WO1998056750A1 - A process for the preparation of diacerein - Google Patents
A process for the preparation of diacerein Download PDFInfo
- Publication number
- WO1998056750A1 WO1998056750A1 PCT/EP1998/003221 EP9803221W WO9856750A1 WO 1998056750 A1 WO1998056750 A1 WO 1998056750A1 EP 9803221 W EP9803221 W EP 9803221W WO 9856750 A1 WO9856750 A1 WO 9856750A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- diacerein
- acid
- crude
- process according
- solution
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2603/00—Systems containing at least three condensed rings
Definitions
- the present invention relates to a process for the preparation of diacerein.
- Diacerein or diacetylrein (1 ,8-diacetoxy-3- carboxyanthraquinone) is a known antiarthritic medicament used for some time in clinical practice.
- FR-A-2508798 describes the acetylation of rein ( 1 , 8-dihydroxyanthraquinone-3- carboxylic acid), with an acetic anhydride excess in the presence of sulfuric acid.
- EP-A-636602 discloses a preparation process characterized by purificating the crude diacerein by crystallization from 2-methoxyethanol or N,N- dimethylacetamide .
- the methods described above, as well as other known ones, suffer anyway from some drawbacks (use of expensive, toxic solvents, difficulty of purification, unsatisfactory yields) which restrict its industrial use.
- the purification step of crude diacerein is particularly critical.
- the process of the invention comprises: a) acetylation of aloin, of formula (I): to give acetyl-barbaloin (II)
- Step a) is preferably effected using acetic anhydride as acetylating agent.
- the reaction is typically carried out using an acetic anhydride excess in the presence of bases such as potassium acetate, at a temperature of about 130°-140 ⁇ C.
- Step b) is preferably carried out using chromic anhydride in acetic acid solution.
- Chromic anhydride is used in excess to the stoichiometric, for example in molar ratios ranging from 5:1 to 10:1 compared with the starting aloin.
- the reaction temperature usually ranges from 40 to 60°C.
- the oxidation is preferably carried out without previous recovery of the compound (II).
- step c) organic amines such as triethylamine, trimethylamine and the like can be used.
- triethylamine in acetone solution is used, which is added to an acetone aqueous solution of crude diacerein.
- the organic acid alkali salt is preferably 2-sodium ethylhexanoate , added in acetone/isopropanol solution.
- the sodium salt is filtered, washed with acetone and dried.
- Any organic or inorganic acid such as hydrochloric acid, sulfuric acid, acetic acid, p-toluenesulfonic acid, phosphoric acid, can be used for the conversion to acid diacerein.
- Particularly preferred is the use of diluted phosphoric acid, at concentrations ranging from 1 to about 30%.
- Example 1 illustrates the invention in greater detail.
- a 1000 It reactor is loaded with 25 kg of aloin, 8.8 kg of anhydrous potassium acetate and 125 kg of acetic anhydride. The mixture is heated to 135°C, keeping said temperature for 60 minutes, after that is cooled to about 50 ⁇ C and added with 250 kg of acetic anhydride. Keeping the temperature at 55 ⁇ C, a solution of 30 kg of chromic anhydride dissolved in 100 kg of acetic acid is added in about 4 hours. At the end of the addition, temperature is kept at 55°C for 30 minutes, then 210 kg of water are added. After cooling at 15°C, the reaction mixture is centrifuged and washed to neutrality with water, finally dried at 70"C. The yield in crude diacerein is 15 kg with a K.F. lower than 0.5%.
