There's No Industrial Biocatalyst Like Hydrolase:  Development of Scalable Enantioselective Processes Using Hydrolytic Enzymes1

Chiral, racemic esters, ethyl (±)-tetrahydrofuran-2-carboxylate 4c, methyl (±)-α-phenylpropionate 9b, methyl (±)-5,5-dimethyl-1,3-thiazolidine-4-carboxylate 12a, 2-methoxyethyl (±)-1-(4-tert-butylphenyl)-2-oxopyrrolidine-4-carboxylate 15a, (±)-1-benzyloxy-3-chloropropan-2-yl hydrogen succinate 18c,...

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Published inOrganic process research & development Vol. 7; no. 3; pp. 289 - 296
Main Authors Chikusa, Yasuo, Hirayama, Yoshihiro, Ikunaka, Masaya, Inoue, Toru, Kamiyama, Shunji, Moriwaki, Masafumi, Nishimoto, Yukifumi, Nomoto, Fumiki, Ogawa, Kazuo, Ohno, Tomoyasu, Otsuka, Koutaro, Sakota, Akiko K, Shirasaka, Naoki, Uzura, Atsuko, Uzura, Kensaku
Format Journal Article
LanguageEnglish
Published American Chemical Society 16.05.2003
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Summary:Chiral, racemic esters, ethyl (±)-tetrahydrofuran-2-carboxylate 4c, methyl (±)-α-phenylpropionate 9b, methyl (±)-5,5-dimethyl-1,3-thiazolidine-4-carboxylate 12a, 2-methoxyethyl (±)-1-(4-tert-butylphenyl)-2-oxopyrrolidine-4-carboxylate 15a, (±)-1-benzyloxy-3-chloropropan-2-yl hydrogen succinate 18c, and (±)-3-butyryloxyquinuclidinium butyrate [(±)-20b·n-PrCO2H], are resolved kinetically by enantioselective hydrolysis catalyzed by an Aspergillus melleus protease [E = 60; 93.9% ee and 35% yield for (R)-tetrahydrofuran-2-carboxylic acid 4a], a Klebsiella oxytoca hydrolase [E > 200; 99.5% ee and 36% yield for (S)-α-phenylpropionic acid 9a], a K. oxytoca hydrolase [E = 145; 97.7% ee and 34% yield for (R)-5,5-dimethyl-1,3-thiazolidine-4-carboxylic acid 12b], a Bacillus brevis protease [E = 77; 99% ee and 45% yield for (S)-15a], a Serratia marcescence esterase [E = 49; 99% ee and 43% yield for (S)-18c], and an A. melleus protease [E = 96; 96% ee and 42% yield for (R)-20b], respectively. Each enzymatic process is discussed with focus on the following tactical issues:  (1) identification of a hydrolase with high enantioselectivity, (2) substrate concentrations not less than 1 M that allow for industrially viable volume efficiency (space−time yield), (3) product separation by partition between organic and aqueous phases, and (4) alleviation of a hydrolysate inhibiting the enzymatic activity.
ISSN:1083-6160
1520-586X
DOI:10.1021/op034014b