WO2016150465A1 - Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases - Google Patents

Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases Download PDF

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Publication number
WO2016150465A1
WO2016150465A1 PCT/EP2015/055952 EP2015055952W WO2016150465A1 WO 2016150465 A1 WO2016150465 A1 WO 2016150465A1 EP 2015055952 W EP2015055952 W EP 2015055952W WO 2016150465 A1 WO2016150465 A1 WO 2016150465A1
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WO
WIPO (PCT)
Prior art keywords
filter
gas
ceramic
silicates
scr
Prior art date
Application number
PCT/EP2015/055952
Other languages
French (fr)
Inventor
Francesco Castellino
Lars Storm PEDERSEN
Original Assignee
Haldor Topsøe A/S
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 Haldor Topsøe A/S filed Critical Haldor Topsøe A/S
Priority to PCT/EP2015/055952 priority Critical patent/WO2016150465A1/en
Priority to CN201580077976.1A priority patent/CN107427771B/en
Priority to CA2976131A priority patent/CA2976131C/en
Priority to US15/545,499 priority patent/US10105682B2/en
Priority to JP2017546964A priority patent/JP6571788B2/en
Priority to EP15711179.0A priority patent/EP3271050A1/en
Priority to KR1020177021030A priority patent/KR102424112B1/en
Priority to EP15720318.3A priority patent/EP3271051A1/en
Priority to PCT/EP2015/059192 priority patent/WO2016150523A1/en
Priority to CN201580077977.6A priority patent/CN107427772B/en
Priority to US15/545,517 priority patent/US10232352B2/en
Priority to JP2017546958A priority patent/JP6576461B2/en
Priority to KR1020177021032A priority patent/KR102454125B1/en
Priority to CA2976143A priority patent/CA2976143C/en
Priority to TW104114109A priority patent/TWI652100B/en
Priority to ARP160100631A priority patent/AR103898A1/en
Publication of WO2016150465A1 publication Critical patent/WO2016150465A1/en

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    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
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    • B01D53/34—Chemical or biological purification of waste gases
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    • B01D53/8646—Simultaneous elimination of the components
    • B01D53/865—Simultaneous elimination of the components characterised by a specific catalyst
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    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases
    • B01D2258/0291—Flue gases from waste incineration plants
    • 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
    • B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
    • 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
    • F01N2370/00—Selection of materials for exhaust purification
    • F01N2370/02—Selection of materials for exhaust purification used in catalytic reactors
    • 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
    • F01N2510/00—Surface coverings
    • F01N2510/06—Surface coverings for exhaust purification, e.g. catalytic reaction
    • F01N2510/068—Surface coverings for exhaust purification, e.g. catalytic reaction characterised by the distribution of the catalytic coatings
    • 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

