GB2338660A - Optimisation of flow in gas treatment reactors - Google Patents
Optimisation of flow in gas treatment reactors Download PDFInfo
- Publication number
- GB2338660A GB2338660A GB9813482A GB9813482A GB2338660A GB 2338660 A GB2338660 A GB 2338660A GB 9813482 A GB9813482 A GB 9813482A GB 9813482 A GB9813482 A GB 9813482A GB 2338660 A GB2338660 A GB 2338660A
- Authority
- GB
- United Kingdom
- Prior art keywords
- annular space
- bed
- reactor
- active material
- gaseous medium
- 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.)
- Withdrawn
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9445—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC]
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/32—Separation 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 by electrical effects other than those provided for in group B01D61/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
- B01J8/0214—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a cylindrical annular shaped bed
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/0892—Electric or magnetic treatment, e.g. dissociation of noxious components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J2219/0803—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
- B01J2219/0805—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy giving rise to electric discharges
- B01J2219/0807—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy giving rise to electric discharges involving electrodes
- B01J2219/0809—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy giving rise to electric discharges involving electrodes employing two or more electrodes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J2219/0803—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
- B01J2219/0805—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy giving rise to electric discharges
- B01J2219/0807—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy giving rise to electric discharges involving electrodes
- B01J2219/0824—Details relating to the shape of the electrodes
- B01J2219/0826—Details relating to the shape of the electrodes essentially linear
- B01J2219/083—Details relating to the shape of the electrodes essentially linear cylindrical
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J2219/0894—Processes carried out in the presence of a plasma
-
- 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Abstract
A reactor 1 for the processing of a gaseous medium including a cylindrical reactor chamber 2 within which there is a hollow cylindrical bed 11 of active material 12, and the annular space 18, 311 between the outside of the bed of active material and the reactor chamber is arranged to provide an impedance to axial gas flow which increases in the direction of gas flow along the said annular spaces. The gases are constrained to flow through the bed by the tapered wall (Fig 5). In the embodiment the device is a plasma-assisted gas reactor, with co-axial perforated cylindrical electrodes 6 and 7 defining the borders of the active bed.
Description
1 - 2338660 The Qptimisation of Gas Flow in Reactors for the Treatment of
Gaseous Media The present invention relates to reactors for the treatment of gaseous media and, more specifically to reactors for the removal of noxious substances from the exhaust gases from internal combustion engines.
One type of reactor for the treatment of gaseous media consists of a cylindrical reactor chamber which has inlet and outlet ports by means of which it can be connected into a gas flow system. Inside the reactor chamber,- and co-axial within it, is a hollow cylindrical gas permeable bed of active material. The bed of active material is held in place by two supporting disks made of an impermeable material. One support disk has a ring of axially directed holes around its periphery and the other disk has a central hole the diameter of which is approximately equal to the inside diameter of the cylindrical bed of active material. In use a gaseous medium to be processed is admitted to the reactor chamber via the port closer to the first support disk. The gaseous medium is then directed into the annular space between the outside of the cylindrical bed of active material and the wall of the reactor chainber. The closure of this space by the other support disk constrains the gaseous medium to pass radially through the bed of activate material prior to leaving the reactor via the central electrode. The support disks are made of a temperature resistant insulating material and there is provided an electrical connection to the inner electrode by means of which a potential of some kilovolts can be applied to the inner electrode so as to establish a plasma discharge in the gaseous medium in the interstices in the gas permeable bed of active material.
In practice, it has been found that the gas flow distribution through the bed of active material of such a reactor is unev'-en, being greater at the downstream end of the bed of active material. Thus the reactor may not operate at its maximum efficiency because the upstream end of the bed of active material may be underused while the downstream end of the bed of active material may be subjected to a higher rate of gas flow than it can usefully process.
It is an object of the present invention to provide an improved reactor of the type described above for the processing of a gaseous medium.
1 According to the preset invention there is provided a reactor for the treatment of a gaseous medium, including a cylindrical reactor chamber having an inlet port and an outlet port for a gaseous medium to be processed, a hollow cylindrical gas permeable bed of an active material contained within the reactor chamber and co-axial therewith, an annular space between the outside of the bed of'active material and the inside of the reactor chamber and means for constraining the gaseous medium to enter the said annular space at one end in an axial direction, and pass radially through the bed of active material, wherein the said annular space is configured to provide an impedance to the flow of the gaseous medium which increases along the length of the said annular space.
