JP2013533804A5 - - Google Patents

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JP2013533804A5
JP2013533804A5 JP2013519191A JP2013519191A JP2013533804A5 JP 2013533804 A5 JP2013533804 A5 JP 2013533804A5 JP 2013519191 A JP2013519191 A JP 2013519191A JP 2013519191 A JP2013519191 A JP 2013519191A JP 2013533804 A5 JP2013533804 A5 JP 2013533804A5
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copper
zeolitic material
containing zsm
eri
eri zeolitic
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Priority claimed from PCT/IB2011/052980 external-priority patent/WO2012007874A1/en
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シリカ:アルミナモル比が約4〜約50であり、CuOとしての銅含量が焼成ゼオライト系材料の全質量に対して約1〜約10質量%であり、金属酸化物としてのアルカリ金属含量が約0.7〜約1.5質量%の範囲である銅含有ZSM−34、OFF及び/又はERIゼオライト系材料であって、その750℃で養生後の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料の、時間当たりのガスの体積流量(空間速度)が30000h−1で、定常状態条件で最大のNHスリップ条件で、500ppmのNOと500ppmのNH、10%のO、5%のHO、残りがNの混合ガス中でのNO変換率が、200℃で少なくとも約75%、450℃で少なくとも約90%である銅含有ZSM−34、OFF及び/又はERIゼオライト系材料。 The silica: alumina molar ratio is about 4 to about 50, the copper content as CuO is about 1 to about 10% by weight, based on the total weight of the calcined zeolitic material, and the alkali metal content as metal oxide is about 0. Copper-containing ZSM-34, OFF and / or ERI zeolitic material in the range of 7 to about 1.5% by weight, the copper-containing ZSM-34, OFF and / or ERI zeolite after curing at 750 ° C. The volume flow rate (space velocity) of gas per hour of the system material is 30000 h −1 , 500 ppm NO and 500 ppm NH 3 , 10% O 2 , 5% under the maximum NH 3 slip condition in the steady state condition. of H 2 O, remainder NO conversion in a mixed gas of N 2 is at least about 75% at 200 ° C., the copper-containing ZSM-34, OFF and at least about 90% at 450 ° C. / ERI zeolite-based materials. 金属酸化物としてのアルカリ金属含量が0.9〜5質量%の範囲である請求項1に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料。   The copper-containing ZSM-34, OFF and / or ERI zeolitic material according to claim 1, wherein the alkali metal content as the metal oxide is in the range of 0.9 to 5% by mass. フレッシュなまたは750℃で養生後のゼオライト系材料では、CuOとしての銅含量が、焼成ゼオライト系材料の全質量に対して2〜5質量%の範囲であり、800℃養生後のゼオライト系材料では、焼成ゼオライト系材料の全質量に対して2〜4.2質量%である請求項1または2に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料。   In a zeolitic material that is fresh or cured at 750 ° C., the copper content as CuO is in the range of 2 to 5% by mass with respect to the total mass of the calcined zeolitic material, and in the zeolitic material after curing at 800 ° C. The copper-containing ZSM-34, OFF and / or ERI zeolitic material according to claim 1 or 2, which is 2 to 4.2% by mass relative to the total mass of the calcined zeolitic material. シリカ:アルミナモル比が8〜15である請求項1〜3のいずれか一項に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料。   The copper-containing ZSM-34, OFF and / or ERI zeolitic material according to any one of claims 1 to 3, wherein the silica: alumina molar ratio is 8-15. 上記銅含有ZSM−34、OFF及び/又はERIゼオライト系材料のシリカ:アルミナモル比が10〜15であって、かつ
上記銅含有ZSM−34、OFF及び/又はERIゼオライト系材料がフレッシュであるか750℃で10%スチーム中で24時間養生後である場合には、銅:アルミニウム原子比が0.04〜0.5の範囲であり、
上記銅含有ZSM−34、OFF及び/又はERIゼオライト系材料が800℃で10%スチーム中で12時間養生後である場合には、該銅:アルミニウム原子比が0.04〜0.3の範囲であり、
上記銅含有ZSM−34、OFF及び/又はERIゼオライト系材料のシリカ:アルミナモル比が4〜10であって、かつ
上記銅含有ZSM−34、OFF及び/又はERIゼオライト系材料がフレッシュであるか750℃で10%スチーム中で24時間養生後である場合には、銅:アルミニウム原子比が0.02〜0.5の範囲であり、
上記銅含有ZSM−34、OFF及び/又はERIゼオライト系材料が800℃で10%スチーム中で12時間養生後である場合には、該銅:アルミニウム原子比が0.02〜0.21の範囲である
請求項1〜4のいずれか一項に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料。
Whether the copper-containing ZSM-34, OFF and / or ERI zeolitic material has a silica: alumina molar ratio of 10-15, and is the copper-containing ZSM-34, OFF and / or ERI zeolitic material fresh 750 When after curing for 24 hours in 10% steam at ° C., the copper: aluminum atomic ratio is in the range of 0.04 to 0.5,
When the copper-containing ZSM-34, OFF and / or ERI zeolitic material is after curing for 12 hours in 800% 10% steam, the copper: aluminum atomic ratio is in the range of 0.04 to 0.3. And
Whether the copper-containing ZSM-34, OFF and / or ERI zeolitic material has a silica: alumina molar ratio of 4 to 10 and the copper-containing ZSM-34, OFF and / or ERI zeolitic material is fresh 750 When after curing for 24 hours in 10% steam at ° C., the copper: aluminum atomic ratio is in the range of 0.02-0.5,
When the copper-containing ZSM-34, OFF and / or ERI zeolitic material is after 12 hours of curing in 800% 10% steam, the copper: aluminum atomic ratio is in the range of 0.02-0.21. The copper-containing ZSM-34, OFF and / or ERI zeolitic material according to any one of claims 1 to 4.
