WO2003091235A1 - Manufacture of ketopantolactone - Google Patents
Manufacture of ketopantolactone Download PDFInfo
- Publication number
- WO2003091235A1 WO2003091235A1 PCT/EP2003/003655 EP0303655W WO03091235A1 WO 2003091235 A1 WO2003091235 A1 WO 2003091235A1 EP 0303655 W EP0303655 W EP 0303655W WO 03091235 A1 WO03091235 A1 WO 03091235A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- ruthenium
- pantolactone
- process according
- solvent system
- iii
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
- C07D307/02—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
- C07D307/34—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
- C07D307/56—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D307/60—Two oxygen atoms, e.g. succinic anhydride
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
- C07D307/02—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
- C07D307/34—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
- C07D307/56—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D307/58—One oxygen atom, e.g. butenolide
Definitions
- the present invention relates to an oxidation process for the manufacture of ketopantolactone. More particularly, the invention relates to a process for the oxidation of pantolactone to ketopantolactone in a microwave field.
- Ketopantolactone is a key intermediate in the manufacture of pantothenic acid, the latter being a member of the B complex vitamins and a constituent of coenzyme A.
- Asymmetric hydrogenation of ketopantolactone yields (D)-(-)-pantolactone, from which pantothenic acid can then be manufactured.
- pantolactone which is the compound of the formula
- ketopantolactone can be produced from pantolactone in superior selectivity and conversion and in a shorter reaction time by oxidation with a periodate (IO 4 , also known as “metaperiodate”; further references to “periodate” hereafter are to be considered equally as references to “metaperiodate”) in the presence of a ruthenium catalyst, in an aqueous solvent system and in a microwave field.
- a periodate IO 4
- the present invention provides a process for the oxidation of pantolactone to ketopantolactone which comprises carrying out the oxidation with a periodate in the presence of a ruthenium catalyst, in an aqueous solvent system and in a microwave field.
- the periodate used in the process of the present invention is suitably an alkali metal periodate such as sodium or potassium periodate [Na + IO or K + IO ].
- the ruthenium catalyst can be any ruthenium catalyst conventionally used in oxidation processes and which is soluble in the aqueous solvent system used in the process of the invention.
- ruthenium(III) salts such as ruthenium(III) halides, particularly ruthenium(III) chloride [RuCl 3 ] and ruthenium(III) bromide [RuBr 3 ], and ruthenium oxides, particularly ruthenium(III) oxide [Ru 2 O 3 ] and hydrates thereof, and ruthenium(IV) oxide [RuO 2 ] and hydrates thereof.
- the preferred catalyst is ruthenium(III) chloride.
- aqueous solvent system denotes a solvent system comprising a mixture of water and an organic water-miscible solvent wherein pantolactone and ketopantolactone are soluble.
- the organic solvent must be at least partially soluble in water; the system, depending upon the organic solvent used, is often a two-phase system. This is the case with for example ethyl acetate as the organic solvent.
- suitable organic solvents are aliphatic esters, e.g. ethyl acetate and isopropyl acetate; cyclic esters, e.g. ⁇ -butyrolactone; and carbonates (“carbonate esters”), e.g. ethylene carbonate and propylene carbonate.
- the volume ratio of water to the organic solvent in the aqueous solvent system is suitably about 1.5 : 1 to about 10 : 1, preferably about 3 : 1 to about 5 : 1.
- the amount of water in the solvent system relative to the amount of starting material pantolactone is suitably from about 1 ml to about 5 ml of water per mmol of pantolactone, preferably about 1.5 ml to about 2.5 ml of water per mmol of pantolactone.
- the preferred organic solvent is ethyl acetate, and the preferred aqueous solvent system containing ethyl acetate as the organic solvent is a mixture of about 2 volumes of water to 1 volume of ethyl acetate.
- the amount of periodate relative to the amount of starting material, pantolactone, used in the process of the present invention is suitably from about 4 g to about 10 g per 1 g of pantolactone, preferably from about 4.5 g to about 6.5 g per 1 g of pantolactone.
- ruthenium catalyst there is suitably used from about 0.001 g to about 0.05 g of ruthenium catalyst per 1 g of pantolactone, preferably about 0.01 g to about 0.015 g of said catalyst per 1 g of pantolactone.
- the microwave field can be provided by any conventional microwave emitting equipment.
- microwave refers to the region of the electromagnetic spectrum having frequencies of 300 MHz to 30 GHz, thus corresponding to wavelengths of 1 m to 1 cm.
- industrial microwave emitters are required by international regulations to operate at wavelengths of either 12.2 cm (2.45 GHz) or 33.3 cm (900 MHz). See in this connection Chem. Soc. Rev. 20, 1-47 ( 1991).
- the applied microwave field has a wavelength of about 12.2 cm or about 33.3 cm.
- the microwave field is generally applied to promote the oxidation for a period of about 1 to about 60 minutes, preferably about 5 to about 40 minutes, and especially preferred about 10 to about 30 minutes.
- Microwave reactors suitable for use in the process of the present invention are for example those in the "Ethos" range, e.g. the Ethos 1600 reactor, as supplied, e.g., by the firm MLS GmbH, Auenweg 37, D-88299 Leutkirch im Allgau, Germany (suppliers outside Germany are for example Milestone S.r.l., Via Fatebenefratelli, 1/5, 1-24010 Sorisole (BG), Italy and Milestone Inc., 160 B Shelton Road, Monroe, CT 06468, USA).
- the irradiation in the process of the invention is carried out applying a power of irradiation of from about 400 W to about 1000 W, more preferably from about 500 W to about 800 W.
- the microwave field is preferably so applied in the oxidation process in accordance with the present invention that the oxidation is carried out at the boiling temperature of the aqueous solvent system used.