The increasing impedance to the axial flow of the gaseous medium through the said annular space preferably is provided by progressively reducing the cross-sectional area of the said annular space. The reduction in the cross-sectional area of the said annular space may be continuous, but preferably is discontinuous. A preferred arrangement has two step reductions in the cross sectional area of the said annular space, the first being greater than the second.
According to the present invention in a particular aspect the reactor is for the plasma-assisted treatment of gaseous media, the bed of active material is contained between two gas permeable co-axial disks and two support disks made of an impermeable temperature-resistant insulating material, the support disk nearer the inlet end of the reactor has a plurality of axially directed gas passages around its periphery, and the support disk nearer the outlet end of the reactor has a central hole the diameter of which is substantially equal to the internal diameter of the inner electrode so that a gaseous medium to be processed enters the annular space between the outer electrode and the wall of the reactor chamber axially but is constrained to pass radially through the bed of active material.
Preferably the active material is adapted to remove nitrogenous oxides and carbonaceous combustion products from the exhaust emissions from internal combustion engines.
The invention will now be described, by way of example, with reference to the accompanying drawings, in which:
Figure 1 is a schematic longitudinal section of an existing type of reactor for the plasma-assisted processing of a gaseous medium; Figure 2 illustrates how the radial component of gas flow through a bed of active material included in the reactor of Figure 1 varies with distance along the reactor bed from the entrance to the active region of the reactor; Figure 3 is a schematic longitudinal half-section of a first reactor embodying the invention for the processing of a gaseous medium; Figure 4 is a schematic longitudinal half-section of a second reactor embodying the invention for the processing of a gaseous medium; Figure 5 is a schematic longitudinal half-section of a third reactor embodying the invention for the processing of a gaseous medium; is Figure 6 is a flow diagram showing the radial components of gas flow for the embodiment of Figure 3; Figure 7 is a flow diagram showing the radial component of gas flow for the embodiment of Figure 4; Figure 8 is a flow diagram showing the radial component of gas flow for the embodiment of Figure 5; and Figure 9 is a schematic longitudinal half-section of a fourth embodiment of the invention.
Referring to Figure 1, a reactor 1 for the plasmaassisted processing of a gaseous medium consists of a stainless chamber 2 which has an inlet stub 3 and an outlet stub 4. The chamber 2 is arranged, in use, to be connected to an earthing point 5. Perforated cylindrical stainless steel electrodes 6 and 7 and positioned coaxially within the chamber 2 by means of two impervious electrically-insulating supports 8 and 9. The space 10 bounded by the electrodes 6 and 7 and the insulating - 5 supports is filled with a bed 11 of pellets 12 of an active material which has a dielectric constant suf f icient to enable a plasma to be established and maintained in the gaseous medium in the interstices between the pellets 12 of the bed 11 of active material. The upstream end 13 of the inner electrode 6 is closed off and arranged to be connected via an insulating feedthrough 14 to a source 15 of an electrical potential sufficient to excite the above-mentioned plasma in the gaseous medium.
The upstream electrode support 8 has a ring of axially-oriented gas passages 16 around its periphery, whereas the downstream electrode support 9 has a central hole 17 in it of approximately the same diameter as the internal diameter of the inner electrode 6. Thus, in use, a gaseous medium to be processed is directed axially into the annular space 18 between the outer electrode 7 and the wall of the chamber 2. As the gas cannot escape from the downstream end of the space 18, it is constrained to enter the bed 11 of active material and pass radially through it.
Figure 2 is a flow diagram showing how the radial component of gas flow for such a reactor varies along the length of the bed of active material. It can be seen that there is very little radial flow through the bed 11 for almost half its length and the radial gas flow increases progressively along the remainder of the bed 11 of active material. Thus, the overall efficiency of the bed 11 of active material is much below that which would be achieved if the radial flow of gas through the bed 11 of the reactor was regular. At present the active material at the downstream end of the reactor may be saturated while that at the upstream end of the reactor largely is unused.
6 - The present invention seeks to overcome this problem by progressively increasing the resistance to axial flow along the annular space 18 between the wall 2 of the reactor 1 and the outer electrode. Figures 3, 4 and 5 illustrate three ways in which this increase in the resistance to axial flow of the gaseous medium can be achieved.
