TY - JOUR
T1 - A mathematical model for the synthesis of Gly-Phe by papain in an aqueous-organic system
AU - Feliu, J.A
AU - de Mas, C
AU - López Santín, J
PY - 1996/1/1
Y1 - 1996/1/1
N2 - The synthesis of the protected dipeptide BocGly-PheOMe, has been modellised when working in an aqueous-organic biphasic system, with papain as a catalyst. The mathematical model takes into account that one of the substrates, PheOMe, has parallel hydrolysis reactions and that the reaction only takes place in the aqueous phase while the whole reaction system is biphasic. The reaction system has been modellised when working in batch as well as when working in fed-batch mode, achieving a good prediction of the product evolution for both working strategies. When working in fed-batch mode, the extension of the undesired parallel reactions has been diminished, the model has been used for a computer aided optimisation of the addition sequence of PheOMe. The results obtained led to a process operation strategy with a compromise between yield and productivity.
AB - The synthesis of the protected dipeptide BocGly-PheOMe, has been modellised when working in an aqueous-organic biphasic system, with papain as a catalyst. The mathematical model takes into account that one of the substrates, PheOMe, has parallel hydrolysis reactions and that the reaction only takes place in the aqueous phase while the whole reaction system is biphasic. The reaction system has been modellised when working in batch as well as when working in fed-batch mode, achieving a good prediction of the product evolution for both working strategies. When working in fed-batch mode, the extension of the undesired parallel reactions has been diminished, the model has been used for a computer aided optimisation of the addition sequence of PheOMe. The results obtained led to a process operation strategy with a compromise between yield and productivity.
UR - https://www.scopus.com/pages/publications/85047676613
U2 - 10.1007/BF00369435
DO - 10.1007/BF00369435
M3 - Article
SN - 0178-515X
VL - 14
SP - 163
EP - 168
JO - Bioprocess Engineering
JF - Bioprocess Engineering
IS - 3
ER -