Definitions

  • the present invention relates to ceramic candle filters and a method for cleaning of off- or exhaust gases. More par ⁇ ticularly, the invention provides a catalyzed ceramic can ⁇ dle filter for the removal of dust and particulate matter in a process gas and harmful components contained in the process gas.
  • the catalyzed ceramic candle filter is in par- ticular useful in the cleaning of process or raw gas from industrial processes involving combustion, like the produc ⁇ tion of minerals, glass, cement, waste incineration, or from coal fired boilers and engines.
  • Ceramic filters in form of filter candles are used in many industries for removal of particulate matter from process gases. They are one of the most efficient types of dust collectors available and can achieve collection efficien ⁇ cies of more than 99% for particulates.
  • the filters can be made from various ceramic materials comprising ceramic fi ⁇ bres made of alkali and alkaline earth silicates, or alumi- no silicates.
  • the high particulate removal efficiency of ceramic candle filters is partly due to the dust cake formed on the sur ⁇ faces of the candle filter and partly due to the candle filter composition and porosity.
  • conventional ceramic candle filters have a porosity of between 70 and 90%.
  • the wall thickness of those filters should be in the range of 10-20 mm for sufficient stability and mechanical strength.
  • Particle-containing process off-gas and engine exhaust gas often contains a plurality of pollutants, e.g. NO x , vola ⁇ tile organic compounds (VOC) , SO 2 , CO, N3 ⁇ 4, dioxins and fu- rans, in concentrations that have to be reduced depending on local legislation.
  • pollutants e.g. NO x , vola ⁇ tile organic compounds (VOC) , SO 2 , CO, N3 ⁇ 4, dioxins and fu- rans, in concentrations that have to be reduced depending on local legislation.
  • VOC vola ⁇ tile organic compounds
  • va- nadium oxide-based catalysts are commonly used catalysts for NO x reduction by selective reduction of NO x with N3 ⁇ 4 in stationary and automotive applications.
  • This catalyst is active both in the oxidative removal of hydrocarbons (VOC) and in the selective catalytic reduction (SCR) of NOx by reaction with NH 3 .
  • the vanadium oxide catalyst is less selective in the formation of CO 2 and some amounts of CO are produced during the oxidation reactions. CO cannot be oxidized to CO 2 at a feasible reaction rate by contact with the vanadi ⁇ um oxide catalyst.
  • a catalyst comprising both vanadium oxide and palladium results in an effective oxidation of hydrocarbons and soot together with ammonia-SCR of NOx and a lower slip of ammo ⁇ nia and carbon monoxide from the filter.
  • the present invention provides a ceramic candle filter suitable for the removal of partic ⁇ ulate matter in form of soot, ash, metals and metal com ⁇ pounds, together with hydrocarbons and nitrogen oxides be ⁇ ing present in process off-gas or engine exhaust gas, the filter comprises a combined SCR and oxidation catalyst ar ⁇ ranged at least on the dispersion side and/or within wall of the filter, the combined SCR and oxidation catalyst com ⁇ prises palladium, a vanadium oxide and titania.
  • the terms "dispersion side” and “permeate side” as used herein refer to the flow side of the filter facing the un- filtered exhaust gas and to flow side facing the filtered off- or exhaust gas, respectively.
  • the invention provides additionally a method for the remov ⁇ al of particulate matter in form of soot, ash, metals and metal compounds, together with hydrocarbons and nitrogen oxides being present in process off-gas or engine exhaust gas, comprising the steps of
  • SCR selective cata ⁇ lytic reduction
  • a vanadium oxide or “vanadium oxide” refers to: Vanadium ( I I ) oxide (vanadium monoxide), VO; or
  • vanadium ( I I I ) oxide vanadium sesquioxide or trioxide
  • V 2 0 3 vanadium sesquioxide or trioxide
  • vanadium (IV) oxide vanadium dioxide
  • VO 2 vanadium dioxide
  • V vanadium oxide
  • vanadium pentoxide vanadium pentoxide
  • vanadium oxide for use in the invention comprises or consists of vanadium (V) oxide (vanadium pentox ⁇ ide), V 2 0 5 .
  • V vanadium oxide
  • titanium dioxide T1O 2
  • the catalytically active form of palladium is palladium in the metallic and/or oxidic form.
  • the shortage Pd/V/Ti shall mean a catalyst consisting of palladium, a vanadium oxide and titania.
  • the Pd/V/Ti catalyst has i) dual functionality (removal of NOx and removal of VOC, volatile organic compounds) ; ii) a S-tolerance ; and iii) a lower SO 2 oxidation activity com ⁇ pared to other catalyst compositions, e.g. Pt-based cata ⁇ lysts.
  • the catalyzed filter can- dies are sulfur resistant, i.e. not subjected to sulfur de ⁇ activation.
  • the Pd/V/Ti catalyst additionally reduces the amount of SO 3 formed by oxidation of SO 2 . If 3 ⁇ 4S is also present in the process gas entering the filter, it will al ⁇ so be oxidized to SO 2 on the Pd/V/Ti catalyst.
  • the catalytically active material may be applied on the ce- ramie filter by impregnation with a slurry containing the catalytically active material in form of titania micro- particles and the precursors of the active materials, i.e. salts of vanadium and palladium.
  • a slurry containing the catalytically active material in form of titania micro- particles and the precursors of the active materials, i.e. salts of vanadium and palladium Once impregnated, the fil ⁇ ter is subsequently dried and heated up to the required temperature for the decomposition of all precursors and ac ⁇ tivation of the catalyst.
  • the catalyst employed in the invention contains palladium in an amount of between 20 and 1000 ppm/weight of the filter, preferably less than 200
  • fibers may be used for their production. These can be constituted e.g. by silica-aluminate and calcium- silicates fibers, or a mixture thereof.
  • Other preferred ceramic fibres comprise bio-soluble fibres selected from the group of calcium-magnesium-silicates.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Toxicology (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)
  • Dispersion Chemistry (AREA)
  • Processes For Solid Components From Exhaust (AREA)
  • Filtering Materials (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Exhaust Gas After Treatment (AREA)

