EP1334093A1 - Procede de preparation de dl-alpha-tocopherol avec un haut rendement - Google Patents
Procede de preparation de dl-alpha-tocopherol avec un haut rendementInfo
- Publication number
- EP1334093A1 EP1334093A1 EP00971854A EP00971854A EP1334093A1 EP 1334093 A1 EP1334093 A1 EP 1334093A1 EP 00971854 A EP00971854 A EP 00971854A EP 00971854 A EP00971854 A EP 00971854A EP 1334093 A1 EP1334093 A1 EP 1334093A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- tocopherol
- catalyst
- silica
- alumina
- isophytol
- 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.)
- Withdrawn
Links
- GVJHHUAWPYXKBD-IEOSBIPESA-N α-tocopherol Chemical compound OC1=C(C)C(C)=C2O[C@@](CCC[C@H](C)CCC[C@H](C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-IEOSBIPESA-N 0.000 title claims abstract description 47
- GVJHHUAWPYXKBD-UHFFFAOYSA-N d-alpha-tocopherol Natural products OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-UHFFFAOYSA-N 0.000 title claims abstract description 45
- 229960000984 tocofersolan Drugs 0.000 title claims abstract description 43
- 235000001815 DL-alpha-tocopherol Nutrition 0.000 title claims abstract description 42
- 239000011627 DL-alpha-tocopherol Substances 0.000 title claims abstract description 42
- 238000000034 method Methods 0.000 title claims abstract description 16
- 239000003054 catalyst Substances 0.000 claims abstract description 45
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 30
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims abstract description 29
- KEVYVLWNCKMXJX-ZCNNSNEGSA-N Isophytol Natural products CC(C)CCC[C@H](C)CCC[C@@H](C)CCC[C@@](C)(O)C=C KEVYVLWNCKMXJX-ZCNNSNEGSA-N 0.000 claims abstract description 26
- AUFZRCJENRSRLY-UHFFFAOYSA-N 2,3,5-trimethylhydroquinone Chemical compound CC1=CC(O)=C(C)C(C)=C1O AUFZRCJENRSRLY-UHFFFAOYSA-N 0.000 claims abstract description 24
- -1 Zn(II) ion Chemical class 0.000 claims abstract description 14
- 239000002904 solvent Substances 0.000 claims abstract description 12
- BOTWFXYSPFMFNR-PYDDKJGSSA-N phytol Chemical class CC(C)CCC[C@@H](C)CCC[C@@H](C)CCC\C(C)=C\CO BOTWFXYSPFMFNR-PYDDKJGSSA-N 0.000 claims abstract description 10
- 238000009833 condensation Methods 0.000 claims abstract description 9
- 230000005494 condensation Effects 0.000 claims abstract description 9
- 239000011592 zinc chloride Substances 0.000 claims description 20
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 20
- 238000005245 sintering Methods 0.000 claims description 5
- 125000003668 acetyloxy group Chemical group [H]C([H])([H])C(=O)O[*] 0.000 claims description 2
- 125000005843 halogen group Chemical group 0.000 claims description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 abstract description 14
- 238000002360 preparation method Methods 0.000 abstract description 12
- 229910007570 Zn-Al Inorganic materials 0.000 abstract description 4
- 239000002638 heterogeneous catalyst Substances 0.000 abstract description 3
- 238000007086 side reaction Methods 0.000 abstract description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 2
- 239000000377 silicon dioxide Substances 0.000 abstract 1
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 27
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 9
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 description 5
- 239000006227 byproduct Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 238000010992 reflux Methods 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- 239000011732 tocopherol Substances 0.000 description 4
- 229960001295 tocopherol Drugs 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 229930003799 tocopherol Natural products 0.000 description 3
- 235000010384 tocopherol Nutrition 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229910002796 Si–Al Inorganic materials 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 229940087168 alpha tocopherol Drugs 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000007810 chemical reaction solvent Substances 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000011968 lewis acid catalyst Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000003863 metallic catalyst Substances 0.000 description 1
- 239000012454 non-polar solvent Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 229960001866 silicon dioxide Drugs 0.000 description 1
- ABVVEAHYODGCLZ-UHFFFAOYSA-N tridecan-1-amine Chemical compound CCCCCCCCCCCCCN ABVVEAHYODGCLZ-UHFFFAOYSA-N 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 235000004835 α-tocopherol Nutrition 0.000 description 1
- 239000002076 α-tocopherol Substances 0.000 description 1
Definitions
- the present invention relates to a preparation method of DL-alpha-tocopherol through the condensation between isophytol or phytol derivatives and trimethylhydroquinone (TMHQ) in the presence of a Zn-Al heterogeneous catalyst. More particularly, the present invention relates to a Zn(II)-coated silica-alumina synthetic catalyst which is anchored with a Zn and an Al site, simultaneously and thus are very effective in the preparation of DL- ⁇ -tocopherol with high yield.
