CN102143932A - 使用负载金属催化剂由乙酸直接选择性制备乙醛 - Google Patents
使用负载金属催化剂由乙酸直接选择性制备乙醛 Download PDFInfo
- Publication number
- CN102143932A CN102143932A CN2009801340830A CN200980134083A CN102143932A CN 102143932 A CN102143932 A CN 102143932A CN 2009801340830 A CN2009801340830 A CN 2009801340830A CN 200980134083 A CN200980134083 A CN 200980134083A CN 102143932 A CN102143932 A CN 102143932A
- Authority
- CN
- China
- Prior art keywords
- catalyst
- iron
- support
- dioxide
- silicon
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/41—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by hydrogenolysis or reduction of carboxylic groups or functional derivatives thereof
-
- 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
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/62—Platinum group metals with gallium, indium, thallium, germanium, tin or lead
-
- 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
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C47/00—Compounds having —CHO groups
- C07C47/02—Saturated compounds having —CHO groups bound to acyclic carbon atoms or to hydrogen
- C07C47/06—Acetaldehyde
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/221,135 | 2008-07-31 | ||
| US12/221,135 US7816565B2 (en) | 2008-07-31 | 2008-07-31 | Direct and selective production of acetaldehyde from acetic acid utilizing a supported metal catalyst |
| PCT/US2009/004187 WO2010014146A2 (en) | 2008-07-31 | 2009-07-20 | Direct and selective production of acetaldehyde from acetic acid utilizing a supported metal catalyst |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102143932A true CN102143932A (zh) | 2011-08-03 |
Family
ID=41354062
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009801340830A Pending CN102143932A (zh) | 2008-07-31 | 2009-07-20 | 使用负载金属催化剂由乙酸直接选择性制备乙醛 |
Country Status (14)
| Country | Link |
|---|---|
| US (4) | US7816565B2 (enExample) |
| EP (1) | EP2318348A2 (enExample) |
| JP (2) | JP5053458B2 (enExample) |
| KR (1) | KR20110047209A (enExample) |
| CN (1) | CN102143932A (enExample) |
| AR (1) | AR074714A1 (enExample) |
| AU (1) | AU2009277184B2 (enExample) |
| CA (1) | CA2732364A1 (enExample) |
| CO (1) | CO6541516A2 (enExample) |
| IL (1) | IL210947A0 (enExample) |
| RU (1) | RU2011107273A (enExample) |
| TW (1) | TW201012785A (enExample) |
| WO (1) | WO2010014146A2 (enExample) |
| ZA (1) | ZA201100790B (enExample) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104162446A (zh) * | 2014-08-11 | 2014-11-26 | 华东理工大学 | 用于乙酸加氢制备乙醛的催化剂的制备方法 |
| CN113198521A (zh) * | 2021-04-30 | 2021-08-03 | 江苏常青树新材料科技股份有限公司 | 一种usy分子筛催化剂的制备方法、及该催化剂在制备二乙烯苯中的应用 |
Families Citing this family (65)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8546622B2 (en) | 2008-07-31 | 2013-10-01 | Celanese International Corporation | Process for making ethanol from acetic acid using acidic catalysts |
| US8309772B2 (en) | 2008-07-31 | 2012-11-13 | Celanese International Corporation | Tunable catalyst gas phase hydrogenation of carboxylic acids |
| US8501652B2 (en) | 2008-07-31 | 2013-08-06 | Celanese International Corporation | Catalysts for making ethanol from acetic acid |
| US8637714B2 (en) | 2008-07-31 | 2014-01-28 | Celanese International Corporation | Process for producing ethanol over catalysts containing platinum and palladium |
| US8680317B2 (en) * | 2008-07-31 | 2014-03-25 | Celanese International Corporation | Processes for making ethyl acetate from acetic acid |
| US8304586B2 (en) * | 2010-02-02 | 2012-11-06 | Celanese International Corporation | Process for purifying ethanol |