Abstract

Ceramic candle filter and use of the filter in the removal of particulate matter in form of soot, ash, metals and metal compounds, together with hydrocarbons and nitrogen oxides being present in process off-gas or engine exhaust gas, the filter comprises a combined SCR and oxidation catalyst arranged at least on the dispersion side and/or with in wall of the filter, the combined SCR and oxidation catalyst comprises palladium, a vanadium oxide and titania.

Description

Title: Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases
The present invention relates to ceramic candle filters and a method for cleaning of off- or exhaust gases. More par¬ ticularly, the invention provides a catalyzed ceramic can¬ dle filter for the removal of dust and particulate matter in a process gas and harmful components contained in the process gas. The catalyzed ceramic candle filter is in par- ticular useful in the cleaning of process or raw gas from industrial processes involving combustion, like the produc¬ tion of minerals, glass, cement, waste incineration, or from coal fired boilers and engines. Ceramic filters in form of filter candles are used in many industries for removal of particulate matter from process gases. They are one of the most efficient types of dust collectors available and can achieve collection efficien¬ cies of more than 99% for particulates. The filters can be made from various ceramic materials comprising ceramic fi¬ bres made of alkali and alkaline earth silicates, or alumi- no silicates.
The high particulate removal efficiency of ceramic candle filters is partly due to the dust cake formed on the sur¬ faces of the candle filter and partly due to the candle filter composition and porosity. In order to provide suffi¬ cient filtration activity and an acceptable low pressure drop over the filter conventional ceramic candle filters have a porosity of between 70 and 90%. The wall thickness of those filters should be in the range of 10-20 mm for sufficient stability and mechanical strength. Particle-containing process off-gas and engine exhaust gas often contains a plurality of pollutants, e.g. NOx, vola¬ tile organic compounds (VOC) , SO2, CO, N¾, dioxins and fu- rans, in concentrations that have to be reduced depending on local legislation. For this purpose, several conventional methods are available. The abatement of gaseous contami¬ nants like ΝΟχ, VOC, dioxins and furans can be effectively carried out by contact with a catalyst. In particular, va- nadium oxide-based catalysts are commonly used catalysts for NOx reduction by selective reduction of NOx with N¾ in stationary and automotive applications.
This catalyst is active both in the oxidative removal of hydrocarbons (VOC) and in the selective catalytic reduction (SCR) of NOx by reaction with NH3.
In comparison to the precious metal catalysts, like the Pd catalyst, the vanadium oxide catalyst is less selective in the formation of CO2 and some amounts of CO are produced during the oxidation reactions. CO cannot be oxidized to CO2 at a feasible reaction rate by contact with the vanadi¬ um oxide catalyst. We have found that when providing the candle filter with a catalyst comprising both vanadium oxide and palladium results in an effective oxidation of hydrocarbons and soot together with ammonia-SCR of NOx and a lower slip of ammo¬ nia and carbon monoxide from the filter.
