Abstract

Ursodeoxycholic acid is an important clinical drug in the treatment of liver disease. In our previous work, ursodeoxycholic acid was prepared by electroreduction of 7-ketolithocholic acid. The separation of ursodeoxycholic acid from the electroreduction product (47% (w/w) ursodeoxycholic acid) by silylation crystallization is described herein. N,N-dimethylformamide was used as the solvent, whereas hexamethyldisilazane was the reaction agent. The optimal material ratio of electroreduction product/N,N-dimethylformamide/hexamethyldisilazane was found to be 1:10:2 (w/v/v). The reaction proceeded for 2 h at 60°C, and the corresponding silylation derivative was separated by crystallization and pure ursodeoxycholic acid was recovered by 5% acid hydrolysis at 50°C for 0.5 h. The maximum recovery and purity of ursodeoxycholic acid were 99.8% and 99.5%, respectively. Ursodeoxycholic acid with high purity and high recovery can be prepared directly. The developed method offers a potential application for large-scale production of ursodeoxycholic acid.

Highlights

  • Ursodeoxycholic acid is an important clinical drug in the treatment of liver disease

  • Ursodeoxycholic acid (3α, 7β-2-hydroxy-5β-cholanic acid, UDCA) is an important clinical drug used in the treatment of liver disease, such as gallstones [1], alcoholic fatty liver [2], nonalcoholic fatty liver [3], viral hepatitis [4], primary biliary cirrhosis [5], primary sclerosing cholangitis [6], and cholestatic [7]

  • These results indicate that the silylating reagent has an important effect on the recovery and purity of UDCA

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Summary

Introduction

Ursodeoxycholic acid is an important clinical drug in the treatment of liver disease. UDCA was prepared by electroreduction of 7-ketolithocholic acid (3α-hydroxy-7oxo-5β-cholanic acid, 7K-LCA) [9]. UDCA and its epimer chenodeoxycholic acid (3α, 7α-2-hydroxy-5βcholanic acid, CDCA) were both reduction products of 7K-LCA; the product of this electrochemistry conversion was a mixture of 7K-LCA, UDCA, and CDCA, which are difficult to separate. This problem limits its application in the production of UDCA.

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