| US8471075B2 (en) | 2008-07-31 | 2013-06-25 | Celanese International Corporation | Processes for making ethanol from acetic acid |
| US7863489B2 (en) | 2008-07-31 | 2011-01-04 | Celanese International Corporation | Direct and selective production of ethanol from acetic acid utilizing a platinum/tin catalyst |
| US7816565B2 (en) | 2008-07-31 | 2010-10-19 | Celanese International Corporation | Direct and selective production of acetaldehyde from acetic acid utilizing a supported metal catalyst |
| GB0817109D0 (en) * | 2008-09-18 | 2008-10-29 | Johnson Matthey Plc | Catalyst and process |
| US8178715B2 (en) * | 2008-12-31 | 2012-05-15 | Celanese International Corporation | Integrated process for the production of vinyl acetate from acetic acid via acetaldehyde |
| US8680321B2 (en) * | 2009-10-26 | 2014-03-25 | Celanese International Corporation | Processes for making ethanol from acetic acid using bimetallic catalysts |
| US8710277B2 (en) * | 2009-10-26 | 2014-04-29 | Celanese International Corporation | Process for making diethyl ether from acetic acid |
| US8344186B2 (en) | 2010-02-02 | 2013-01-01 | Celanese International Corporation | Processes for producing ethanol from acetaldehyde |
| US8728179B2 (en) | 2010-02-02 | 2014-05-20 | Celanese International Corporation | Ethanol compositions |
| US8222466B2 (en) | 2010-02-02 | 2012-07-17 | Celanese International Corporation | Process for producing a water stream from ethanol production |
| US8541633B2 (en) * | 2010-02-02 | 2013-09-24 | Celanese International Corporation | Processes for producing anhydrous ethanol compositions |
| US8858659B2 (en) * | 2010-02-02 | 2014-10-14 | Celanese International Corporation | Processes for producing denatured ethanol |
| US8747492B2 (en) | 2010-02-02 | 2014-06-10 | Celanese International Corporation | Ethanol/fuel blends for use as motor fuels |
| US8575403B2 (en) | 2010-05-07 | 2013-11-05 | Celanese International Corporation | Hydrolysis of ethyl acetate in ethanol separation process |
| US8460405B2 (en) | 2010-02-02 | 2013-06-11 | Celanese International Corporation | Ethanol compositions |
| EP2531292A2 (en) | 2010-02-02 | 2012-12-12 | Celanese International Corporation | Processes for producing ethanol from acetaldehyde |
| US8680343B2 (en) | 2010-02-02 | 2014-03-25 | Celanese International Corporation | Process for purifying ethanol |
| US8932372B2 (en) | 2010-02-02 | 2015-01-13 | Celanese International Corporation | Integrated process for producing alcohols from a mixed acid feed |
| US8668750B2 (en) | 2010-02-02 | 2014-03-11 | Celanese International Corporation | Denatured fuel ethanol compositions for blending with gasoline or diesel fuel for use as motor fuels |
| US8569551B2 (en) | 2010-05-07 | 2013-10-29 | Celanese International Corporation | Alcohol production process integrating acetic acid feed stream comprising water from carbonylation process |
| US8754267B2 (en) | 2010-05-07 | 2014-06-17 | Celanese International Corporation | Process for separating acetaldehyde from ethanol-containing mixtures |
| US8680342B2 (en) | 2010-05-07 | 2014-03-25 | Celanese International Corporation | Process for recovering alcohol produced by hydrogenating an acetic acid feed stream comprising water |
| US8664454B2 (en) | 2010-07-09 | 2014-03-04 | Celanese International Corporation | Process for production of ethanol using a mixed feed using copper containing catalyst |
| US8710279B2 (en) | 2010-07-09 | 2014-04-29 | Celanese International Corporation | Hydrogenolysis of ethyl acetate in alcohol separation processes |