Unlike Figure 1, these figures are half-sections and extraneous detail has been omitted. However, those parts which are common to all three figures have the same reference numerals.
Referring to Figure 3, a reactor for the processing of a gaseous medium consists of a reactor chamber 300 which has inlet and outlet fixing stubs 301 and 302, respectively. Within the reactor chamber 300 is a hollow cylindrical gas permeable bed 303 made of an active material adapted to carry out a desired process an the gaseous medium. For example, the active material may be adapted to catalyse a reaction between one or more components of the gaseous medium. The bed 303 of active materials is contained between two co-axial cylindrical support members 304 and 305, which are gas permeable and two disk transverse supports 306 and 307, made of an unpermeable material, as in the reactor described with reference to Figure 1. If the bed 303 is made of a material which is self supporting, the support members 304 and 305 can be omitted. As before, the support 306 nearer the inlet to the reactor chamber 300 has a number of axially directed gas passages 308 around its periphery and the support 307 nearer the outlet from the reactor chamber 300 has a central hole 309 of approximately the same diameter as the inner active bed support member 304. The inner active bed support 304 has a closed, domed end 310 which projects through the support 306 and facilitates the deflection of the incoming gaseous medium towards the periphery of the reactor chamber 300. As with the reactor previously described, a gaseous medium entering the reactor chamber 300 is directed into the annular space 311 between the outer active bed support 305 and the wall of the reactor chamber 300 initially in an axial direction but is then constrained to pass radially through the bed 303 of active material.
However, in the present case, the reactor chamber 300 is not a true cylinder, but tapers in the direction of gas flow along the space 311 between the outer active bed support 305 and the wall of the reactor 300. As a result, the impedance to axial gas flow increases along the annular space 311 between the outer active bed support 305 and the wall of the reactor chamber 300, so increasing the amount of gaseous medium which flows radially through the upstream part of the bed 303 of active material. A suitable taper angle is in the region of two degrees.
Figure 4 shows a second embodiment of the invention in which the diameter of the reactor chamber 300 is reduced half way along the bed 303 of active material. In a particular example, the width of the annular space 311 between the outer active bed support 305 and the wall of the reactor chamber is 10 mm initially and 5 mm for the second part of the reactor chamber 300. All other components are as for the reactor described with reference to Figure 3.
Figure 5 shows another embodiment of the invention in which there is a second step-wise reduction in the width of the annular space 311 between the outer active bed support 305 and the wall of the reactor chamber 300 8 - half way along the second part of the bed 303 of active material. In another specific case, the widths of the regions of the-annular space 311 between the outer active bed support 305 and the wall of the reactor chamber 300 5 are 10, 5 and 3 mm.
Figure 6 is a diagram showing the variation in radial gas flow along the bed 303 of active material for the embodiment of Figure 3. Compared with Figure 2 it can be seen that much more gas passes radially through first half of the bed 303 of active material. In fact the distribution of radial gas flow along the length of the bed 303 of active material is now approximately, symmetrical, but the middle two fifths, approximately of the bed 303 of active material still are underused.
Figure 7 is a diagram showing the variation in radial gas flow along the bed 303 of active material for the embodiment of Figure 4. more gas now passes radially through the first half of the bed 303 of active material than through the second half, with an intermediate peak at the position of the step where the width of the annular space 311 between the outer active bed support 305 and the wall of the reactor chamber 300 is halved.
Immediately downstream of this position the radial gas flow rate is less than half that before it. This region of low gas flow extends about one fifth of the length of the bed 303 of active material.
Figure 8 is another gas flow diagram, similar to those of Figures 6 and 7, for the embodiment of Figure 5.
It can be seen that this embodiment of the invention gives the most even distribution of radial gas flow through the bed 303 of active material.
1 1 9 - Figure 9 shows another embodiment of the invention in which the opposite approach to the problem is adopted. In this embodiment of the invention, instead of reducing the width of the gap 311 between the outer active bed support 305 and the wall of the reactor chamber 300 along the length of the bed 303 of active material so as to cause more gas to be diverted radially in the upstream regions of the bed 303 of active material, a number of axial expansion chambers 901 are provided along the first part of the reactor chamber 300. In this arrangement, not only is the impedance to axial gas flow higher in the second region of the reactor 300 than in the first region, but the expansion chambers 901 reduce the pressure of the gaseous medium as it enters the second region of the reactor chamber 300.
