JP2005514319A5 - - Google Patents

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Publication number
JP2005514319A5
JP2005514319A5 JP2003559958A JP2003559958A JP2005514319A5 JP 2005514319 A5 JP2005514319 A5 JP 2005514319A5 JP 2003559958 A JP2003559958 A JP 2003559958A JP 2003559958 A JP2003559958 A JP 2003559958A JP 2005514319 A5 JP2005514319 A5 JP 2005514319A5
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JP
Japan
Prior art keywords
molecular sieve
metalloaluminophosphate molecular
ammonia
metalloaluminophosphate
chemisorbed
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Withdrawn
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JP2003559958A
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Japanese (ja)
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JP2005514319A (en
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Priority claimed from PCT/US2002/034114 external-priority patent/WO2003059849A1/en
Publication of JP2005514319A publication Critical patent/JP2005514319A/en
Publication of JP2005514319A5 publication Critical patent/JP2005514319A5/ja
Withdrawn legal-status Critical Current

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Claims (8)

a.メタロアルミノ燐酸塩分子篩を用いてアンモニアを化学収着する条件下で、メタロアルミノ燐酸塩分子篩をアンモニア供給源で処理する工程及び
b.メタロアルミノ燐酸塩分子篩で化学収着されたアンモニアを、少なくとも24時間保持する工程
を含む、安定化されたメタロアルミノ燐酸塩分子篩を提供する方法。
a. Treating the metalloaluminophosphate molecular sieve with an ammonia source under conditions of chemisorbing ammonia using the metalloaluminophosphate molecular sieve; and b. A method for providing a stabilized metalloaluminophosphate molecular sieve comprising the step of holding ammonia chemisorbed with a metalloaluminophosphate molecular sieve for at least 24 hours.
a.メタロアルミノ燐酸塩分子篩を用いてアンモニアを化学収着する条件下で、メタロアルミノ燐酸塩分子篩をアンモニア供給源で処理する工程、
b.メタロアルミノ燐酸塩分子篩で化学収着されたアンモニアを少なくとも24時間保持する工程及び
c.その化学収着されたアンモニアを脱着する工程
を含む、活性メタロアルミノ燐酸塩分子篩を提供する方法。
a. Treating the metalloaluminophosphate molecular sieve with an ammonia source under conditions of chemisorbing ammonia using the metalloaluminophosphate molecular sieve;
b. Holding the chemisorbed ammonia on a metalloaluminophosphate molecular sieve for at least 24 hours; and c. A method of providing an active metalloaluminophosphate molecular sieve comprising the step of desorbing the chemisorbed ammonia.
a.少なくとも一つのメタロアルミノ燐酸塩分子篩を、少なくとも一つのバインダー物質及び/又は少なくとも一つの他の触媒的に活性な物質とともに含有する混合物を生成する工程及び
b.メタロアルミノ燐酸塩分子篩を用いてアンモニアを化学収着する条件下で、その混合物をアンモニア供給源で処理する工程、
を含む、触媒組成物を生成する方法。
a. Producing a mixture containing at least one metalloaluminophosphate molecular sieve together with at least one binder material and / or at least one other catalytically active material; b. Treating the mixture with an ammonia source under conditions of chemisorbing ammonia using a metalloaluminophosphate molecular sieve;
A process for producing a catalyst composition comprising:
a.メタロアルミノ燐酸塩分子篩上に化学収着されたアンモニアを有する少なくとも一つのメタロアルミノ燐酸塩分子篩を、少なくとも一つのバインダー物質及び/又は少なくとも一つの他の触媒的に活性な物質とともに含有する混合物を生成し、触媒組成物を生成する工程を含む、触媒組成物を生成する方法。 a. Producing a mixture containing at least one metalloaluminophosphate molecular sieve having ammonia chemisorbed on the metalloaluminophosphate molecular sieve together with at least one binder material and / or at least one other catalytically active material; A method for producing a catalyst composition comprising the step of producing a catalyst composition. メタロアルミノ燐酸塩分子篩を用いるアンモニアの化学収着の前に、メタロアルミノ燐酸塩分子篩のミクロ細孔構造から、メタロアルミノ燐酸塩分子篩の合成において用いられたテンプレートを除去する、請求項1乃至4のいずれか1請求項に記載の方法。 The template used in the synthesis of the metalloaluminophosphate molecular sieve is removed from the micropore structure of the metalloaluminophosphate molecular sieve before ammonia chemisorption using the metalloaluminophosphate molecular sieve. The method of claim. メタロアルミノ燐酸塩分子篩が蒸気に暴露されている間、化学収着された状態におけるアンモニアと接触させたままメタロアルミノ燐酸塩分子篩を維持することを含む、メタロアルミノ燐酸塩分子篩を蒸気への暴露から防ぐ方法。 A method of preventing a metalloaluminophosphate molecular sieve from exposure to steam, comprising maintaining the metalloaluminophosphate molecular sieve in contact with ammonia in a chemisorbed state while the metalloaluminophosphate molecular sieve is exposed to steam. 少なくとも一つのバインダー及び/又は少なくとも一つの他の触媒的に活性な物質及び化学収着されたアンモニアとの混合物における少なくとも一つのメタロアルミノ燐酸塩分子篩を含有する分子篩組成物。 A molecular sieve composition comprising at least one metalloaluminophosphate molecular sieve in a mixture with at least one binder and / or at least one other catalytically active material and chemisorbed ammonia. (a)請求項1乃至のいずれか1請求項に記載の方法により提供された又は生成された、又は、請求項に記載の形態における分子篩の存在下で、供給原料を反応器系に導入する工程、
(b)反応器系から流出流れを取り出す工程及び
(c)前記流出流れを、少なくとも一つ以上の変換生成物を回収する回収系に通す工程
を含む、炭化水素変換方法。
(a) Feedstock is fed into the reactor system in the presence of a molecular sieve provided or produced by the process of any one of claims 1 to 5 or in the form of claim 7. Introducing process,
(b) removing the effluent stream from the reactor system;
(c) A hydrocarbon conversion method comprising the step of passing the effluent stream through a recovery system for recovering at least one or more conversion products.
JP2003559958A 2002-10-24 2002-10-24 Stabilization of acid catalyst Withdrawn JP2005514319A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US2002/034114 WO2003059849A1 (en) 2002-01-03 2002-10-24 Stabilisation of acid catalysts