上記銅含有ZSM−34、OFF及び/又はERIゼオライト系材料のシリカ:アルミナモル比が10〜15であって、かつ
上記銅含有ZSM−34、OFF及び/又はERIゼオライト系材料がフレッシュであるか750℃で10%スチーム中で24時間養生後である場合には、Cuの2倍とアルカリ金属の合計:アルミニウムの原子比(2Cu+M)/Alが0.14〜1の範囲であり;
含有ZSM−34、OFF及び/又はERIゼオライト系材料が800℃で10%スチーム中で12時間養生した後である場合には、Cuの2倍とアルカリ金属の合計:アルミニウムの原子比(2Cu+M)/Alが0.14〜0.86の範囲であり;
該銅含有ZSM−34、OFF及び/又はERIゼオライト系材料のシリカ:アルミナモル比4〜10であって、かつ
該銅含有ZSM−34、OFF及び/又はERIゼオライト系材料がフレッシュであるか750℃で10%スチーム中で24時間養生した後である場合には、Cuの2倍とアルカリ金属の合計:アルミニウムの原子比(2Cu+M)/Alが0.07〜1の範囲であり、
該銅含有ZSM−34、OFF及び/又はERIゼオライト系材料が800℃で10%スチーム中で12時間養生した後であるなら、Cuの2倍とアルカリ金属の合計:アルミニウムの原子比(2Cu+M)/Alが0.07〜0.6の範囲である
請求項1〜5のいずれか一項に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料。
Whether the copper-containing ZSM-34, OFF and / or ERI zeolitic material has a silica: alumina molar ratio of 10-15, and is the copper-containing ZSM-34, OFF and / or ERI zeolitic material fresh 750 When cured in 10% steam at 10 ° C. for 24 hours, the sum of Cu and alkali metal: aluminum atomic ratio (2Cu + M) / Al is in the range of 0.14 to 1;
When the containing ZSM-34, OFF and / or ERI zeolitic material is after curing in 800% 10% steam for 12 hours, the total Cu plus 2 times alkali metal: aluminum atomic ratio (2Cu + M) / Al is in the range of 0.14-0.86;
The silica-to-alumina molar ratio of the copper-containing ZSM-34, OFF and / or ERI zeolitic material is 4-10, and the copper-containing ZSM-34, OFF and / or ERI zeolitic material is 750 ° C. And after curing for 24 hours in 10% steam, the total of the Cu and twice the alkali metal: aluminum atomic ratio (2Cu + M) / Al is in the range of 0.07 to 1,
If the copper-containing ZSM-34, OFF and / or ERI zeolitic material is cured for 12 hours in 10% steam at 800 ° C., then 2 times Cu plus the total alkali metal: aluminum atomic ratio (2Cu + M) / Al is in the range of 0.07 to 0.6. The copper-containing ZSM-34, OFF and / or ERI zeolitic material according to any one of claims 1 to 5.