The invention has been described above in connection with gas reactors in general. As before, if the reactor is for use in the plasma-assisted processing of gaseous media, specifically, the treatment of the exhaust emissions from internal combustion engines to remove noxious combustion products therefrom, then the inner and outer active bed supports 304 and 305 are made of a metal such as stainless steel and used as electrodes, the outer one being earthed, as is the reactor chamber 300. Also, the transverse supports 306 and 307 have to be made of a temperature resistant insulating material. The material of the active bed 303 has to have a dielectric constant sufficient to enable a plasma to be established and maintained in the interstices within the bed of active material.
- 10
Claims (10)
1. A reactorfor the treatment of a gaseous medium, including a cylindrical reactor chamber having an inlet port and an outlet port for a gaseous medium to be processed, a hollow cylindrical gas permeable bed of an active material contained within the reactor chamber and co-axial therewith, an annular space between the outside of the bed of active material and the inside of the reactor chamber and means for constraining the gaseous medium to enter the said annular space at one end in an axial direction, and pass radially through the bed of active material, wherein the said annular space is configured to provide an impedance to the flow of the gaseous medium which increases along the length of the said annular space.
2. A reactor according to Claim 1 wherein the width of the said annular space decreases continuously along the length of the said annular space.
A reactor according to Claim 1 wherein there is at least one discontinuous decrease in the width of the said annular space along the length of the said annular space.
4. A reactor according to Claim 3 wherein there is a single discontinuous decrease in the width of the said annular space approximately at the middle of the said annular space.
5. A reactor according to Claim 3 wherein there are two discontinuous decreases in the width of the said annular space.
6. A reactor according to Claim 5 wherein the first discontinuous decrease in the width of the said annular space occurs approximately at the middle of the said annular space and the second discontinuous decrease In the width of the annular space occurs approximately three quarters along the length of the said annular space.
7. A reactor according to Claim 5 wherein the second discontinuous decrease in the width of the said annular space is less than the first discontinuous decrease in the width of the said annular space.
8. A reactor according to Claim 1 wherein a first portion of the reactor chamber is provided with axially extending expansion chambers.
9. A reactor according to any-preceding claim wherein the bed of active material is contained between two coaxial gas permeable electrodes and two unpermeable transverse insulating supports, the transverse support nearer the inlet port to the reactor has a plurality of axially directed gas flow passages disposed around its periphery, the transverse support has a central hole the diameter of which is approximately equal to the diameter of the inner co-axial electrode and there is provided means for applying to the inner electrode a potential sufficient to excite and maintain a plasma in a gaseous medium passing through the bed of active material.
10. A reactor for the processing of a gaseous medium substantially as hereinbefore described and with reference to Figures 3 to 9 of the accompanying drawings.
15245 LgCm P.A. Wood Chartered Patent Agent Agent for the Applicants
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9813482A GB2338660A (en) | 1998-06-24 | 1998-06-24 | Optimisation of flow in gas treatment reactors |
DE69901613T DE69901613T2 (en) | 1998-06-24 | 1999-06-16 | GAS FLOW OPTIMIZATION IN GAS TREATMENT REACTORS |
AU43809/99A AU4380999A (en) | 1998-06-24 | 1999-06-16 | The optimisation of gas flow in reactors for the treatment of gaseous media |
JP2000556136A JP2002519166A (en) | 1998-06-24 | 1999-06-16 | Techniques for optimizing gas flow in gaseous media processing reactors |
PCT/GB1999/001912 WO1999067510A1 (en) | 1998-06-24 | 1999-06-16 | The optimisation of gas flow in reactors for the treatment of gaseous media |
