (13), a high-frequency high-voltage supply (10) present between first ends of the electrodes (11, 12), a jacket tube (14), providing a flow channel which houses the spiral electrode (12), and a fan (8) for blowing air through the flow channel, whereby a corona effect developing around the spiral electrode (12) breaks up oxygen molecules of the flowing gas to singlet oxygen.
5. An apparatus as set forth in claim 3, which is provided with a singlet oxygen generator as set forth in claim 4.
6. An apparatus as set forth in claim 3 or 5, characterized in that the apparatus is used for cleaning gases from a waste disposal plant and that the apparatus includes a gas analyzer (21) for analyzing the composition of a gas to be cleaned upstream and downstream of a singlet oxygen supply point.
PCT/FI2003/000108 2002-02-15 2003-02-12 Method, apparatus and singlet oxygen generator for cleaning gases Ceased WO2003068369A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2003205796A AU2003205796A1 (en) 2002-02-15 2003-02-12 Method, apparatus and singlet oxygen generator for cleaning gases

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI20020304 2002-02-15
FI20020304A FI117852B (en) 2002-02-15 2002-02-15 Process, apparatus and singlet acid generator for purification of gases

Publications (1)

Publication Number Publication Date
WO2003068369A1 true WO2003068369A1 (en) 2003-08-21

Family

ID=8563217

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/FI2003/000108 Ceased WO2003068369A1 (en) 2002-02-15 2003-02-12 Method, apparatus and singlet oxygen generator for cleaning gases

Country Status (3)

Country Link
AU (1) AU2003205796A1 (en)
FI (1) FI117852B (en)
WO (1) WO2003068369A1 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0308505A1 (en) * 1986-04-24 1989-03-29 Ebara Corporation Method and device for flue gas treatment by irradiation with electron beams
DE4425117A1 (en) * 1994-07-15 1996-01-25 Rheinische Braunkohlenw Ag Process and reactor assembly for incineration of de-watered industrial sludge
WO1998011982A1 (en) * 1996-09-20 1998-03-26 Thermo Power Corporation Preparation and use of independently generated highly reactive chemical species
JP3365819B2 (en) * 1993-05-10 2003-01-14 正 持麾 Method for producing dissolved oxygen in water

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0308505A1 (en) * 1986-04-24 1989-03-29 Ebara Corporation Method and device for flue gas treatment by irradiation with electron beams
JP3365819B2 (en) * 1993-05-10 2003-01-14 正 持麾 Method for producing dissolved oxygen in water
DE4425117A1 (en) * 1994-07-15 1996-01-25 Rheinische Braunkohlenw Ag Process and reactor assembly for incineration of de-watered industrial sludge
WO1998011982A1 (en) * 1996-09-20 1998-03-26 Thermo Power Corporation Preparation and use of independently generated highly reactive chemical species

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Week 200308, Derwent World Patents Index; Class D15, AN 1994-341691 *

Also Published As

Publication number Publication date
FI117852B (en) 2007-03-30
FI20020304A0 (en) 2002-02-15
AU2003205796A1 (en) 2003-09-04
FI20020304A7 (en) 2003-08-16

Similar Documents

Publication Publication Date Title
KR100239017B1 (en) Apparatus and method for removing indoor air pollutants using corona discharge
CN102791381B (en) For removing unexpected composition from air and getting rid of the apparatus and method of this composition
US7959884B2 (en) Apparatus for purifying air and purifying method thereof
US7318857B2 (en) Dual flow wet electrostatic precipitator
JP5400379B2 (en) Particle extraction apparatus in air by semi-wet electrostatic collection and method of using the apparatus
US7297182B2 (en) Wet electrostatic precipitator for treating oxidized biomass effluent
Hołub et al. Plasma supported odour removal from waste air in water treatment plants: An industrial case study
US7459009B2 (en) Method and apparatus for flue gas desulphurization
KR20010068436A (en) Apparatus for removing and deodorizing volatile organic compound by using corona plasma
JPH10325A (en) Removal device for volatile organic compounds in air using discharge plasma
WO2003068369A1 (en) Method, apparatus and singlet oxygen generator for cleaning gases
JPH06190236A (en) Gas cleaning method and device
Liqiang et al. Effects of water vapor on flue gas conditioning in the electric fields with corona discharge
KR20180006021A (en) Electrical dust precipitator
JP2005246353A (en) Gas reforming apparatus
CN107486002A (en) A kind of ceramic decoration firing smoke eliminator
CN208591698U (en) Low temperature plasma electroplating sludge desiccation odor treating device
CN107754573A (en) A kind of low-temperature plasma exhaust treatment system
KR20190066941A (en) Reduction apparatus for complex pollutants from semiconductor process
KR101194702B1 (en) Device for removing odorous gas using plasma discharge
CN107837658A (en) A kind of novel low temperature plasma processing equipment
KR100347649B1 (en) An improving method of dust collection efficiency in flue gas using plasma reaction
CN205065954U (en) Eliminate ion integrated device of ozone release
KR0133456B1 (en) Process for gas removal
KR20220118141A (en) Hazardous gas treatment device of waste synthetic resin recycling facility

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ OM PH PL PT RO RU SC SD SE SG SK SL TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LU MC NL PT SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
122 Ep: pct application non-entry in european phase
NENP Non-entry into the national phase

Ref country code: JP

WWW Wipo information: withdrawn in national office

Country of ref document: JP