JP2014511259A5 - - Google Patents

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Publication number
JP2014511259A5
JP2014511259A5 JP2013549930A JP2013549930A JP2014511259A5 JP 2014511259 A5 JP2014511259 A5 JP 2014511259A5 JP 2013549930 A JP2013549930 A JP 2013549930A JP 2013549930 A JP2013549930 A JP 2013549930A JP 2014511259 A5 JP2014511259 A5 JP 2014511259A5
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Japan
Prior art keywords
mass
catalyst
production method
particles
manufacturing
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JP2013549930A
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JP2014511259A (en
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Priority claimed from PCT/IB2012/050303 external-priority patent/WO2012101567A2/en
Publication of JP2014511259A publication Critical patent/JP2014511259A/en
Publication of JP2014511259A5 publication Critical patent/JP2014511259A5/ja
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Claims (14)

二酸化ジルコニウム及び任意に酸化ケイ素を含む触媒担体粒子の製造方法であって、
(i)二酸化ジルコニウムの前駆体化合物及び任意に酸化ケイ素の前駆体化合物を含有する溶液を調製する工程、
(ii)溶液をエアロゾルに変換する工程、
(iii)エアロゾルを、直接的又は間接的に加熱された熱分解領域に供給する工程、
(iv)熱分解を実行する工程、及び
(v)熱分解ガスから生成される触媒担体粒子を分離する工程、
を含むことを特徴とする製造方法。
A process for producing catalyst support particles comprising zirconium dioxide and optionally silicon oxide,
(I) preparing a solution containing a zirconium dioxide precursor compound and optionally a silicon oxide precursor compound;
(Ii) converting the solution into an aerosol;
(Iii) supplying the aerosol to a directly or indirectly heated pyrolysis zone;
(Iv) a step of performing pyrolysis, and (v) a step of separating the catalyst carrier particles generated from the pyrolysis gas,
The manufacturing method characterized by including.
熱分解領域が火炎により加熱される請求項1に記載の製造方法。   The manufacturing method according to claim 1, wherein the pyrolysis region is heated by a flame. 二酸化ジルコニウムの前駆体化合物が、2−エチルヘキサン酸ジルコニウム(IV)を含む請求項1又は2に記載の製造方法。   The production method according to claim 1 or 2, wherein the precursor compound of zirconium dioxide contains zirconium (IV) 2-ethylhexanoate. 二酸化ケイ素の前駆体化合物が、ヘキサメチルジシロキサンを含む請求項1〜3の何れか1項に記載の製造方法。   The manufacturing method of any one of Claims 1-3 in which the precursor compound of silicon dioxide contains hexamethyldisiloxane. 二酸化ジルコニウムの前駆体化合物が、ジルコニウム(IV)プロポキシレートを含む請求項1〜4の何れか1項に記載の製造方法。   The production method according to any one of claims 1 to 4, wherein the precursor compound of zirconium dioxide contains zirconium (IV) propoxylate. 一以上の前駆体化合物を、酢酸、エタノール、及び水の混合物に溶解させる請求項1〜5の何れか1項に記載の製造方法。   The production method according to any one of claims 1 to 5, wherein one or more precursor compounds are dissolved in a mixture of acetic acid, ethanol, and water. 一以上の前駆体化合物を、キシレンに溶解させる請求項1〜6の何れか1項に記載の製造方法。   The production method according to claim 1, wherein one or more precursor compounds are dissolved in xylene. 熱分解を、900〜1500℃で実行する請求項1〜7の何れか1項に記載の製造方法。   The manufacturing method of any one of Claims 1-7 which performs a thermal decomposition at 900-1500 degreeC. 請求項1〜8の何れか1項に記載の製造方法により得られる触媒担体粒子。   Catalyst carrier particles obtained by the production method according to any one of claims 1 to 8. 白金及びスズ、並びにランタン及びセシウムから選択される一種以上の他の元素の化合物を二酸化ジルコニウム含有の担体上に含む触媒粒子の製造方法であって、
請求項1〜8の何れか1項に記載の工程(i)〜(v)を有し、
さらに、
(vi)白金及びスズ、並びにランタン及びセシウムから選択される一種以上の他の元素の化合物を含有する一種以上の溶媒で、生成された触媒担体粒子を含浸する工程と、
(vii)含浸された触媒担体粒子を乾燥及び焼成する工程と、
を有することを特徴とする製造方法。
A method for producing catalyst particles comprising a compound of one or more other elements selected from platinum and tin, and lanthanum and cesium on a zirconium dioxide-containing support,
It has process (i)-(v) of any one of Claims 1-8,
further,
(Vi) impregnating the produced catalyst support particles with one or more solvents containing a compound of one or more other elements selected from platinum and tin, and lanthanum and cesium;
(Vii) drying and calcining the impregnated catalyst support particles;
The manufacturing method characterized by having.
請求項10に記載の製造方法により得られる触媒粒子。   Catalyst particles obtained by the production method according to claim 10. 0.05〜1質量%のPt、及び0.05〜2質量%のSnを含有する請求項11に記載の触媒粒子。   The catalyst particles according to claim 11, containing 0.05 to 1% by mass of Pt and 0.05 to 2% by mass of Sn. 比表面積が20〜70m/gである請求項11又は12に記載の触媒粒子。 The catalyst particles according to claim 11 or 12 having a specific surface area of 20~70m 2 / g. 30〜99.5質量%のZrO及び0.5〜25質量%のSiOを担体として含み、並びに担体の質量に対して0.1〜1質量%のPt、0.1〜10質量%のSn、La、及び/又はCsを含み、
少なくともSn、及び少なくともLa又はCsを含有する請求項11〜13の何れか1項に記載の触媒粒子。
30 to 99.5% by mass of ZrO 2 and 0.5 to 25% by mass of SiO 2 as a carrier, and 0.1 to 1% by mass of Pt, 0.1 to 10% by mass with respect to the mass of the carrier Sn, La, and / or Cs
The catalyst particle according to any one of claims 11 to 13, containing at least Sn and at least La or Cs.
JP2013549930A 2011-01-25 2012-01-23 Catalyst support from spray flame pyrolysis and autothermal propane dehydrogenation catalyst Withdrawn JP2014511259A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP11151958 2011-01-25
EP11151958.3 2011-01-25
PCT/IB2012/050303 WO2012101567A2 (en) 2011-01-25 2012-01-23 Catalyst support produced by flame spray pyrolysis and catalyst for autothermal propane dehydrogenation

