KR910006196A - 알코올의 제조 공정(제2단계) - Google Patents
알코올의 제조 공정(제2단계) Download PDFInfo
- Publication number
- KR910006196A KR910006196A KR1019900015399A KR900015399A KR910006196A KR 910006196 A KR910006196 A KR 910006196A KR 1019900015399 A KR1019900015399 A KR 1019900015399A KR 900015399 A KR900015399 A KR 900015399A KR 910006196 A KR910006196 A KR 910006196A
- Authority
- KR
- South Korea
- Prior art keywords
- nickel
- catalyst
- carbonyl compound
- weight
- alcohol
- Prior art date
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-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/159—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with reducing agents other than hydrogen or hydrogen-containing gases
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
- C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
- C07C29/14—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of a —CHO group
- C07C29/141—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of a —CHO group with hydrogen or hydrogen-containing gases
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
- C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
- C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
- C07C29/143—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of ketones
- C07C29/145—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of ketones with hydrogen or hydrogen-containing gases
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/17—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrogenation of carbon-to-carbon double or triple bonds
- C07C29/172—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrogenation of carbon-to-carbon double or triple bonds with the obtention of a fully saturated alcohol
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/02—Monohydroxylic acyclic alcohols
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Abstract
내용 없음
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
Claims (11)
- 승온과, 적절하다면, 승압상태에서 유기 카르보닐 화합물과 수소를 2단계 반응시키되 유기 카르보닐 화합물은 제1단계에서 기상으로 구리함유 촉매에 투입되고 제2단계에서는 액상으로 니켈 함유 촉매에 투입되는데, 제1단계에서의 유기 카르보닐 화합물의 이론적 변환율은 80 내지 99.5%이고, 제2단계의 반응은 니켈/알루미나/이산화 지르코늄을 함유하는 지지촉매(Supported catalyst)에 의해서 수행되는 것을 특징으로 하는 알코올의 제조공정.
- 제1항에 있어서, 카르보닐 화합물은 케톤, 케톤유도체, 알데히드 및 알데히드 유도체인 것을 특징으로 하는 알코올의 제조 공정.
- 제1항 내지 2항중 하나 또는 그 이상의 항에 있어서, 카르보닐 화합물은 알데히드 및 알데히드 유도체, 특히 포화 및 불포화 지방족 알데히드인 것을 특징으로 하는 알코올의 제조공정.
- 제1항 내지 2항중 하나 또는 그 이상의 항에 있어서, 카르보닐 화합물은 노르말-부탄알, 2-에틸헥션알인 것을 특징으로 하는 알코올의 제조공정.
- 제1항 내지 4항중 하나 또는 그 이상의 항에 있어서, 구리함유 촉매는 전체 촉매 조성물을 기준으로 하여 15 내지 85중량%의 구리와 0.2 내지 20중량%의 Mgo, 0.03 내지 12중량%의 Cr2O3및 5 내지 80중량%의 SiO2를 부재로 함유하는 것을 특징으로 하는 알코올의 제조공정.
- 제1항 내지 5항중 하나 또는 그 이상의 항에 있어서, 제1단계에서는 온도가 100 내지 200℃, 압력이 0.05 내지 2.0MPa이고 제2단계에서는 온도가 60 내지 150℃, 압력이 0.1 내지 25MPa인 것을 특징으로 하는 알코올의 제조공정.
- 제1항 내지 6중 하나 또는 그 이상의 항에 있어서, 제1단계에서의 카르보닐 화합물의 이론적 변환율은 90 내지 99.0, 특히 93 내지 98%인 것을 특징으로 하는 알코올의 제조공정.
- 제1항 내지 7중 하나 또는 그 이상의 항에 있어서, 수소화반응 촉매는 촉매 조성물을 기준으로 20 내지 90중량%의 니켈과, 니켈 100중량부에 대하여 1 내지 30중량부의 알루미나 및 0.5 내지 20중량부의 이산화 지르코늄이 지지재에 공침된 형태로 이루어진 것을 특징으로 하는 알코올의 제조공정.