上記銅含有ZSM−34、OFF及び/又はERIゼオライト系材料のシリカ:アルミナモル比が10〜15であって、かつ
該銅含有ZSM−34、OFF及び/又はERIゼオライト系材料がフレッシュであるか750℃で10%スチーム中で24時間養生した後である場合には、銅:プロトン原子比が0.05〜600の範囲であり、
該銅含有ZSM−34、OFF及び/又はERIゼオライト系材料が800℃で10%スチーム中で12時間養生した後である場合には、銅:プロトン原子比が0.05〜300の範囲であり、
該銅含有ZSM−34、OFF及び/又はERIゼオライト系材料のシリカ:アルミナモル比4〜10であり、
該銅含有ZSM−34、OFF及び/又はERIゼオライト系材料がフレッシュであるか750℃で10%スチーム中で24時間養生した後である場合には、銅:プロトン原子比が0.02〜100の範囲であり、
該銅含有ZSM−34、OFF及び/又はERIゼオライト系材料が800℃で10%スチーム中で12時間養生した後である場合には、銅:プロトン原子比が好ましくは0.02〜20の範囲である
請求項1〜6のいずれか一項に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料。
Whether the copper-containing ZSM-34, OFF and / or ERI zeolitic material has a silica: alumina molar ratio of 10-15, and is the copper-containing ZSM-34, OFF and / or ERI zeolitic material 750 fresh? When after curing for 24 hours in 10% steam at ° C., the copper: proton atomic ratio is in the range of 0.05-600,
When the copper-containing ZSM-34, OFF and / or ERI zeolitic material is after curing in 800% 10% steam for 12 hours, the copper: proton atomic ratio is in the range of 0.05-300. ,
The silica-to-alumina molar ratio of the copper-containing ZSM-34, OFF and / or ERI zeolitic material is 4-10,
When the copper-containing ZSM-34, OFF and / or ERI zeolitic material is fresh or after curing in 10% steam at 750 ° C. for 24 hours, the copper: proton atomic ratio is 0.02-100. Range of
When the copper-containing ZSM-34, OFF and / or ERI zeolitic material is after curing in 800% 10% steam for 12 hours, the copper: proton atomic ratio is preferably in the range of 0.02-20. The copper-containing ZSM-34, OFF and / or ERI zeolitic material according to any one of claims 1-6.
−時間当たりのガスの体積流量(空間速度)が80000h−1で測定した場合、すな わち上記フレッシュな銅含有ZSM−34、OFF及び/又はERIゼオライト系材料 の200℃でのNO変換率が少なくとも60%で、450℃で少なくとも75%であり、
上記750℃で養生後の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料のNO変換率が200℃で少なくとも55%、450℃で少なくとも70%であり、
上記800℃で養生後の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料のNO変換率が200℃で少なくとも45%、450℃で少なくとも65%である
請求項1〜7のいずれか一項に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料。
-When the volumetric flow rate (space velocity) of gas per hour is measured at 80000h- 1, that is, the NO conversion rate at 200 ° C of the fresh copper-containing ZSM-34, OFF and / or ERI zeolitic materials. Is at least 60% and at least 75% at 450 ° C;
The NO conversion of the copper-containing ZSM-34, OFF and / or ERI zeolitic material after curing at 750 ° C. is at least 55% at 200 ° C. and at least 70% at 450 ° C.,
The NO conversion of the copper-containing ZSM-34, OFF and / or ERI zeolitic material after curing at 800 ° C is at least 45% at 200 ° C and at least 65% at 450 ° C. The copper-containing ZSM-34, OFF and / or ERI zeolitic material according to Item.
上記銅含有ZSM−34、OFF及び/又はERIゼオライト系材料のDIN−ISO−9277により求めたラングミュア表面積が400〜900m/gの範囲であり、該銅含有ZSM−34、OFF及び/又はERIゼオライト系材料の表面積が、最大10体積%のスチームの存在下で750℃の温度に1〜48時間暴露後にそのフレッシュ状態での表面積の少なくとも60%が維持される請求項1〜8のいずれか一項に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料。 The copper-containing ZSM-34, OFF and / or ERI zeolitic material has a Langmuir surface area determined by DIN-ISO-9277 in the range of 400 to 900 m 2 / g, the copper-containing ZSM-34, OFF and / or ERI 9. The surface area of the zeolitic material is maintained at least 60% of its fresh surface area after exposure for 1 to 48 hours at a temperature of 750 [deg.] C. in the presence of up to 10% by volume of steam. The copper-containing ZSM-34, OFF and / or ERI zeolitic material according to one item. ZSM−34が用いられる請求項1〜9のいずれか一項に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料。   The copper-containing ZSM-34, OFF and / or ERI zeolitic material according to any one of claims 1 to 9, wherein ZSM-34 is used. 支持体上に担持された請求項1〜10のいずれか一項に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料を含む触媒。   A catalyst comprising a copper-containing ZSM-34, OFF and / or ERI zeolitic material according to any one of claims 1 to 10 supported on a support. 請求項1〜10のいずれか一項に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料を含む触媒または請求項11の触媒を、酸化窒素NOxの選択的還元(SCR)、NHの酸化、NOの分解、すすの酸化、もしくは先進排出システムの排出制御に、又は流動接触分解(FCC)プロセスの添加物として、有機変換反応の触媒として、もしくは固定排出源プロセスの触媒としての使用法。 