JP2001213665A5 - - Google Patents

Download PDF

Info

Publication number
JP2001213665A5
JP2001213665A5 JP2000269194A JP2000269194A JP2001213665A5 JP 2001213665 A5 JP2001213665 A5 JP 2001213665A5 JP 2000269194 A JP2000269194 A JP 2000269194A JP 2000269194 A JP2000269194 A JP 2000269194A JP 2001213665 A5 JP2001213665 A5 JP 2001213665A5
Authority
JP
Japan
Prior art keywords
titanium
silicon
aluminum
oxide
producing
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.)
Granted
Application number
JP2000269194A
Other languages
Japanese (ja)
Other versions
JP2001213665A (en
JP4588183B2 (en
Filing date
Publication date
Application filed filed Critical
Priority to JP2000269194A priority Critical patent/JP4588183B2/en
Priority claimed from JP2000269194A external-priority patent/JP4588183B2/en
Publication of JP2001213665A publication Critical patent/JP2001213665A/en
Publication of JP2001213665A5 publication Critical patent/JP2001213665A5/ja
Application granted granted Critical
Publication of JP4588183B2 publication Critical patent/JP4588183B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【特許請求の範囲】
【請求項1】 アルミニウム、ケイ素およびチタンを含み、その合計量が酸化物(Al+SiO+TiO)換算で少なくとも99重量%であり、かつpKa+4.8指示薬のメチルレッドにより酸性色を呈するセラミックス体。
【請求項2】 アルミニウム化合物、ケイ素化合物およびチタン化合物を含む混合物を1,000〜2,000℃の温度で焼成することよりなるアルミニウム、ケイ素およびチタンを含み、その合計量が酸化物(Al +SiO +TiO )換算で少なくとも99重量%であり、かつpKa+4.8指示薬のメチルレッドにより酸性色を呈するセラミックス体の製造方法。
【請求項3】 アルミニウム、ケイ素およびチタンを含み、その合計量が酸化物(Al +SiO +TiO )換算で少なくとも99重量%であり、かつpKa+4.8指示薬のメチルレッドにより酸性色を呈するセラミックス体の成形物よりなる触媒用担体。
【請求項4】 アルミニウム化合物、ケイ素化合物およびチタン化合物を含む混合物を成形し、ついで該成形物を1,000〜2,000℃の温度で焼成することよりなるアルミニウム、ケイ素およびチタンを含み、その合計量が酸化物(Al +SiO +TiO )換算で少なくとも99重量%であり、かつpKa+4.8指示薬のメチルレッドにより酸性色を呈する触媒用担体の製造方法。
【請求項5】 請求項3に記載の担体に、銀成分と、アルカリ金属およびアルカリ土類金属よりなる群から選ばれた少なくとも1種の元素とを担持してなる酸化エチレン製造用触媒。
【請求項6】 請求項3に記載の担体に、銀成分および反応促進剤成分を担持したのち、酸化性雰囲気中で150〜450℃で0.1〜10時間焼成し、ついで不活性ガス雰囲気中で450〜800℃で0.1〜10時間焼成してなる酸化エチレン製造用触媒の製造方法。
【請求項7】 請求項5に記載の触媒の存在下にエチレンを分子状酸素含有ガスにより気相酸化することよりなる酸化エチレンの製造方法
[Claims]
    1. The method according to claim 1, comprising aluminum, silicon and titanium, the total amount of which is oxide (Al2O3+ SiO2+ TiO2A) a ceramic body which is at least 99% by weight in conversion and exhibits an acidic color due to pKa + 4.8 indicator methyl red;
    (2) A mixture containing an aluminum compound, a silicon compound and a titanium compound is calcined at a temperature of 1,000 to 2,000 ° C. to contain aluminum, silicon and titanium, and the total amount of the oxide (Al 2 O 3 + SiO 2 + TiO 2 )) A method for producing a ceramic body which is at least 99% by weight in conversion and exhibits an acidic color with pKa + 4.8 indicator methyl red.
    (3) Aluminum, silicon and titanium, the total amount of which is oxide (Al 2 O 3 + SiO 2 + TiO 2 A) a catalyst carrier comprising at least 99% by weight in terms of conversion and having a pKa + 4.8 indicator methyl red and exhibiting an acidic color with a ceramic body;
    (4) Forming a mixture containing an aluminum compound, a silicon compound and a titanium compound, and then baking the formed product at a temperature of 1,000 to 2,000 ° C., containing aluminum, silicon and titanium, the total amount of which is oxide (Al 2 O 3 + SiO 2 + TiO 2 A) a method for producing a catalyst carrier which is at least 99% by weight in conversion and exhibits an acidic color with pKa + 4.8 indicator methyl red;
    (5) A catalyst for producing ethylene oxide, wherein the carrier according to claim 3 supports a silver component and at least one element selected from the group consisting of alkali metals and alkaline earth metals.
    6. 4. The support according to claim 3, wherein the silver component and the reaction accelerator component are supported, and then calcined in an oxidizing atmosphere at 150 to 450 ° C. for 0.1 to 10 hours, and then in an inert gas atmosphere at 450 to 800. A method for producing a catalyst for producing ethylene oxide, which is calcined at 0.1 ° C for 0.1 to 10 hours.
    7. A process for producing ethylene oxide, comprising subjecting ethylene to gas-phase oxidation with a molecular oxygen-containing gas in the presence of the catalyst according to claim 5..