| US8704008B2 (en) | 2010-07-09 | 2014-04-22 | Celanese International Corporation | Process for producing ethanol using a stacked bed reactor |
| US9272970B2 (en) | 2010-07-09 | 2016-03-01 | Celanese International Corporation | Hydrogenolysis of ethyl acetate in alcohol separation processes |
| FR2972450B1 (fr) * | 2011-03-07 | 2013-04-12 | Rhodia Operations | Preparation d'ethers de (poly)glycerol |
| KR101269857B1 (ko) | 2011-04-14 | 2013-06-07 | 서강대학교산학협력단 | 알킨으로부터 알켄의 선택적 수소화 반응용 촉매 |
| US8592635B2 (en) | 2011-04-26 | 2013-11-26 | Celanese International Corporation | Integrated ethanol production by extracting halides from acetic acid |
| US9073816B2 (en) | 2011-04-26 | 2015-07-07 | Celanese International Corporation | Reducing ethyl acetate concentration in recycle streams for ethanol production processes |
| TW201302684A (zh) | 2011-04-26 | 2013-01-16 | Celanese Int Corp | 由醋酸進料及再循環醋酸乙酯進料生產乙醇之製程 |
| US8754268B2 (en) | 2011-04-26 | 2014-06-17 | Celanese International Corporation | Process for removing water from alcohol mixtures |
| US8895786B2 (en) | 2011-08-03 | 2014-11-25 | Celanese International Corporation | Processes for increasing alcohol production |
| US8853466B2 (en) | 2011-08-19 | 2014-10-07 | Celanese International Corporation | Integrated process for producing ethanol from methanol |
| US8829253B2 (en) | 2011-08-19 | 2014-09-09 | Celanese International Corporation | Integrated process for producing ethanol from methanol |
| US8853467B2 (en) | 2011-08-19 | 2014-10-07 | Celanese International Corporation | Integrated process for producing ethanol |
| US8907142B2 (en) | 2011-12-29 | 2014-12-09 | Celanese International Corporation | Process for promoting catalyst activity for ethyl acetate conversion |
| US9353034B2 (en) | 2012-02-07 | 2016-05-31 | Celanese International Corporation | Hydrogenation process with reduced residence time for vapor phase reactants |
| US8729311B2 (en) * | 2012-02-10 | 2014-05-20 | Celanese International Corporaton | Catalysts for converting acetic acid to acetone |
| US8729317B2 (en) | 2012-02-15 | 2014-05-20 | Celanese International Corporation | Ethanol manufacturing process over catalyst with cesium and support comprising tungsten or oxides thereof |
| US8802903B2 (en) | 2012-03-13 | 2014-08-12 | Celanese International Corporation | Stacked bed reactor with diluents for producing ethanol |
| US9073042B2 (en) | 2012-03-14 | 2015-07-07 | Celanese International Corporation | Acetic acid hydrogenation over a group VIII metal calcined catalyst having a secondary promoter |
| CN102658165B (zh) * | 2012-04-06 | 2014-11-05 | 华东理工大学 | 乙酸气相加氢制备乙醇的催化剂及其制备方法 |
| US8853469B2 (en) | 2012-11-20 | 2014-10-07 | Celanese International Corporation | Combined column for separating products of different hydrogenation reactors |
| WO2014119185A1 (ja) * | 2013-01-30 | 2014-08-07 | 株式会社ダイセル | アセトアルデヒドの製造方法 |
| DE102013106790A1 (de) | 2013-06-28 | 2014-12-31 | Oxea Gmbh | Verfahren zur Herstellung von 1,3-Butandiol |
| DE102013106787A1 (de) | 2013-06-28 | 2014-12-31 | Oxea Gmbh | Verfahren zur Herstellung von n-Butanderivaten |
| WO2015156061A1 (ja) * | 2014-04-10 | 2015-10-15 | 株式会社ダイセル | アセトアルデヒドの製造方法 |
| WO2015163020A1 (ja) * | 2014-04-22 | 2015-10-29 | 株式会社ダイセル | アルデヒド類製造用固体触媒、及びアルデヒド類の製造方法 |
| JP6723151B2 (ja) * | 2014-04-28 | 2020-07-15 | 株式会社ダイセル | 酢酸とアセトアルデヒドと酢酸エチルの製造方法 |
| JP6360801B2 (ja) * | 2015-02-19 | 2018-07-18 | 株式会社ダイセル | 触媒、アルデヒド類及び/又はアルコール類の製造方法 |
| JP6480835B2 (ja) * | 2015-09-02 | 2019-03-13 | 株式会社ダイセル | 固体触媒、固体触媒の製造方法、及びアセトアルデヒドの製造方法 |
| CN105478120B (zh) * | 2015-11-18 | 2017-12-15 | 河南理工大学 | 一种赤泥基铁系催化剂的制备方法及其在甲烷裂解制氢中的应用 |
