WO1998056750A1 - A process for the preparation of diacerein - Google Patents

A process for the preparation of diacerein Download PDF

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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
Application number
PCT/EP1998/003221
Other languages
German (de)
English (en)
French (fr)
Inventor
Monica Sinistri
Roberta Sinistri
Original Assignee
Synteco S.R.L.
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Synteco S.R.L. filed Critical Synteco S.R.L.
Priority to AU85356/98A priority Critical patent/AU8535698A/en
Publication of WO1998056750A1 publication Critical patent/WO1998056750A1/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2603/00Systems 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)
PCT/EP1998/003221 1997-06-11 1998-05-29 A process for the preparation of diacerein WO1998056750A1 (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (2)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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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