A catalyst comprising the copper-containing ZSM-34, OFF and / or ERI zeolitic material according to any one of claims 1 to 10 or the catalyst of claim 11 is converted to NOx selective reduction (SCR), NH 3 oxidation, N 2 O decomposition, soot oxidation, or emission control in advanced emission systems, or as an additive in fluid catalytic cracking (FCC) processes, as catalysts for organic conversion reactions, or as catalysts for fixed emission processes Usage as. アンモニア含有排ガス流と、請求項1〜10のいずれか一項に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料を含む触媒または請求項11の触媒、すすフィルターとディーゼル酸化触媒とからなる排ガス処理システム。 An ammonia-containing exhaust gas stream and a catalyst comprising the copper-containing ZSM-34, OFF and / or ERI zeolitic material according to any one of claims 1 to 10 , or the catalyst of claim 11, a soot filter and a diesel oxidation catalyst. An exhaust gas treatment system consisting of 酸化窒素NOxを含むガス流を請求項1〜10のいずれか一項に記載の銅含有ZSM−34、OFF及び/又はERIゼオライト系材料または請求項11の触媒と接触させる酸化窒素NOxの選択的還元方法。 Selective of nitrogen oxide NOx, wherein a gas stream comprising nitric oxide NOx is contacted with the copper-containing ZSM-34, OFF and / or ERI zeolitic material according to any one of claims 1-10 or the catalyst of claim 11. Reduction method.
JP2013519191A 2010-07-15 2011-07-05 Copper-containing ZSM-34, OFF and / or ERI zeolitic materials for selective reduction of NOx Withdrawn JP2013533804A (en)

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EP10169676 2010-07-15
EP10169676.3 2010-07-15
PCT/IB2011/052980 WO2012007874A1 (en) 2010-07-15 2011-07-05 Copper containing zsm-34, off and/or eri zeolitic material for selective reduction of nox

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US9527751B2 (en) 2011-11-11 2016-12-27 Basf Se Organotemplate-free synthetic process for the production of a zeolitic material of the CHA-type structure
JP6416096B2 (en) * 2012-09-28 2018-10-31 パシフィック インダストリアル デベロップメント コーポレイション Method for preparing STT-type zeolite for use as a catalyst in selective catalytic reduction reaction
CN106232209B (en) * 2014-03-24 2022-09-02 庄信万丰股份有限公司 System and method for treating exhaust gas
US9925492B2 (en) 2014-03-24 2018-03-27 Mellanox Technologies, Ltd. Remote transactional memory
GB2547145B (en) * 2015-03-25 2018-09-05 Johnson Matthey Plc Noble metal-off framework type passive NOx adsorber and use thereof
US11014077B2 (en) * 2016-05-03 2021-05-25 Umicore Ag & Co. Kg Active SCR catalyst
JP2020522383A (en) * 2017-06-09 2020-07-30 ビーエーエスエフ コーポレーション Catalytic washcoat with controlled porosity for NOX reduction
WO2020088531A1 (en) * 2018-10-30 2020-05-07 Basf Corporation In-situ copper ion-exchange on pre-exchanged copper zeolitic material
CN115138391A (en) * 2021-03-29 2022-10-04 高化学株式会社 Low temperature carbonylation molecular sieve catalyst and use thereof
CN113198525B (en) * 2021-05-08 2023-05-09 北京工业大学 Catalyst for synergistic purification of laughing gas decomposition and NOx catalytic reduction under low-temperature condition and preparation method thereof

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* Cited by examiner, † Cited by third party
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JP2671551B2 (en) * 1990-03-16 1997-10-29 トヨタ自動車株式会社 Method for producing exhaust purification catalyst
JP3276678B2 (en) * 1992-07-02 2002-04-22 出光興産株式会社 Exhaust gas purification catalyst and exhaust gas purification method using the same
US5254322A (en) * 1992-08-10 1993-10-19 Mobil Oil Corporation Method for reducing automotive NOx emissions in lean burn internal combustion engine exhaust using a transition metal-containing zeolite catalyst which is in-situ crystallized
CN100515561C (en) * 2003-12-16 2009-07-22 广东工业大学 Highly effective catalyst for purifying automobile exhaust and its preparing process
EP1973633A2 (en) * 2005-12-14 2008-10-01 BASF Catalysts LLC Zeolite catalyst with improved nox reduction in scr
EP2517773B2 (en) * 2007-04-26 2019-08-07 Johnson Matthey Public Limited Company Copper/LEV-zeolite SCR catalyst

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