- a 1000 It reactor is loaded with 25 kg of aloin, 9 kg of anhydrous potassium acetate and 130 kg of acetic anhydride. The mixture is heated to 138 ⁇ C keeping said temperature for 60 minutes, after that is cooled to about 50°C and added with 260 kg of acetic anhydride. Temperature is brought to 45°C, then a solution of 31 kg of chromic anhydride dissolved in 105 1 of acetic acid is added in about 5 hours, keeping said temperature. At the end of the addition, temperature is kept for 30 minutes, then 220 kg of water are added. After cooling at 15°C, the reaction mixture is centrifuged, washing the cake with water to neutrality, then dried at 70°C. 15 kg of crude diacerein are obtained, having a 0.5% maximum K.F.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU85356/98A AU8535698A (en) | 1997-06-11 | 1998-05-29 | A process for the preparation of diacerein |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ITMI97A001375 | 1997-06-11 | ||
IT97MI001375A IT1292132B1 (it) | 1997-06-11 | 1997-06-11 | Procedimento per la preparazione di diacereina |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998056750A1 true WO1998056750A1 (en) | 1998-12-17 |
Family
ID=11377340
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP1998/003221 WO1998056750A1 (en) | 1997-06-11 | 1998-05-29 | A process for the preparation of diacerein |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU8535698A (hu) |
IT (1) | IT1292132B1 (hu) |
WO (1) | WO1998056750A1 (hu) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000068179A1 (en) * | 1999-05-07 | 2000-11-16 | Synteco S.P.A. | A process for the purification of diacerein |
WO2001044144A2 (en) * | 1999-12-17 | 2001-06-21 | Ranbaxy Laboratories Limited | Process for the preparation of sodium salts of statins |
CN101696164A (zh) * | 2009-10-19 | 2010-04-21 | 黄再新 | 一步法用芦荟甙合成双醋瑞因粗品的方法 |
WO2011030350A1 (en) | 2009-09-08 | 2011-03-17 | Lupin Limited | Eco-friendly method for catalytic aerial oxidation of aloe-emodin to rheinal |
WO2011099834A2 (es) * | 2010-02-15 | 2011-08-18 | Interquim, S.A. De C.V. | Procedimiento para la purificación de diacereina cruda vía sal de potasio/dimetil formamida |
EP2497761A1 (en) | 2011-02-11 | 2012-09-12 | ICROM S.p.A. | Process for the purification of anthraquinone derivatives |
CN115521205A (zh) * | 2022-09-22 | 2022-12-27 | 北京百奥药业有限责任公司 | 双醋瑞因钠盐的晶型及其制备方法 |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0636602A1 (en) * | 1993-07-30 | 1995-02-01 | Laboratoire Medidom S.A. | A process for the preparation of diacerein |
WO1996024572A1 (fr) * | 1995-02-07 | 1996-08-15 | Steba Beheer B.V. | Procede de purification de la diacetylrheine |
-
1997
- 1997-06-11 IT IT97MI001375A patent/IT1292132B1/it active IP Right Grant
-
1998
- 1998-05-29 WO PCT/EP1998/003221 patent/WO1998056750A1/en active Search and Examination
- 1998-05-29 AU AU85356/98A patent/AU8535698A/en not_active Abandoned
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0636602A1 (en) * | 1993-07-30 | 1995-02-01 | Laboratoire Medidom S.A. | A process for the preparation of diacerein |
WO1996024572A1 (fr) * | 1995-02-07 | 1996-08-15 | Steba Beheer B.V. | Procede de purification de la diacetylrheine |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100700687B1 (ko) * | 1999-05-07 | 2007-03-27 | 신테코 에스.피.아. | 디아세레인 정제방법 |
WO2000068179A1 (en) * | 1999-05-07 | 2000-11-16 | Synteco S.P.A. | A process for the purification of diacerein |
AU772845B2 (en) * | 1999-05-07 | 2004-05-06 | Synteco S.P.A. | A process for the purification of diacerein |
JP2002544183A (ja) * | 1999-05-07 | 2002-12-24 | シンテコ エッセ.ピ.ア. | ジアセレインの精製方法 |
WO2001044144A3 (en) * | 1999-12-17 | 2001-11-15 | Ranbaxy Lab Ltd | Process for the preparation of sodium salts of statins |
US6756507B2 (en) | 1999-12-17 | 2004-06-29 | Ranbaxy Laboratories Limited | Process for the preparation of sodium salts of statins |
WO2001044144A2 (en) * | 1999-12-17 | 2001-06-21 | Ranbaxy Laboratories Limited | Process for the preparation of sodium salts of statins |
WO2011030350A1 (en) | 2009-09-08 | 2011-03-17 | Lupin Limited | Eco-friendly method for catalytic aerial oxidation of aloe-emodin to rheinal |
CN101696164A (zh) * | 2009-10-19 | 2010-04-21 | 黄再新 | 一步法用芦荟甙合成双醋瑞因粗品的方法 |
WO2011099834A2 (es) * | 2010-02-15 | 2011-08-18 | Interquim, S.A. De C.V. | Procedimiento para la purificación de diacereina cruda vía sal de potasio/dimetil formamida |
WO2011099834A3 (es) * | 2010-02-15 | 2013-01-03 | Interquim, S.A. De C.V. | Procedimiento para la purificación de diacereina cruda vía sal de potasio/dimetil formamida |
EP2497761A1 (en) | 2011-02-11 | 2012-09-12 | ICROM S.p.A. | Process for the purification of anthraquinone derivatives |
CN115521205A (zh) * | 2022-09-22 | 2022-12-27 | 北京百奥药业有限责任公司 | 双醋瑞因钠盐的晶型及其制备方法 |
CN115521205B (zh) * | 2022-09-22 | 2023-11-10 | 北京百奥药业有限责任公司 | 双醋瑞因钠盐的晶型及其制备方法 |
Also Published As
Publication number | Publication date |
---|---|
IT1292132B1 (it) | 1999-01-25 |
ITMI971375A0 (hu) | 1997-06-11 |
ITMI971375A1 (it) | 1998-12-11 |
AU8535698A (en) | 1998-12-30 |
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