AT99926626T ATE218187T1 (en) | 1998-06-24 | 1999-06-16 | GAS FLOW OPTIMIZATION IN GAS TREATMENT REACTORS |
ES99926626T ES2178443T3 (en) | 1998-06-24 | 1999-06-16 | OPTIMIZATION OF GAS FLOW IN REACTORS FOR THE TREATMENT OF GASEOUS MEDIA. |
EP99926626A EP1090212B1 (en) | 1998-06-24 | 1999-06-16 | The optimisation of gas flow in reactors for the treatment of gaseous media |
KR1020007014608A KR20010053111A (en) | 1998-06-24 | 1999-06-16 | The optimisation of gas flow in reactors for the treatment of gaseous media |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9813482A GB2338660A (en) | 1998-06-24 | 1998-06-24 | Optimisation of flow in gas treatment reactors |
Publications (2)
Publication Number | Publication Date |
---|---|
GB9813482D0 GB9813482D0 (en) | 1998-08-19 |
GB2338660A true GB2338660A (en) | 1999-12-29 |
Family
ID=10834203
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9813482A Withdrawn GB2338660A (en) | 1998-06-24 | 1998-06-24 | Optimisation of flow in gas treatment reactors |
Country Status (9)
Country | Link |
---|---|
EP (1) | EP1090212B1 (en) |
JP (1) | JP2002519166A (en) |
KR (1) | KR20010053111A (en) |
AT (1) | ATE218187T1 (en) |
AU (1) | AU4380999A (en) |
DE (1) | DE69901613T2 (en) |
ES (1) | ES2178443T3 (en) |
GB (1) | GB2338660A (en) |
WO (1) | WO1999067510A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2370518A (en) * | 2000-12-15 | 2002-07-03 | Aea Technology Plc | Plasma gas purification using a metal hydroxide |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1213052A1 (en) * | 2000-12-09 | 2002-06-12 | Degussa AG | Electrically heated fixed bed reactor and use thereof |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4457895A (en) * | 1981-10-13 | 1984-07-03 | Institut Francais Du Petrole | Catalytic muffler for purifying the exhaust gases of an internal combustion engine |
US4876072A (en) * | 1988-05-16 | 1989-10-24 | Checki Edward T | Catalytic converter with screen enclosure holding pellets under tension |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4390354A (en) * | 1980-03-12 | 1983-06-28 | Witchell Stanley P | Air filters |
US4419113A (en) * | 1982-07-08 | 1983-12-06 | General Motors Corporation | Diesel exhaust particulate trap with axially stacked filters |
US4954320A (en) * | 1988-04-22 | 1990-09-04 | The United States Of America As Represented By The Secretary Of The Army | Reactive bed plasma air purification |
US5632792A (en) * | 1995-08-16 | 1997-05-27 | Purolator Products Company | Air induction filter hose assembly |
ATE201331T1 (en) * | 1997-09-09 | 2001-06-15 | Aea Technology Plc | TREATMENT OF EXHAUST GASES |
-
1998
- 1998-06-24 GB GB9813482A patent/GB2338660A/en not_active Withdrawn
-
1999
- 1999-06-16 ES ES99926626T patent/ES2178443T3/en not_active Expired - Lifetime
- 1999-06-16 JP JP2000556136A patent/JP2002519166A/en active Pending
- 1999-06-16 DE DE69901613T patent/DE69901613T2/en not_active Expired - Fee Related
- 1999-06-16 AT AT99926626T patent/ATE218187T1/en active
- 1999-06-16 KR KR1020007014608A patent/KR20010053111A/en not_active Application Discontinuation
- 1999-06-16 EP EP99926626A patent/EP1090212B1/en not_active Expired - Lifetime
- 1999-06-16 WO PCT/GB1999/001912 patent/WO1999067510A1/en not_active Application Discontinuation
- 1999-06-16 AU AU43809/99A patent/AU4380999A/en not_active Abandoned
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4457895A (en) * | 1981-10-13 | 1984-07-03 | Institut Francais Du Petrole | Catalytic muffler for purifying the exhaust gases of an internal combustion engine |
US4876072A (en) * | 1988-05-16 | 1989-10-24 | Checki Edward T | Catalytic converter with screen enclosure holding pellets under tension |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2370518A (en) * | 2000-12-15 | 2002-07-03 | Aea Technology Plc | Plasma gas purification using a metal hydroxide |
Also Published As
Publication number | Publication date |
---|---|
AU4380999A (en) | 2000-01-10 |
ES2178443T3 (en) | 2002-12-16 |
GB9813482D0 (en) | 1998-08-19 |
DE69901613D1 (en) | 2002-07-04 |
DE69901613T2 (en) | 2002-12-05 |
KR20010053111A (en) | 2001-06-25 |
EP1090212A1 (en) | 2001-04-11 |
JP2002519166A (en) | 2002-07-02 |
ATE218187T1 (en) | 2002-06-15 |
WO1999067510A1 (en) | 1999-12-29 |
EP1090212B1 (en) | 2002-05-29 |
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