Pursuant to this finding, the present invention provides a ceramic candle filter suitable for the removal of partic¬ ulate matter in form of soot, ash, metals and metal com¬ pounds, together with hydrocarbons and nitrogen oxides be¬ ing present in process off-gas or engine exhaust gas, the filter comprises a combined SCR and oxidation catalyst ar¬ ranged at least on the dispersion side and/or within wall of the filter, the combined SCR and oxidation catalyst com¬ prises palladium, a vanadium oxide and titania. The terms "dispersion side" and "permeate side" as used herein refer to the flow side of the filter facing the un- filtered exhaust gas and to flow side facing the filtered off- or exhaust gas, respectively. The invention provides additionally a method for the remov¬ al of particulate matter in form of soot, ash, metals and metal compounds, together with hydrocarbons and nitrogen oxides being present in process off-gas or engine exhaust gas, comprising the steps of
providing a process off-gas or engine exhaust gas contain¬ ing a nitrogenous reductant or adding the nitrogenous re- ductant to the off- or exhaust gas;
passing the off-gas or the exhaust through a ceramic candle filter and capturing the particulate matter; and
reducing amounts of soot in the particulate matter captured on the at least one particulate filter and reducing amounts of nitrogen oxides and hydrocarbons in the off- or exhaust gas by oxidation of the hydrocarbons and by selective cata¬ lytic reduction (SCR) of the nitrogen oxides with the ni- trogenous reductant in contact with a combined SCR and oxi¬ dation catalyst being arranged on the dispersion side and/or within wall of the filter, wherein the combined SCR and oxidation catalyst comprises palladium, a vanadium oxide and titania.
The term "a vanadium oxide" or "vanadium oxide" refers to: Vanadium ( I I ) oxide (vanadium monoxide), VO; or
vanadium ( I I I ) oxide (vanadium sesquioxide or trioxide) , V203; or
vanadium ( IV) oxide (vanadium dioxide), VO2; or
vanadium (V) oxide (vanadium pentoxide) , V2O5.
Preferably, vanadium oxide for use in the invention comprises or consists of vanadium (V) oxide (vanadium pentox¬ ide), V205. The term "titania" refers to titanium dioxide (T1O2) .
The catalytically active form of palladium is palladium in the metallic and/or oxidic form. The shortage Pd/V/Ti shall mean a catalyst consisting of palladium, a vanadium oxide and titania.
The Pd/V/Ti catalyst has i) dual functionality (removal of NOx and removal of VOC, volatile organic compounds) ; ii) a S-tolerance ; and iii) a lower SO2 oxidation activity com¬ pared to other catalyst compositions, e.g. Pt-based cata¬ lysts.
When employing a Pd/V/Ti catalyst the catalyzed filter can- dies are sulfur resistant, i.e. not subjected to sulfur de¬ activation. The Pd/V/Ti catalyst additionally reduces the amount of SO3 formed by oxidation of SO2. If ¾S is also present in the process gas entering the filter, it will al¬ so be oxidized to SO2 on the Pd/V/Ti catalyst.
The catalytically active material may be applied on the ce- ramie filter by impregnation with a slurry containing the catalytically active material in form of titania micro- particles and the precursors of the active materials, i.e. salts of vanadium and palladium. Once impregnated, the fil¬ ter is subsequently dried and heated up to the required temperature for the decomposition of all precursors and ac¬ tivation of the catalyst.
Compared to monolithic formed filters or wall flow filters, the effective gas contact between the palladium metal par- tides and reactants in gas is much higher, which results in a much reduced amount of palladium necessary to obtain a reasonable oxidation activity.
Typically, the catalyst employed in the invention the cata- lyst contains palladium in an amount of between 20 and 1000 ppm/weight of the filter, preferably less than 200
ppm/weight .
In the case of high temperature ceramic filters several types of fibers may be used for their production. These can be constituted e.g. by silica-aluminate and calcium- silicates fibers, or a mixture thereof.
Other preferred ceramic fibres comprise bio-soluble fibres selected from the group of calcium-magnesium-silicates.

