JP5073170B2 - アルコールの製造方法 - Google Patents
アルコールの製造方法 Download PDFInfo
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- JP5073170B2 JP5073170B2 JP2005063359A JP2005063359A JP5073170B2 JP 5073170 B2 JP5073170 B2 JP 5073170B2 JP 2005063359 A JP2005063359 A JP 2005063359A JP 2005063359 A JP2005063359 A JP 2005063359A JP 5073170 B2 JP5073170 B2 JP 5073170B2
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- fats
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- organic solvent
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- glycerin
- Prior art date
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- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims description 12
- 238000004519 manufacturing process Methods 0.000 title claims description 12
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 56
- 239000003054 catalyst Substances 0.000 claims description 28
- 239000003960 organic solvent Substances 0.000 claims description 26
- 238000006243 chemical reaction Methods 0.000 claims description 20
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 claims description 11
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 125000003158 alcohol group Chemical group 0.000 claims 1
- 239000003921 oil Substances 0.000 description 48
- 235000019198 oils Nutrition 0.000 description 48
- 239000003925 fat Substances 0.000 description 47
- 235000019197 fats Nutrition 0.000 description 47
- 235000011187 glycerol Nutrition 0.000 description 26
- 238000000034 method Methods 0.000 description 25
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 18
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 13
- 239000012071 phase Substances 0.000 description 13
- 239000002994 raw material Substances 0.000 description 13
- 238000005984 hydrogenation reaction Methods 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 10
- 235000014113 dietary fatty acids Nutrition 0.000 description 10
- 239000000194 fatty acid Substances 0.000 description 10
- 229930195729 fatty acid Natural products 0.000 description 10
- -1 aliphatic alcohols Chemical class 0.000 description 8
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 8
- 239000010949 copper Substances 0.000 description 8
- 239000012530 fluid Substances 0.000 description 7
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 7
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 6
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 5
- 229910052739 hydrogen Inorganic materials 0.000 description 5
- 235000013772 propylene glycol Nutrition 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 150000001298 alcohols Chemical class 0.000 description 4
- 239000008346 aqueous phase Substances 0.000 description 4
- 150000004665 fatty acids Chemical class 0.000 description 4
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 125000005456 glyceride group Chemical group 0.000 description 3
- 229960004592 isopropanol Drugs 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 3
- 235000014593 oils and fats Nutrition 0.000 description 3
- 239000001294 propane Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 2
- BBMCTIGTTCKYKF-UHFFFAOYSA-N 1-heptanol Chemical compound CCCCCCCO BBMCTIGTTCKYKF-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 2
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- OGBUMNBNEWYMNJ-UHFFFAOYSA-N batilol Chemical class CCCCCCCCCCCCCCCCCCOCC(O)CO OGBUMNBNEWYMNJ-UHFFFAOYSA-N 0.000 description 2
- 239000012018 catalyst precursor Substances 0.000 description 2
- MWKFXSUHUHTGQN-UHFFFAOYSA-N decan-1-ol Chemical compound CCCCCCCCCCO MWKFXSUHUHTGQN-UHFFFAOYSA-N 0.000 description 2
- LQZZUXJYWNFBMV-UHFFFAOYSA-N dodecan-1-ol Chemical compound CCCCCCCCCCCCO LQZZUXJYWNFBMV-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000012046 mixed solvent Substances 0.000 description 2
