TY - JOUR
T1 - Continuous production of butanol from starch-based packing peanuts
AU - Ezeji, Thaddeus C.
AU - Groberg, Marisa
AU - Qureshi, Nasib
AU - Blaschek, Hans P.
N1 - Funding Information:
We gratefully acknowledge the kind gift of the packing peanuts from Storopack, Cleveland, OH. This work was supported by grants from Illinois Corn Marketing Board and Illinois Council on Food and Agricultural Research (CFAR IDA CF 01E-35-1).
PY - 2003/3
Y1 - 2003/3
N2 - Acetone, butanol, ethanol (ABE, or solvents) were produced from starch-based packing peanuts in batch and continuous reactors. In a batch reactor, 18.9 g/L of total ABE was produced from 80 g/L packing peanuts in 110 h of fermentation. The initial and final starch concentrations were 69.6 and 11.1 g/L, respectively. In this fermentation, ABE yield and productivity of 0.32 and 0.17 g/(L·h) were obtained, respectively. Compared to the batch fermentation, continuous fermentation of 40 g/L of starch-based packing peanuts in P2 medium resulted in a maximum solvent production of 8.4 g/L at a dilution rate of 0.033 h-1. This resulted in a productivity of 0.27 g/(L·h). However, the reactor was not stable and fermentation deteriorated with time. Continuous fermentation of 35 g/L of starch solution resulted in a similar performance. These studies were performed in a vertical column reactor using Clostridium beijerinckii BA101 and P2 medium. It is anticipated that prolonged exposure of culture to acrylamide, which is formed during boiling/autoclaving of starch, affects the fermentation negatively.
AB - Acetone, butanol, ethanol (ABE, or solvents) were produced from starch-based packing peanuts in batch and continuous reactors. In a batch reactor, 18.9 g/L of total ABE was produced from 80 g/L packing peanuts in 110 h of fermentation. The initial and final starch concentrations were 69.6 and 11.1 g/L, respectively. In this fermentation, ABE yield and productivity of 0.32 and 0.17 g/(L·h) were obtained, respectively. Compared to the batch fermentation, continuous fermentation of 40 g/L of starch-based packing peanuts in P2 medium resulted in a maximum solvent production of 8.4 g/L at a dilution rate of 0.033 h-1. This resulted in a productivity of 0.27 g/(L·h). However, the reactor was not stable and fermentation deteriorated with time. Continuous fermentation of 35 g/L of starch solution resulted in a similar performance. These studies were performed in a vertical column reactor using Clostridium beijerinckii BA101 and P2 medium. It is anticipated that prolonged exposure of culture to acrylamide, which is formed during boiling/autoclaving of starch, affects the fermentation negatively.
KW - Butanol
KW - Clostridium beijerinckii BA101
KW - Continuous fermentation
KW - Dilution rate
KW - Reactor
KW - Starch-based packing peanuts
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U2 - 10.1385/ABAB:106:1-3:375
DO - 10.1385/ABAB:106:1-3:375
M3 - Article
C2 - 12721460
AN - SCOPUS:0038748266
SN - 0273-2289
VL - 106
SP - 375
EP - 382
JO - Applied Biochemistry and Biotechnology - Part A Enzyme Engineering and Biotechnology
JF - Applied Biochemistry and Biotechnology - Part A Enzyme Engineering and Biotechnology
IS - 1-3
ER -