- 제1항 내지 8항중 하나 또는 그 이상의 항에 있어서, 니켈/알루미나/이산화지루코늄으로 된 지지 촉매는 지지재로서 활성화 탄소, 클레이, 퓨미스, r-Al2O3, SiO2, 실리카 겔, 규조토와/또는 규산토, 특히 SiO2, 실리카 겔, 규조토와/또는 규산토, 더욱 바람직하게는 규조토와/또는 침전 실리카형태의 SiO2를 함유하는 것을 특징으로 하는 알코올의 제조공정.
- 제1항 내지 9항중 하나 또는 그 이상의 항에 있어서, 니켈/알루미나/이산화지루코늄으로 된 지지 촉매는 니켈 100중량부를 기준으로 하여 6 내지 80, 특히 15 내지 65, 더욱 바람직하게는 35 내지 50중량부의 지지재를 함유하는 것을 특징으로 하는 알코올의 제조공정.
- 제1항 내지 10항중 하나 또는 그 이상의 항에 있어서, 촉매의 부피에 대한 시간당 액상 공급물의 부피(v/vh)로 표시되는 공간속도가 제1단계에서 0.3 내지 1.8, 바람직하게는 0.6 내지 1.5이고, 제2단계에서는 0.5 내지 2.5, 특히 0.7 내지 2.0, 특히 0.5 내지 1.8, 바람직하게는 0.8 내지 1.5인 것을 특징으로 하는 알코올의 제조공정.※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3932331A DE3932331A1 (de) | 1989-09-28 | 1989-09-28 | Verfahren zur herstellung von alkoholen (zweistufig) |
DEP39323315 | 1989-09-28 |
Publications (2)
Publication Number | Publication Date |
---|---|
KR910006196A true KR910006196A (ko) | 1991-04-27 |
KR920009791B1 KR920009791B1 (ko) | 1992-10-22 |
Family
ID=6390349
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1019900015399A KR920009791B1 (ko) | 1989-09-28 | 1990-09-27 | 알코올의 제조 공정(2단계) |
Country Status (10)
Country | Link |
---|---|
US (1) | US5475161A (ko) |
EP (1) | EP0420035B1 (ko) |
JP (1) | JPH0672113B2 (ko) |
KR (1) | KR920009791B1 (ko) |
AT (1) | ATE92456T1 (ko) |
AU (1) | AU628658B2 (ko) |
BR (1) | BR9004787A (ko) |
CA (1) | CA2025859C (ko) |
DE (2) | DE3932331A1 (ko) |
ES (1) | ES2059944T3 (ko) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4025245A1 (de) * | 1990-08-09 | 1992-02-13 | Huels Chemische Werke Ag | Verfahren zur herstellung von gesaettigten alkoholen aus aldehyden |
DE19933691A1 (de) * | 1999-07-17 | 2001-01-18 | Phenolchemie Gmbh & Co Kg | Verfahren zur Hydrierung von Aceton |
JP4754058B2 (ja) * | 2000-10-16 | 2011-08-24 | 三井化学株式会社 | イソプロピルアルコールの製造方法 |
BRPI0508693B1 (pt) * | 2004-03-16 | 2014-10-29 | Mitsubishi Chem Corp | Processo para produção de álcoois purificados |
JP4826709B2 (ja) * | 2004-03-16 | 2011-11-30 | 三菱化学株式会社 | 精製アルコールの製造方法 |
DE102008002201A1 (de) * | 2008-06-04 | 2009-12-10 | Evonik Oxeno Gmbh | Verfahren zur Herstellung von Alkoholen aus Hydroformylierungsgemischen |
DE102011012846B4 (de) | 2011-03-03 | 2016-08-18 | Oxea Gmbh | Verfahren zur Durchführung von mehrphasigen Aldolkondensationsreaktionen zu gemischten α,β-ungesättigten Aldehyden |
DE102012105878A1 (de) | 2012-07-02 | 2014-01-02 | Oxea Gmbh | Verfahren zur Herstellung von Isopentanderivaten |
DE102013113724A1 (de) | 2013-12-09 | 2015-06-11 | Oxea Gmbh | Verfahren zur Herstellung von Pentanderivaten und Derivaten alpha, beta-ungesättigter Decenale aus Propylen |