JP2000269194A 1999-09-06 2000-09-05 Ceramic body, catalyst carrier, production method thereof, ethylene oxide production catalyst using the carrier, production method thereof, and ethylene oxide production method Expired - Fee Related JP4588183B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000269194A JP4588183B2 (en) 1999-09-06 2000-09-05 Ceramic body, catalyst carrier, production method thereof, ethylene oxide production catalyst using the carrier, production method thereof, and ethylene oxide production method

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
JP25188399 1999-09-06
JP11-251883 1999-11-24
JP11-332588 1999-11-24
JP33258899 1999-11-24
JP2000269194A JP4588183B2 (en) 1999-09-06 2000-09-05 Ceramic body, catalyst carrier, production method thereof, ethylene oxide production catalyst using the carrier, production method thereof, and ethylene oxide production method

Publications (3)

Publication Number Publication Date
JP2001213665A JP2001213665A (en) 2001-08-07
JP2001213665A5 true JP2001213665A5 (en) 2007-05-17
JP4588183B2 JP4588183B2 (en) 2010-11-24

Family

ID=27334071

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000269194A Expired - Fee Related JP4588183B2 (en) 1999-09-06 2000-09-05 Ceramic body, catalyst carrier, production method thereof, ethylene oxide production catalyst using the carrier, production method thereof, and ethylene oxide production method

Country Status (1)

Country Link
JP (1) JP4588183B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4539289B2 (en) * 2004-10-29 2010-09-08 住友化学株式会社 Method for producing aluminum oxide-titanium oxide mixed molded body
KR100631931B1 (en) 2004-12-22 2006-10-04 윤현진 Photocatalyst can confirm whether it is spread or not
KR101072239B1 (en) 2005-06-07 2011-10-12 생-고뱅 세라믹스 앤드 플라스틱스, 인코포레이티드 A catalyst carrier
JP5258485B2 (en) * 2008-09-30 2013-08-07 株式会社日本触媒 Catalyst for producing ethylene oxide and method for producing ethylene oxide using the catalyst
KR102551215B1 (en) * 2016-01-27 2023-07-03 삼성전기주식회사 Ceramic Composition, Electrostatic Chuck, and Manufacturing Method of Electrostatic Chuck
JP2022070506A (en) * 2020-10-27 2022-05-13 住友化学株式会社 Particle composition and formed body

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4483944A (en) * 1983-07-27 1984-11-20 Corning Glass Works Aluminum titanate-mullite ceramic articles
JPH075361B2 (en) * 1990-04-21 1995-01-25 日本碍子株式会社 Aluminum titanate-mullite ceramic body
EP0463437B2 (en) * 1990-06-22 1998-12-02 Bayer Ag Sintered bodies based on aluminium titanate, process for their production and use thereof
JP3313164B2 (en) * 1992-02-27 2002-08-12 株式会社日本触媒 Silver catalyst for producing ethylene oxide and method for producing the same
JPH0987009A (en) * 1995-09-29 1997-03-31 Kyocera Corp Alumina-mullite combined sintered compact and its production
US5733840A (en) * 1996-06-06 1998-03-31 Norton Chemical Process Products Corporation Catalyst carrier
JP3664201B2 (en) * 1996-12-19 2005-06-22 トヨタ自動車株式会社 Exhaust gas purification catalyst
JP4001429B2 (en) * 1998-02-20 2007-10-31 株式会社日本触媒 Silver catalyst for producing ethylene oxide, method for producing the same, and method for producing ethylene oxide

Similar Documents

Publication Publication Date Title
US5932750A (en) Catalysts for partial oxidation of hydrocarbons and method of partial oxidation of hydrocarbons
RU2007148500A (en) METHOD FOR SELECTIVE OXIDATION OF ETHANE TO ETHYLENE
JP2003525920A5 (en)
JP2003524579A5 (en)
WO2000043341A3 (en) Method for producing acrolein by heterogeneous catalytic gas-phase partial oxidation of propene
JP2001213665A5 (en)
JP2004531386A5 (en) Ethylene purification method
RU2009108303A (en) APPLICATION OF THE CATALYST ON THE BASIS OF ZEOLITES FOR THE TRANSFORMATION OF OXYGEN CONTAINING COMPOUNDS TO LOW OLEFINS, AND ALSO THE METHOD FOR PRODUCING LOW OLEFINS
CA2534872A1 (en) Catalyst composition and use thereof in ethane oxidation
TW200927728A (en) Process for preparation of N-methyl pyrrolidone
JP2009090283A (en) Catalyst
JPS5817174B2 (en) Manufacturing method of phenol
JP4395580B2 (en) Production method of epoxide
JP2006219375A (en) Method for producing propylene
JP4588183B2 (en) Ceramic body, catalyst carrier, production method thereof, ethylene oxide production catalyst using the carrier, production method thereof, and ethylene oxide production method
JPS605339B2 (en) Method for producing a catalyst for oxidizing O-xylene to phthalic anhydride
JP2004181435A5 (en)
CN105524037B (en) A kind of method of oxidizing cyclohexanone
JP2001259420A (en) Method for producing high activity selective catalyst for preparation of unsaturated nitriles
JP4048746B2 (en) Catalyst for selectively oxidizing hydrogen, and hydrocarbon dehydrogenation method using the same
JP3757624B2 (en) Hydrogen selective oxidation catalyst, hydrogen selective oxidation method, and hydrocarbon dehydrogenation method
JP3969030B2 (en) Catalyst for selectively oxidizing hydrogen and hydrocarbon dehydrogenation method using the same
JP3801352B2 (en) Method for producing oxidation catalyst, oxidation catalyst, and hydrocarbon dehydrogenation method
JPH0551342B2 (en)
JP2003267924A (en) Method of producing methacrylic acid and method of producing methacrylic acid ester