- the microwave field is applied to a solution of pantolactone and the ruthenium catalyst in the appropriate aqueous solvent system until the temperature of the reaction mixture has reached its boiling point, i.e. reflux temperature, whereupon the periodate oxidizing agent is added.
- the reaction is suitably monitored, e.g., by gas chromatography, to determine the optimal point of conversion of pantolactone into the desired ketopantolactone.
- the reaction solution is cooled and the desired product, ketopantolactone, isolated, suitably by separating the two solvent phases and evaporation of the non-aqueous phase after removal of solid materials by filtration.
- the aqueous phase normally contains the unreacted materials, and can be recycled if desired to recover inter alia unreacted pantolactone.
- a mixture of 29.5 g of pantolactone, 300 mg of rufheniurn(III) chloride, 400 ml of water and 200 ml of ethyl acetate was heated with stirring to reflux temperature by applying a microwave field generated from a microwave reactor (Ethos 1600, available from MLS GmbH, D-88299 Leutkirch im Allgau, Germany) having a power output of 700 W. 145.5 g of sodium (meta)periodate were added to the boiling mixture within 10 minutes. The reaction mixture was then stirred for a further 20 minutes and thereafter rapidly cooled.
- a microwave reactor Ethos 1600, available from MLS GmbH, D-88299 Leutkirch im Allgau, Germany
- the organic phase was separated from the aqueous phase and the sodium iodate precipitate in the former phase filtered off by suction and washed five times with 20 ml quantities of ethyl acetate.
- the two-phase mixture was separated and the aqueous phase extracted twice with 50 ml of ethyl acetate.
- the combined organic phases were dried over anhydrous magnesium sulphate, filtered and evaporated under reduced pressure.
- Ketopantolactone was thus obtained in a purity of 98% and a yield of 60% based on starting pantolactone. From the aqueous phase an additional 12% of product could be isolated. Unreacted pantolactone was recovered from the aqueous phase.
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)
- Furan Compounds (AREA)
- Catalysts (AREA)
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2003240450A AU2003240450A1 (en) | 2002-04-25 | 2003-04-09 | Manufacture of ketopantolactone |
KR1020047016921A KR100969111B1 (en) | 2002-04-25 | 2003-04-09 | Manufacture of ketopantolactone |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP02009428 | 2002-04-25 | ||
EP02009428.0 | 2002-04-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2003091235A1 true WO2003091235A1 (en) | 2003-11-06 |
Family
ID=29265899
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2003/003655 WO2003091235A1 (en) | 2002-04-25 | 2003-04-09 | Manufacture of ketopantolactone |
Country Status (5)
Country | Link |
---|---|
KR (1) | KR100969111B1 (en) |
CN (1) | CN1332956C (en) |
AU (1) | AU2003240450A1 (en) |
TW (1) | TW200307676A (en) |
WO (1) | WO2003091235A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113816932A (en) * | 2021-10-14 | 2021-12-21 | 宁夏优维生物科技有限公司 | Synthesis method of keto pantolactone |
CN115536520A (en) * | 2022-11-02 | 2022-12-30 | 金川集团股份有限公司 | Preparation method of ruthenium acetate |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4225506A (en) * | 1978-05-30 | 1980-09-30 | Hoffmann-La Roche Inc. | Process for manufacturing a diketone |
US4503238A (en) * | 1982-11-18 | 1985-03-05 | Basf Aktiengesellschaft | Preparation of dihydro-4,4-dimethylfuran-2,3-dione |
US4891435A (en) * | 1982-08-04 | 1990-01-02 | Basf Aktiengesellschaft | Preparation of 4,4-dimethyltetrahydrofuran-2,3-dione |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61242586A (en) | 1985-04-19 | 1986-10-28 | Seitetsu Kagaku Co Ltd | Production of ketopantoic acid salt and/or ketopantolactone |
JPH05306276A (en) * | 1992-04-27 | 1993-11-19 | Mitsubishi Petrochem Co Ltd | Production of ketopantolactone |
-
2003
- 2003-04-09 KR KR1020047016921A patent/KR100969111B1/en not_active IP Right Cessation
- 2003-04-09 WO PCT/EP2003/003655 patent/WO2003091235A1/en not_active Application Discontinuation
- 2003-04-09 AU AU2003240450A patent/AU2003240450A1/en not_active Abandoned
- 2003-04-09 CN CNB038093065A patent/CN1332956C/en not_active Expired - Fee Related
- 2003-04-16 TW TW092108813A patent/TW200307676A/en unknown
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4225506A (en) * | 1978-05-30 | 1980-09-30 | Hoffmann-La Roche Inc. | Process for manufacturing a diketone |
US4891435A (en) * | 1982-08-04 | 1990-01-02 | Basf Aktiengesellschaft | Preparation of 4,4-dimethyltetrahydrofuran-2,3-dione |
US4503238A (en) * | 1982-11-18 | 1985-03-05 | Basf Aktiengesellschaft | Preparation of dihydro-4,4-dimethylfuran-2,3-dione |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113816932A (en) * | 2021-10-14 | 2021-12-21 | 宁夏优维生物科技有限公司 | Synthesis method of keto pantolactone |
CN115536520A (en) * | 2022-11-02 | 2022-12-30 | 金川集团股份有限公司 | Preparation method of ruthenium acetate |
Also Published As
Publication number | Publication date |
---|---|
CN1649860A (en) | 2005-08-03 |
KR100969111B1 (en) | 2010-07-09 |
TW200307676A (en) | 2003-12-16 |
AU2003240450A1 (en) | 2003-11-10 |
CN1332956C (en) | 2007-08-22 |
KR20040111543A (en) | 2004-12-31 |
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