DE102013113719A1 (de) | 2013-12-09 | 2015-06-11 | Oxea Gmbh | Verfahren zur Herstellung von Pentanderivaten und Derivaten α,β-ungesättigter Decenale |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH338045A (de) * | 1954-08-10 | 1959-04-30 | Larsen Ejner | Verfahren zum Einsilieren von Futtermitteln und Siloverschluss zur Ausübung des Verfahrens |
DE1276618B (de) * | 1965-11-26 | 1968-09-05 | Huels Chemische Werke Ag | Verfahren zur Herstellung von gesaettigten aliphatischen Alkoholen |
US3591656A (en) * | 1969-01-24 | 1971-07-06 | Exxon Research Engineering Co | Heterogeneous catalyst process |
US3978149A (en) * | 1974-08-22 | 1976-08-31 | Exxon Research And Engineering Company | Hydrogenation of organic compounds |
JPS60106534A (ja) * | 1983-11-14 | 1985-06-12 | Mitsubishi Gas Chem Co Inc | メタノ−ル合成用流動触媒 |
JPS60161933A (ja) * | 1984-01-31 | 1985-08-23 | Agency Of Ind Science & Technol | 酸素含有炭化水素化合物の製造方法 |
DE3530839A1 (de) * | 1985-08-29 | 1987-03-05 | Ruhrchemie Ag | Verfahren zur herstellung von 2-ethylhexanol |
GB8613354D0 (en) * | 1986-06-03 | 1986-07-09 | Davy Mckee Ltd | Process |
JP2535876B2 (ja) * | 1987-02-27 | 1996-09-18 | 三菱瓦斯化学株式会社 | 混合アルコ−ル合成用流動触媒 |
GB8917862D0 (en) * | 1989-08-04 | 1989-09-20 | Davy Mckee London | Process |
-
1989
- 1989-09-28 DE DE3932331A patent/DE3932331A1/de not_active Withdrawn
-
1990
- 1990-09-20 ES ES90118080T patent/ES2059944T3/es not_active Expired - Lifetime
- 1990-09-20 DE DE9090118080T patent/DE59002182D1/de not_active Expired - Lifetime
- 1990-09-20 AT AT90118080T patent/ATE92456T1/de not_active IP Right Cessation
- 1990-09-20 CA CA002025859A patent/CA2025859C/en not_active Expired - Fee Related
- 1990-09-20 EP EP90118080A patent/EP0420035B1/de not_active Expired - Lifetime
- 1990-09-21 JP JP2250475A patent/JPH0672113B2/ja not_active Expired - Fee Related
- 1990-09-25 BR BR909004787A patent/BR9004787A/pt not_active IP Right Cessation
- 1990-09-27 KR KR1019900015399A patent/KR920009791B1/ko not_active IP Right Cessation
- 1990-09-27 AU AU63226/90A patent/AU628658B2/en not_active Ceased
-
1992
- 1992-01-17 US US07/824,745 patent/US5475161A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
KR920009791B1 (ko) | 1992-10-22 |
DE3932331A1 (de) | 1991-04-11 |
AU6322690A (en) | 1991-04-11 |
JPH0672113B2 (ja) | 1994-09-14 |
EP0420035A1 (de) | 1991-04-03 |
CA2025859A1 (en) | 1991-03-29 |
ES2059944T3 (es) | 1994-11-16 |
US5475161A (en) | 1995-12-12 |
BR9004787A (pt) | 1991-09-10 |
ATE92456T1 (de) | 1993-08-15 |
EP0420035B1 (de) | 1993-08-04 |
DE59002182D1 (de) | 1993-09-09 |
CA2025859C (en) | 1999-12-21 |
JPH03120234A (ja) | 1991-05-22 |
AU628658B2 (en) | 1992-09-17 |
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