Publications (2)

Publication Number Publication Date
JP2005514319A JP2005514319A (en) 2005-05-19
JP2005514319A5 true JP2005514319A5 (en) 2006-01-05

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP2003559958A Withdrawn JP2005514319A (en) 2002-10-24 2002-10-24 Stabilization of acid catalyst

Country Status (1)

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JP (1) JP2005514319A (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7998423B2 (en) 2007-02-27 2011-08-16 Basf Corporation SCR on low thermal mass filter substrates
US20090196812A1 (en) * 2008-01-31 2009-08-06 Basf Catalysts Llc Catalysts, Systems and Methods Utilizing Non-Zeolitic Metal-Containing Molecular Sieves Having the CHA Crystal Structure
US10583424B2 (en) 2008-11-06 2020-03-10 Basf Corporation Chabazite zeolite catalysts having low silica to alumina ratios
JP5428540B2 (en) * 2009-06-02 2014-02-26 東ソー株式会社 SAPO-34 having high water resistance and large particles, synthesis method thereof and use thereof
CN104582841A (en) * 2012-06-29 2015-04-29 巴斯夫欧洲公司 Catalyst coating and method for the conversion of oxygenates to olefins
US9802182B2 (en) * 2013-03-13 2017-10-31 Basf Corporation Stabilized metal-exchanged SAPO material

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