- GLDOVTGHNKAZLK-UHFFFAOYSA-N octadecan-1-ol Chemical compound CCCCCCCCCCCCCCCCCCO GLDOVTGHNKAZLK-UHFFFAOYSA-N 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000003346 palm kernel oil Substances 0.000 description 2
- 235000019865 palm kernel oil Nutrition 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- HLZKNKRTKFSKGZ-UHFFFAOYSA-N tetradecan-1-ol Chemical compound CCCCCCCCCCCCCCO HLZKNKRTKFSKGZ-UHFFFAOYSA-N 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 235000019482 Palm oil Nutrition 0.000 description 1
- 241000183024 Populus tremula Species 0.000 description 1
- 235000019484 Rapeseed oil Nutrition 0.000 description 1
- 239000004164 Wax ester Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000003240 coconut oil Substances 0.000 description 1
- 235000019864 coconut oil Nutrition 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 150000002191 fatty alcohols Chemical class 0.000 description 1
- 235000021323 fish oil Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- BXWNKGSJHAJOGX-UHFFFAOYSA-N hexadecan-1-ol Chemical compound CCCCCCCCCCCCCCCCO BXWNKGSJHAJOGX-UHFFFAOYSA-N 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229940057995 liquid paraffin Drugs 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 235000012149 noodles Nutrition 0.000 description 1
- 239000002540 palm oil Substances 0.000 description 1
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000003826 tablet Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
- 150000003626 triacylglycerols Chemical class 0.000 description 1
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 description 1
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 235000019386 wax ester Nutrition 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Images
Classifications
-
- 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
- C07C29/147—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 carboxylic acids or derivatives thereof
- C07C29/149—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 carboxylic acids or derivatives thereof with hydrogen or hydrogen-containing gases
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Fats And Perfumes (AREA)
Description
内径13mmの反応器に30ccの日揮化学社製Cu/Cr成形触媒(N202D)を充填した固定床反応器を用い、圧力19.8MPa、触媒層温度200℃、原料油脂に対する水素モル比75の条件で接触水素化反応を行った。
また、グリセリン選択性は、ガスクロマトグラフ法にて検出された水相中の全有機物に対するグリセリンの割合(重量%)と定義した。油相中の脂肪族アルコール以外の物質は脂肪酸アルキルエステル、モノグリセリド、ジグリセリドが主であり、水相中のグリセリン以外の物質はプロピレングリコール、n−プロパノール、iso−プロパノールが主であった。
実施例1の方法に従い、原料油脂を12cc/Hr、メタノールを原料油脂1モルに対して60モル倍相当の流量で反応器に供給し、反応器出口の原料油脂の反応率、油相中の脂肪族アルコールの含有量、脂肪酸アルキルエステルの含有量及びグリセリン選択性を実施例1と同様に分析した。
内径13mmの反応器に30ccの日揮化学社製Cu/Cr成形触媒(N202D)を充填した固定床反応器を用い、圧力19.8MPa、触媒層温度200℃、原料油脂に対する水素モル比75の条件で接触水素化反応を行った。
原料油脂200gを容積500mlの回転攪拌式オートクレーブに仕込んだ。反応には日揮化学社製Cu/Cr成形触媒(N202D)15gをバスケットに入れて使用し、230℃に昇温後、全圧24.5MPa、攪拌速度900r/minの条件で0.2時間接触水素化反応を行った。また、触媒は予め水素圧力1MPa、温度200℃、2時間の条件で活性化したものを使用した。
比較例2の方法に従い、5時間接触水素化反応を行った。
Claims (2)
- 触媒存在下、油脂の水素化反応を行いアルコールを製造する方法であって、有機溶媒を共存させて、温度120〜280℃、圧力1〜30MPa、有機溶媒の原料油脂に対するモル比(有機溶媒/油脂)が1〜500、触媒を除く反応系が均一相を形成しない条件で反応を行う、脂肪族アルコール及びグリセリンの製造方法。
- 有機溶媒が、炭素数1〜6のアルコールである請求項1に記載の脂肪族アルコール及びグリセリンの製造方法。
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2005063359A JP5073170B2 (ja) | 2005-03-08 | 2005-03-08 | アルコールの製造方法 |
US11/367,340 US7667059B2 (en) | 2005-03-08 | 2006-03-06 | Process for producing glycerin and fatty alcohol via hydrogenation |
DE102006010549A DE102006010549A1 (de) | 2005-03-08 | 2006-03-07 | Verfahren zur Herstellung eines Alkohols |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2005063359A JP5073170B2 (ja) | 2005-03-08 | 2005-03-08 | アルコールの製造方法 |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2012133684A Division JP2012193187A (ja) | 2012-06-13 | 2012-06-13 | アルコールの製造方法 |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2006248899A JP2006248899A (ja) | 2006-09-21 |
JP5073170B2 true JP5073170B2 (ja) | 2012-11-14 |
Family
ID=36934055
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2005063359A Expired - Fee Related JP5073170B2 (ja) | 2005-03-08 | 2005-03-08 | アルコールの製造方法 |
