TY - JOUR
T1 - Construction of recombinant Escherichia coli for enhanced bioconversion of colchicine into 3-demethylated colchicine at 70l bioreactor level
AU - Dubey, Kashyap Kumar
AU - Haque, Shafiul
AU - Jawed, Arshad
AU - Singh, Bhanu P.
AU - Behera, B. K.
PY - 2010/7
Y1 - 2010/7
N2 - A recombinant strain of Escherichia coli with CYP102A1 gene was developed for the demethylation of colchicine into their derivatives. The CYP102A1 gene responsible for demethylation was isolated from Bacillus megaterium ACBT03 and amplified using suitable primers. The amplified product was cloned into pET28a+ expression vector using host E. coli BL21(DE3) cells. The CYP3A4 (product of CYP102A1 gene) protein expression and other parameters like substrate toxicity, product toxicity and enzyme activity were optimized in shake flasks; and further scaled-up to 5l bioreactor with 3l working volume. In 5l bioreactor, dissolved oxygen (DO) was optimized for maximum specific growth and enhanced 3-demethylated colchicine (3-DMC) production. The optimized conditions from shake flasks were scaled-up to 70l bioreactor and resulted into ∼80% conversion of 20mM colchicine in 48h with a volumetric productivity of 6.62mgl-1h-1. Scale-up factors were measured as volumetric oxygen transfer coefficient (kLa) i.e., 56h-1 and impeller tip velocity (Vtip) i.e., 7.065ms-1, respectively. The kinetic parameters Km, kcat, and kcat/Km of the CYP3A4 enzyme using colchicine as the substrate were determined to be 271±30μM, 8533±25min-1, and 31.49μMmin-1, respectively, when IPTG induced recombinant E. coli culture was used.
AB - A recombinant strain of Escherichia coli with CYP102A1 gene was developed for the demethylation of colchicine into their derivatives. The CYP102A1 gene responsible for demethylation was isolated from Bacillus megaterium ACBT03 and amplified using suitable primers. The amplified product was cloned into pET28a+ expression vector using host E. coli BL21(DE3) cells. The CYP3A4 (product of CYP102A1 gene) protein expression and other parameters like substrate toxicity, product toxicity and enzyme activity were optimized in shake flasks; and further scaled-up to 5l bioreactor with 3l working volume. In 5l bioreactor, dissolved oxygen (DO) was optimized for maximum specific growth and enhanced 3-demethylated colchicine (3-DMC) production. The optimized conditions from shake flasks were scaled-up to 70l bioreactor and resulted into ∼80% conversion of 20mM colchicine in 48h with a volumetric productivity of 6.62mgl-1h-1. Scale-up factors were measured as volumetric oxygen transfer coefficient (kLa) i.e., 56h-1 and impeller tip velocity (Vtip) i.e., 7.065ms-1, respectively. The kinetic parameters Km, kcat, and kcat/Km of the CYP3A4 enzyme using colchicine as the substrate were determined to be 271±30μM, 8533±25min-1, and 31.49μMmin-1, respectively, when IPTG induced recombinant E. coli culture was used.
KW - Biocatalyst
KW - Bioreactor
KW - CYP3A4 enzyme
KW - Colchicine derivatives
KW - Dissolved oxygen (DO)
KW - Scale-up
UR - https://www.scopus.com/pages/publications/77954815822
U2 - 10.1016/j.procbio.2010.03.014
DO - 10.1016/j.procbio.2010.03.014
M3 - Artículo
AN - SCOPUS:77954815822
SN - 1359-5113
VL - 45
SP - 1036
EP - 1042
JO - Process Biochemistry
JF - Process Biochemistry
IS - 7
ER -