- TMHQ trimethylhydroquinone
- DL- ⁇ -tocopherol For the past few decades, extensive effort has been made to effectively prepare DL- ⁇ -tocopherol by use of Zn(II) ions as metallic catalysts (Lewis acid catalyst).
- Zn(II) ions As metallic catalysts (Lewis acid catalyst).
- the DL- ⁇ -tocopherol is prepared through the condensation of an isophytol and trimethylhydroquinone (TMHQ) represented by the following reaction formula 1 :
- U. S . Pat. No. 4,217,285 discloses the synthesis of DL- ⁇ -tocopherol in toluene or n-hexane solvent with ZnCl 2 and silica-alumina (or silica-gel) in the presence of acid, especially HC1, asserting that tocopherol can be obtained with a purity of 95 to 96 % at a production yield of 99 % or higher.
- acid especially HC1
- Hexane although not reacting with isophytol, lengthens the reaction time owing to its low boiling point (approximately 69 °C) such that the catalyst aggravates the dehydration of isophytol. Furthermore, when the synthesis of DL- ⁇ -tocopherol is carried out in such a reaction procedure, by-products analogous in structure to DL- ⁇ - tocopherol are found in relatively large quantities, decreasing the purity of the DL- ⁇ -tocopherol. This is made worse when acid or base is used as a co-catalyst.
- the present inventors developed a Zn(II) ion catalyst system into a Zn-Al based catalyst system which affords an ideal synthetic site for DL- ⁇ -tocopherol.
- a silica-alumina catalyst coated with Zn(II) ions was found to be the most effective in preparing DL- ⁇ -tocopherol from a minimum amount of isophytol or phytol derivatives while generating substantially no by-products.
- the above objects could be accomplished by providing a method for preparing DL- ⁇ - tocopherol at a high yield, comprising condensation reacting isophytol or phytol derivatives with trimethylhydroquinone at 80 to 120 °C for 2 to 7 hours in the presence of a Zn(II) ion-coated silica-alumina catalyst system in hydrocarbon solvent, particularly in n-heptane solvent.
- DL- ⁇ -tocopherol is prepared through the condensation between isophytol or phytol derivatives and TMHQ in the presence of a Zn(II) ion-coated silica-alumina heterogeneous catalyst in a non-polar solvent.
- isophytol or phytol derivatives represented by the following chemical formula I or II:
- mixed catalyst systems in the prior art suffer from the problem caused by employing component catalysts separately. In addition, they are not convenient to handle. With these disadvantages, conventional mixed catalyst systems are considerably difficult to apply for continuous processes for the preparation of DL- ⁇ -tocopherol.
- the problems with the conventional catalyst systems can be overcome by the catalyst system according to the present invention, which has Zn(II) coated on silica-alumina.
- the suitable catalyst in the present invention is made in the form of a Zn(II) supported silica-alumina, such that is anchored with a Zn(II) and an Al (III) site, simultaneously.
- the coating of Zn(II) ions on the silica-alumina support is achieved by impregnating ZnCl 2 into a silica-alumina support and sintering the ZnCl 2 impregnated support at about 400 °C for 2 hours.
- a preferable result is obtained when the catalyst of the present invention is used at an amount of 20 to 450 weight parts based on 100 weight parts of TMHQ.
- the range of 100 to 200 weight parts of the catalyst brings about a more preferable result in the preparation of DL- ⁇ -tocopherol.
- ZnCl 2 is preferably used at an amount of 5 to 250 weight parts based on 100 weight parts of silica-alumina and most preferably at an amount of 20 to 80 weight parts.
- an excellent product of tocopherol is obtained when the amount of the catalyst is maintained in a specific range to the amount of TMHQ as well as when the amount ratio of ZnCl 2 to Si0 2 -Al 2 0 3 is maintained within such a range.
- solvent useful in the present invention examples include aromatic solvents such as toluene, benzene and xylene and aliphatic saturated hydrocarbon solvents such as n-heptane, n- hexane and n-octane with a preference for toluene and n-heptane. Of them, n-heptane guarantees the most preferable synthesis results in the present invention.
- the most preferable period of reaction time falls within the range of 2 to 7 hours, while suitable reaction temperatures are in the range of 80 to 120 °C.
- n-heptane improved the production yield to at least 99%, leaving TMHQ unreacted at a level of 1 % or less.
- 99 % or more of the isophytol took part in the reaction while the corresponding amount, that is, 1 % or less of isophytol was decomposed by the catalyst.
- This result indicates that isophytol is more stable in heptane than in other solvents. Consequently, the employment of heptane as a reaction solvent can minimize the amount of isophytol needed to completely react a given amount of TMHQ, thereby reducing raw material cost for the production of DL- ⁇ -tocopherol.