Claims

Claims
1. A ceramic candle filter suitable for the removal of particulate matter in form of soot, ash, metals and metal compounds, together with hydrocarbons and nitrogen oxides being present in process off-gas or engine exhaust gas, the filter comprises a combined SCR and oxidation catalyst ar¬ ranged at least on the dispersion side and/or within wall of the filter, the combined SCR and oxidation catalyst com- prises palladium, a vanadium oxide and titania.
2. The ceramic candle filter of claim 1, wherein the cat¬ alyst contains palladium in an amount of between 20 and 1000 ppm/weight of the filter, preferably between 20 and 200 ppm.
3. The ceramic candle filter according to claim 1 or 2, wherein the ceramic material of the filter is selected from the group of silica-aluminate, calcium-magnesium-silicates, calcium-silicates fibers, or a mixture thereof.
4. The ceramic candle filter according to any one of claims 1 to 3, wherein the ceramic material of the filter consists of bio-soluble fibres selected from the group of calcium-magnesium-silicates.
5. A method for the removal of particulate matter in form of soot, ash, metals and metal compounds, together with hy¬ drocarbons and nitrogen oxides being present in process off-gas or engine exhaust gas, comprising the steps of providing a process off-gas or engine exhaust gas contain¬ ing a nitrogenous reductant or adding the nitrogenous re- ductant to the off- or exhaust gas;
passing the off-gas or the exhaust through a ceramic candle filter and capturing the particulate matter; and
reducing amounts of soot in the particulate matter captured on the at least one particulate filter and reducing amounts of nitrogen oxides and hydrocarbons in the off- or exhaust gas by oxidation of the hydrocarbons and by selective cata- lytic reduction (SCR) of the nitrogen oxides with the ni¬ trogenous reductant in contact with a combined SCR and oxi¬ dation catalyst being arranged on the dispersion side and/or within wall of the filter, wherein the combined SCR and oxidation catalyst comprises palladium, a vanadium ox- ide and titania.
6. The method according to claim 5, wherein wherein combined oxidation and SCR catalyst contains palladium in an amount of between 20 and 1000 ppm/weight of the filter, preferably between 20 and 200 ppm.
7. The method of claim 5 or 6, wherein the ceramic mate¬ rial of the filter is selected from silica-aluminate, cal¬ cium-magnesium-silicates, calcium-silicates fibers, or a mixture thereof.
8. The method according to any one of of claim 5 to 6, wherein the ceramic material of the filter comprises bio- soluble fibres selected from the group of calcium- magnesium-silicates.
PCT/EP2015/055952 2015-03-20 2015-03-20 Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases WO2016150465A1 (en)

Priority Applications (16)

Application Number Priority Date Filing Date Title
PCT/EP2015/055952 WO2016150465A1 (en) 2015-03-20 2015-03-20 Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases
CN201580077976.1A CN107427771B (en) 2015-03-20 2015-03-20 Catalyzed ceramic candle filter and method for cleaning exhaust gas or waste gas
CA2976131A CA2976131C (en) 2015-03-20 2015-03-20 Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases
US15/545,499 US10105682B2 (en) 2015-03-20 2015-03-20 Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases
JP2017546964A JP6571788B2 (en) 2015-03-20 2015-03-20 Catalytic ceramic candle filter and method for cleaning off-gas or exhaust gas
EP15711179.0A EP3271050A1 (en) 2015-03-20 2015-03-20 Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases
KR1020177021030A KR102424112B1 (en) 2015-03-20 2015-03-20 Catalyzed Ceramic Candle Filters and Methods for Purification of Offgases or Exhaust Gases
EP15720318.3A EP3271051A1 (en) 2015-03-20 2015-04-28 Catalyzed ceramic candle filter and method of cleaning process off- or exhaust gases
PCT/EP2015/059192 WO2016150523A1 (en) 2015-03-20 2015-04-28 Catalyzed ceramic candle filter and method of cleaning process off- or exhaust gases
CN201580077977.6A CN107427772B (en) 2015-03-20 2015-04-28 Catalyzed ceramic candle filter and method for cleaning process exhaust or gas
US15/545,517 US10232352B2 (en) 2015-03-20 2015-04-28 Catalyzed ceramic candle filter and method of cleaning process off- or exhaust gases
JP2017546958A JP6576461B2 (en) 2015-03-20 2015-04-28 Catalytic ceramic candle filter and process off-gas or exhaust gas cleaning method
KR1020177021032A KR102454125B1 (en) 2015-03-20 2015-04-28 Catalyzed Ceramic Candle Filters and Methods for Purification of Process Offgases or Exhaust Gases
CA2976143A CA2976143C (en) 2015-03-20 2015-04-28 Catalyzed ceramic candle filter and method of cleaning process off- or exhaust gases
TW104114109A TWI652100B (en) 2015-03-20 2015-05-04 Catalytic ceramic core filter and method for cleaning process discharge or gas consumption
ARP160100631A AR103898A1 (en) 2015-03-20 2016-03-10 CATALYZED CERAMIC SPARK PLUG FILTER AND METHOD FOR CLEANING GASEOUS EFFLUENTS OR EXHAUST GASES

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EP (1) EP3271050A1 (en)
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KR (1) KR102424112B1 (en)
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KR102424112B1 (en) 2022-07-25
US10105682B2 (en) 2018-10-23
AR103898A1 (en) 2017-06-14
KR20170128220A (en) 2017-11-22
US20180008964A1 (en) 2018-01-11
JP6571788B2 (en) 2019-09-04
EP3271050A1 (en) 2018-01-24
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