Publications (2)

Publication Number Publication Date
JP2014511259A JP2014511259A (en) 2014-05-15
JP2014511259A5 true JP2014511259A5 (en) 2015-03-12

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JP2013549930A Withdrawn JP2014511259A (en) 2011-01-25 2012-01-23 Catalyst support from spray flame pyrolysis and autothermal propane dehydrogenation catalyst

Country Status (6)

Country Link
EP (1) EP2667968A2 (en)
JP (1) JP2014511259A (en)
KR (1) KR20140006909A (en)
CN (1) CN103379957A (en)
BR (1) BR112013019047A2 (en)
WO (1) WO2012101567A2 (en)

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US8933262B2 (en) 2011-05-24 2015-01-13 Basf Se Process for preparing polyisocyanates from biomass
CN103566933B (en) * 2012-08-08 2016-09-07 中国石油化工股份有限公司 A kind of acetate preparation of ethanol by hydrogenating catalyst and preparation method thereof
CN104248953A (en) * 2013-06-28 2014-12-31 中国石油化工股份有限公司 Catalyst for preparation of ethanol by acetate hydrogenation and preparation method thereof
KR101814451B1 (en) 2015-11-10 2018-01-04 희성촉매 주식회사 A stabilized active metal complex based catalyst for dehydrogenation of straight-chain hydrocarbons
KR101716170B1 (en) 2015-11-10 2017-03-14 희성촉매 주식회사 A stabilized active metal complex based catalyst for dehydrogenation of light straight-chain hydrocarbons
CN106753391A (en) * 2016-11-28 2017-05-31 新沂市中诺新材料科技有限公司 A kind of nano material and preparation method for being passivated heavy metal in rehabilitating soil
CN111821996B (en) * 2019-04-18 2022-11-29 清华大学 Efficient hydrothermal-resistant and sulfur-resistant demercuration catalyst and preparation method and application thereof
CN115069246B (en) * 2021-03-15 2023-08-15 中国石油化工股份有限公司 Supported silver catalyst and preparation method and application thereof

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US3701805A (en) * 1971-09-27 1972-10-31 Pfizer Preparation of citraconic and itaconic acids
US6057030A (en) * 1997-07-21 2000-05-02 Kanebo Ltd. Porous ceramic body and kiln furniture made from a porous ceramic body
DE19937107A1 (en) * 1999-08-06 2001-02-08 Basf Ag Catalyst with bimodal pore radius distribution
CN1513600A (en) * 2003-08-19 2004-07-21 丁章云 Catalyst active carrier and preparation thereof
CN101204654A (en) * 2006-12-20 2008-06-25 中国科学院生态环境研究中心 Supported noble metal catalyst for low-temperature catalytic oxidation benzene series and preparation method thereof
CN101433863B (en) * 2007-11-15 2012-08-29 中国石油化工股份有限公司 Composite oxide carrier and preparation method thereof

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