- the Zn(II) ion-coated silica- alumina catalyst system according to the present invention can remarkably reduce side-reactions upon the condensation between isophytol and TMHQ in comparison with the conventional catalysts for use in preparing DL- ⁇ -tocopherol; thus, producing DL- ⁇ -tocopherol with a high purity at a high yield.
- the catalyst system according to the present invention is greatly improved in being handled and applied for continuous reactions for the preparation of DL- ⁇ -tocopherol.
- the Zn(II) ion-coated silica-alumina catalyst according to the present invention can be effectively used in preparing highly pure DL- ⁇ -tocopherol at a high yield on a commercial scale.
- the present invention has been described in an illustrative manner, and it is to be understood that the terminology used is intended to be in the nature of description rather than of limitation. Many modifications and variations of the present invention are possible in light of the above teachings. Therefore, it is to be understood that within the scope of the appended claims, the invention may be practiced otherwise than as specifically described.
Landscapes
- Pyrane Compounds (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
La présente invention concerne un procédé de préparation de DL-α-tocophérol avec un haut rendement, par condensation d'isophytol ou de dérivés de phytol avec de la triméthylhydroquinone (TMHQ), en présence d'un système catalytique hétérogène à base de Zn-Al. La condensation est menée pendant 2 à 7 heures, à une température allant de 80 à 120 °C, en présence d'un catalyseur à base d'alumine-silice à revêtement d'ions Zn(II), dans un solvant à base de n-heptane. Le système catalytique synthétique à base d'alumine-silice à revêtement d'ions Zn(II) synthétiques est en mesure de réduire de façon remarquable les réactions parallèles lors de la condensation d'isophytol ou de dérivés de phytol et de TMHQ, ce qui permet de produire du DL-α-tocophérol très pur, avec un haut rendement. De plus, le système catalytique est très simple à manipuler et s'applique donc à des réactions continues de préparation de DL-α-tocophérol. De par ces avantages, le système catalytique peut être mis en oeuvre de manière efficace dans la préparation à l'échelle industrielle de DL-α-tocophérol très pur, avec un haut rendement.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/KR2000/001201 WO2002034738A1 (fr) | 2000-10-23 | 2000-10-23 | Procede de preparation de dl-alpha-tocopherol avec un haut rendement |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1334093A1 true EP1334093A1 (fr) | 2003-08-13 |
EP1334093A4 EP1334093A4 (fr) | 2004-02-04 |
Family
ID=27606949
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP00971854A Withdrawn EP1334093A4 (fr) | 2000-10-23 | 2000-10-23 | Procede de preparation de dl-alpha-tocopherol avec un haut rendement |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP1334093A4 (fr) |
JP (1) | JP2004512332A (fr) |
CN (1) | CN1186337C (fr) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103396392B (zh) * | 2013-08-10 | 2014-12-17 | 吉林北沙制药有限公司 | 一种维生素e的绿色环保合成方法 |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5622868B2 (fr) * | 1972-08-30 | 1981-05-27 | ||
JPS6019309B2 (ja) * | 1976-09-29 | 1985-05-15 | 日清製粉株式会社 | 高純度dl−α−トコフエロ−ルの製造法 |
JPS607993B2 (ja) * | 1978-01-12 | 1985-02-28 | 株式会社クラレ | dl−α−トコフエロ−ルの製造方法 |
JPS59190987A (ja) * | 1983-04-11 | 1984-10-29 | Mitsui Toatsu Chem Inc | dl−α−トコフエロ−ルの製造方法 |
JP3416281B2 (ja) * | 1994-04-12 | 2003-06-16 | エーザイ株式会社 | α−トコフェロール誘導体の製造方法および触媒 |
US6005122A (en) * | 1996-12-23 | 1999-12-21 | Basf Aktiengesellschaft | Preparation of α-tocopherol or α-tocopheryl acetate by reacting trimethylhydroquinone and phytol or isophytol, with recycling of the zinc halide condensation catalyst |
FR2784104B1 (fr) * | 1998-09-18 | 2002-12-27 | Rhone Poulenc Nutrition Animal | Procede de preparation de la vitamine e |
-
2000
- 2000-10-23 EP EP00971854A patent/EP1334093A4/fr not_active Withdrawn
- 2000-10-23 JP JP2002537729A patent/JP2004512332A/ja active Pending
- 2000-10-23 CN CNB008199744A patent/CN1186337C/zh not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CN1455775A (zh) | 2003-11-12 |
EP1334093A4 (fr) | 2004-02-04 |
CN1186337C (zh) | 2005-01-26 |
JP2004512332A (ja) | 2004-04-22 |
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Legal Events
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RIC1 | Information provided on ipc code assigned before grant |
Ipc: 7C 07D 311/72 A |
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A4 | Supplementary search report drawn up and despatched |
Effective date: 20031219 |
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RBV | Designated contracting states (corrected) |
Designated state(s): CH DE FR GB LI NL |
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Effective date: 20061117 |
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Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
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Effective date: 20070327 |