TY - JOUR
T1 - Continuous enzymatic penicillin G hydrolysis in countercurrent water-butyl acetate biphasic systems
AU - Den Hollander, J. L.
AU - Zomerdijk, M.
AU - Straathof, A. J.J.
AU - Van Der Wielen, L. A.M.
PY - 2002/5/15
Y1 - 2002/5/15
N2 - Penicillin G (Pen G) was continuously hydrolyzed into phenylacetic acid (PAA) and aminopenicillanic acid (APA) by penicillin acylase in countercurrently contacted water-butyl acetate biphasic systems. A set of three mixer-settlers was used to establish countercurrent contact of the two immiscible liquid phases. The enzymatic reaction was catalyzed by immobilized penicillin acylase. Pen G was fed in the central mixer. APA continuously left the system with the aqueous exit stream and PAA with the organic exit stream. The conversion in the countercurrently contacted biphasic system was significantly higher than the conversion that can be achieved in an equivalent batch system. A mathematical model, which is based on partition and reaction equilibria, was used to predict the concentrations and pH along the countercurrent reactor. Provided that no APA crystallization occurs, the mathematical model predicted the conversion and the pH profile in the mixer-settler cascade accurately.
AB - Penicillin G (Pen G) was continuously hydrolyzed into phenylacetic acid (PAA) and aminopenicillanic acid (APA) by penicillin acylase in countercurrently contacted water-butyl acetate biphasic systems. A set of three mixer-settlers was used to establish countercurrent contact of the two immiscible liquid phases. The enzymatic reaction was catalyzed by immobilized penicillin acylase. Pen G was fed in the central mixer. APA continuously left the system with the aqueous exit stream and PAA with the organic exit stream. The conversion in the countercurrently contacted biphasic system was significantly higher than the conversion that can be achieved in an equivalent batch system. A mathematical model, which is based on partition and reaction equilibria, was used to predict the concentrations and pH along the countercurrent reactor. Provided that no APA crystallization occurs, the mathematical model predicted the conversion and the pH profile in the mixer-settler cascade accurately.
KW - 6-aminopenicillanic acid
KW - Enzyme
KW - Extraction
KW - In situ product recovery
KW - Multiphase reactions
KW - Reaction engineering
UR - http://www.scopus.com/inward/record.url?scp=0037095421&partnerID=8YFLogxK
U2 - 10.1016/S0009-2509(02)00035-0
DO - 10.1016/S0009-2509(02)00035-0
M3 - Article
AN - SCOPUS:0037095421
SN - 0009-2509
VL - 57
SP - 1591
EP - 1598
JO - Chemical Engineering Science
JF - Chemical Engineering Science
IS - 9
ER -