| JP6650351B2 (ja) * | 2016-06-21 | 2020-02-19 | 株式会社ダイセル | 触媒、触媒の製造方法、及びアルデヒド類の製造方法 |
| JP6758113B2 (ja) * | 2016-07-12 | 2020-09-23 | 株式会社ダイセル | 固体触媒、及びアルデヒド類の製造方法 |
| JP2018149507A (ja) * | 2017-03-14 | 2018-09-27 | 株式会社ダイセル | 触媒及びアルデヒド類の製造方法 |
| JP2019107590A (ja) * | 2017-12-15 | 2019-07-04 | 株式会社ダイセル | 触媒、アルデヒド類および/またはアルコール類の製造方法 |
| JP7098434B2 (ja) * | 2017-12-20 | 2022-07-11 | 株式会社ダイセル | 固体触媒、及びアルデヒド類の製造方法 |
| JP7098435B2 (ja) * | 2018-06-22 | 2022-07-11 | 株式会社ダイセル | 固体触媒、及びアルデヒド類の製造方法 |
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| US7820852B2 (en) | 2008-07-31 | 2010-10-26 | Celanese International Corporation | Direct and selective production of ethyl acetate from acetic acid utilizing a bimetal supported catalyst |
| US7816565B2 (en) | 2008-07-31 | 2010-10-19 | Celanese International Corporation | Direct and selective production of acetaldehyde from acetic acid utilizing a supported metal catalyst |
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-
2008
- 2008-07-31 US US12/221,135 patent/US7816565B2/en not_active Expired - Fee Related
-
2009
- 2009-07-20 AU AU2009277184A patent/AU2009277184B2/en not_active Ceased
- 2009-07-20 CA CA2732364A patent/CA2732364A1/en not_active Abandoned
- 2009-07-20 KR KR1020117004664A patent/KR20110047209A/ko not_active Withdrawn
- 2009-07-20 CN CN2009801340830A patent/CN102143932A/zh active Pending
- 2009-07-20 EP EP09788947A patent/EP2318348A2/en not_active Withdrawn
- 2009-07-20 JP JP2011521093A patent/JP5053458B2/ja not_active Expired - Fee Related
- 2009-07-20 WO PCT/US2009/004187 patent/WO2010014146A2/en not_active Ceased
- 2009-07-20 RU RU2011107273/04A patent/RU2011107273A/ru not_active Application Discontinuation
- 2009-07-31 TW TW098125963A patent/TW201012785A/zh unknown
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| US4351964A (en) * | 1980-05-19 | 1982-09-28 | Kuraray Co., Ltd. | Process for producing acetaldehyde |
| CN1204271A (zh) * | 1995-11-08 | 1999-01-06 | 罗狄亚化学公司 | 钌/锡双金属催化剂的制备方法 |
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| E.J.GROOTENDORST ETAL.: "Selective reduction of acetic acid to acetaldehyde on iron oxides", 《JOURNAL OF CATALYSIS》 * |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104162446A (zh) * | 2014-08-11 | 2014-11-26 | 华东理工大学 | 用于乙酸加氢制备乙醛的催化剂的制备方法 |
| CN113198521A (zh) * | 2021-04-30 | 2021-08-03 | 江苏常青树新材料科技股份有限公司 | 一种usy分子筛催化剂的制备方法、及该催化剂在制备二乙烯苯中的应用 |
| CN113198521B (zh) * | 2021-04-30 | 2023-04-07 | 江苏常青树新材料科技股份有限公司 | 一种usy分子筛催化剂的制备方法、及该催化剂在制备二乙烯苯中的应用 |
Also Published As
| Publication number | Publication date |
|---|---|
| US8227644B2 (en) | 2012-07-24 |
| US20100029993A1 (en) | 2010-02-04 |
| AR074714A1 (es) | 2011-02-09 |
| AU2009277184A2 (en) | 2011-02-24 |
| JP5053458B2 (ja) | 2012-10-17 |
| WO2010014146A3 (en) | 2010-05-06 |
| US7994368B2 (en) | 2011-08-09 |
| KR20110047209A (ko) | 2011-05-06 |
| US20120283480A1 (en) | 2012-11-08 |
| EP2318348A2 (en) | 2011-05-11 |
| CA2732364A1 (en) | 2010-02-04 |
| JP5108980B2 (ja) | 2012-12-26 |
| AU2009277184A1 (en) | 2010-02-04 |
| TW201012785A (en) | 2010-04-01 |
| ZA201100790B (en) | 2012-04-25 |
| US8461395B2 (en) | 2013-06-11 |
| JP2011529494A (ja) | 2011-12-08 |
| US7816565B2 (en) | 2010-10-19 |
| JP2012153698A (ja) | 2012-08-16 |
| AU2009277184B2 (en) | 2012-12-06 |
| CO6541516A2 (es) | 2012-10-16 |
| WO2010014146A2 (en) | 2010-02-04 |
| US20110251435A1 (en) | 2011-10-13 |
| RU2011107273A (ru) | 2012-09-10 |
| IL210947A0 (en) | 2011-04-28 |
| US20110004026A1 (en) | 2011-01-06 |
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