In this study, a fibrous bed bioreactor (FBB) system was used to produce ABE (acetone-butanol-ethanol) by immobilized cells of Clostridium beijerinckii NCIMB 8052. To obtain the maximum ABE productivity and yield and maintain the stability of a repeated-batch fermentation process in the FBB system, the optimal dilution rate (0.17 min−1) and initial glucose concentration (18 g/l) in the bioreactor were determined. When the repeated-batch fermentation was maintained at 11 cycles under the optimal conditions, an average of 4.9 g/l butanol (maximum 5.3 g/l) was achieved with an average solvent productivity of 1.0 g/l/h and a yield of 0.41 g/g (maxima of 1.1 g/l/h and 0.43 g/g, respectively). However, the solvent productivity and yield in batch fermentation of free cells were just 0.29 g/l/h and 0.36 g/g, respectively. In addition, scanning electron micrographs demonstrated that C. beijerinckii cells can be adsorbed onto a cotton towel and they exhibited a significantly different morphology compared to immobilized Clostridium acetobutylicum.

1.
D.
Antoni
,
V. V.
Zverlov
, and
W. H.
Schwarz
,
Appl. Microbiol. Biotechnol.
77
,
23
(
2007
).
2.
P.
Dürre
,
Ann. N. Y. Acad. Sci.
1125
,
353
(
2008
).
3.
P.
Kilonzo
,
A.
Margaritis
, and
M.
Bergougnou
,
Bioresour. Technol.
102
,
3662
(
2011
).
4.
K.
Vollherbst-Schneck
,
J. A.
Sands
, and
B. S.
Montenecourt
,
Appl. Environ. Microbiol.
47
,
193
(
1984
).
5.
C.
Lepage
,
F.
Fayolle
,
M.
Herman
, and
J. P.
Vandecasteele
,
J. Microbiol.
133
,
103
(
1987
).
6.
T.
Guo
,
Y.
Tang
,
Y. L.
Xi
,
A. Y.
He
,
B. J.
Sun
,
H.
Wu
,
D. F.
Liang
,
M.
Jiang
, and
P. K.
Ouyang
,
Biotechnol. Lett.
33
,
2379
(
2011
).
7.
E. T.
Papoutsakis
,
Curr. Opin. Biotechnol.
19
,
420
(
2008
).
8.
Y.
Chen
,
H. F.
Ren
,
D.
Liu
,
T.
Zhao
,
X. C.
Shi
,
H.
Cheng
,
N.
Zhao
,
Z. J.
Li
,
B. B.
Li
,
H. Q.
Niu
,
W.
Zhuang
,
J. J.
Xie
,
X. C.
Chen
,
J. L.
Wu
, and
H. J.
Ying
,
Bioresour. Technol.
164
,
276
(
2014
).
9.
T. C.
Ezeji
,
Q.
Nasib
, and
H. P.
Blaschek
,
J. Ind. Microbiol. Biotechnol.
34
,
771
(
2007
).
10.
D. R.
Nielson
and
K. J.
Prather
,
Biotechnol. Bioeng.
102
,
811
(
2009
).
11.
W. E.
Barton
and
A. J.
Daugulis
,
Appl. Microbiol. Biotechnol.
36
,
632
(
1992
).
12.
N.
Qureshi
and
H. P.
Blaschek
,
Biotechnol. Prog.
15
,
594
(
1999
).
13.
E. R.
Kashket
and
Z. Y.
Cao
,
Appl. Environ. Microbiol.
59
,
4198
(
1993
).
14.
N.
Qureshi
,
L. L.
Lai
, and
H. P.
Blaschek
,
Food Bioprod. Process.
82
,
164
(
2004
).
15.
D.
Liu
,
Y.
Chen
,
A.
Li
,
F. Y.
Ding
,
T.
Zhou
,
Y.
He
,
B. B.
Li
,
H. Q.
Niu
,
X. Q.
Lin
,
J. J.
Xie
,
X. C.
Chen
,
J. L.
Wu
, and
H. J.
Ying
,
Bioresour. Technol.
129
,
321
(
2013
).
16.
S.
Loyarkat
,
B.
Cheirsilp
, and
P.
Prasertsan
,
Process Biochem.
50
,
1167
(
2015
).
17.
W. C.
Huang
,
D. E.
Ramey
, and
S. T.
Yang
,
Appl. Biochem. Biotechnol.
115
,
887
(
2004
).
18.
Y.
Chen
,
T.
Zhou
,
D.
Liu
,
A.
Li
,
S. B.
Xu
,
Q. G.
Liu
,
B. B.
Li
, and
H. J.
Ying
,
Biotechnol. Bioprocess Eng.
18
,
234
(
2013
).
19.
Z. M.
Shi
,
L.
Huang
,
X. T.
Wu
,
L. Q.
Luo
,
K. J.
Xiao
,
J.
Cai
, and
Z. N.
Xu
,
J. Chem. Technol. Biotechnol.
89
,
1883
(
2014
).
20.
J.
Lienhardt
,
J.
Schripsema
,
N.
Qureshi
, and
H. P.
Blaschek
,
Appl. Biochem. Biotechnol.
98
,
591
(
2002
).
21.
Y.
Tashiro
,
K.
Takkeda
,
G.
Kobayashi
, and
K.
Sonomoto
,
J. Biotechnol.
120
,
197
(
2005
).
22.
K. V.
Alsaker
,
C.
Paredes
, and
E. T.
Papoutsakis
,
Biotechnol. Bioeng.
105
,
1131
(
2010
).
23.
N.
Qureshi
,
J.
Schripsma
,
J.
Lienhardt
, and
H. P.
Blaschek
,
World J. Microbiol. Biotechnol.
16
,
377
(
2000
).
24.
S. M.
Lee
,
M. O.
Cho
,
C. H.
Park
,
Y. C.
Chung
,
J. H.
Kim
,
B. I.
Sang
, and
Y.
Um
,
Energy Fuel
22
,
3459
(
2008
).
25.
N.
Qureshi
,
A. H. J.
Paterson
, and
I. S.
Maddox
,
Appl. Microbiol. Biotechnol.
29
,
323
(
1988
).
26.
C. U.
Riedel
,
I. R.
Monk
,
P. G.
Casey
,
M. S.
Waidmann
,
C. G. M.
Gahan
, and
C.
Hill
,
Mol. Microbiol.
71
,
1177
(
2009
).
27.
A.
Wuster
and
M. M.
Babu
,
J. Bacteriol.
190
,
743
(
2008
).
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