Country Status (3)
Country | Link |
---|---|
US (1) | US7667059B2 (ja) |
JP (1) | JP5073170B2 (ja) |
DE (1) | DE102006010549A1 (ja) |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100390123C (zh) * | 2003-09-09 | 2008-05-28 | 花王株式会社 | 醇的制造方法 |
MY144033A (en) * | 2005-03-08 | 2011-07-29 | Kao Corp | Process for producing an alcohol |
DE102008008872B4 (de) * | 2008-02-13 | 2010-04-29 | Lurgi Gmbh | Verfahren zum Herstellen von Fettalkoholen |
US8704007B2 (en) | 2011-12-09 | 2014-04-22 | Chevron U.S.A. Inc. | Hydroconversion of renewable feedstocks |
CA2858585C (en) * | 2011-12-09 | 2018-10-16 | Chevron U.S.A. Inc. | Hydroconversion of renewable feedstocks |
US9199909B2 (en) | 2011-12-09 | 2015-12-01 | Chevron U.S.A. Inc. | Hydroconversion of renewable feedstocks |
US9266802B2 (en) | 2011-12-09 | 2016-02-23 | Chevron U.S.A. Inc. | Hydroconversion of renewable feedstocks |
US8865949B2 (en) | 2011-12-09 | 2014-10-21 | Chevron U.S.A. Inc. | Hydroconversion of renewable feedstocks |
JP2012193187A (ja) * | 2012-06-13 | 2012-10-11 | Kao Corp | アルコールの製造方法 |
JP6063722B2 (ja) * | 2012-11-27 | 2017-01-18 | 花王株式会社 | アルコール及びグリセリンの製造方法 |
CN105503527B (zh) * | 2014-09-23 | 2018-08-07 | 中国石油化工股份有限公司 | 超临界癸二酸二甲酯加氢制备1,10-癸二醇的方法 |
WO2017203959A1 (ja) * | 2016-05-24 | 2017-11-30 | 花王株式会社 | 藻類の処理方法 |
JP6985792B2 (ja) * | 2016-05-24 | 2021-12-22 | 花王株式会社 | 藻類の処理方法 |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2241417A (en) | 1930-01-27 | 1941-05-13 | American Hyalsol Corp | Higher aliphatic alcohols |
US2094127A (en) | 1932-01-02 | 1937-09-28 | Du Pont | Mixed higher alcohols |
US2109844A (en) | 1932-02-27 | 1938-03-01 | Du Pont | Catalytic hydrogenation of glycerides of aliphatic carboxylic acids |
DE1668219A1 (de) | 1967-11-10 | 1972-03-16 | Hydrocarbon Research Inc | Hydrierung von Fetten und OElen |
NL7904782A (nl) * | 1979-06-19 | 1980-12-23 | Unilever Nv | Werkwijze voor het selectief hydrogeneren van vetzuurderivaten. |
DE3776997D1 (de) * | 1986-07-23 | 1992-04-09 | Henkel Kgaa | Verfahren zur direkthydrierung von glyceridoelen. |
DE3809270A1 (de) * | 1988-03-19 | 1989-09-28 | Henkel Kgaa | Verfahren zur katalytischen hydrierung von fluessigen fettsaeure-triglyceriden zur gleichzeitigen gewinnung von fettalkoholen und c(pfeil abwaerts)3(pfeil abwaerts)-diolen |
JPH0453474A (ja) * | 1990-06-21 | 1992-02-21 | Morinaga Milk Ind Co Ltd | 直接加熱殺菌方法及び装置 |
JPH04282329A (ja) * | 1991-03-08 | 1992-10-07 | Ube Ind Ltd | アルコールの製造方法 |
DE4242466C2 (de) | 1992-12-16 | 2003-07-03 | Cognis Deutschland Gmbh | Verfahren zur Herstellung von Fettalkoholen |
US5334779A (en) * | 1993-06-01 | 1994-08-02 | Eastman Kodak Company | Catalyst compositions and the use thereof in the hydrogenation of carboxylic acid esters |
MY129140A (en) * | 1994-11-07 | 2007-03-30 | Shell Int Research | Process and a catalyst for the direct hydrogenation of carboxylic esters |
US5475160A (en) | 1994-11-07 | 1995-12-12 | Shell Oil Company | Process for the direct hydrogenation of triglycerides |
JPH08169855A (ja) * | 1994-12-16 | 1996-07-02 | Kao Corp | 高級アルコールの製造方法 |
JP3779752B2 (ja) * | 1995-08-14 | 2006-05-31 | 昭和電工株式会社 | アルコール、ラクトンまたはエーテルの製造法 |
JPH08198786A (ja) * | 1995-01-25 | 1996-08-06 | Mitsubishi Chem Corp | カルボン酸エステルの水素化方法 |
JP4037393B2 (ja) * | 2003-09-09 | 2008-01-23 | 花王株式会社 | アルコールの製造方法 |
-
2005
- 2005-03-08 JP JP2005063359A patent/JP5073170B2/ja not_active Expired - Fee Related
-
2006
- 2006-03-06 US US11/367,340 patent/US7667059B2/en not_active Expired - Fee Related
- 2006-03-07 DE DE102006010549A patent/DE102006010549A1/de not_active Ceased
Also Published As
Publication number | Publication date |
---|---|
JP2006248899A (ja) | 2006-09-21 |
US20060205965A1 (en) | 2006-09-14 |
DE102006010549A1 (de) | 2006-09-21 |
US7667059B2 (en) | 2010-02-23 |
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