Photoautotrophic cell and tissue culture in a tubular photobioreactor

被引:24
作者
Perner-Nochta, I. [1 ]
Lucumi, A. [1 ]
Posten, C. [1 ]
机构
[1] Univ Karlsruhe, Inst Engn Life Sci, D-76128 Karlsruhe, Germany
来源
ENGINEERING IN LIFE SCIENCES | 2007年 / 7卷 / 02期
关键词
algae; bioreactors; biotechnology; mixing; plants;
D O I
10.1002/elsc.200620178
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
An externally illuminated tubular photobioreactor was constructed from 3.4 in stainless steel tubes and 22.1 in glass tubes for the cultivation of photoautotrophic organisms. The 30-L reactor can be equipped with helical static mixers in order to create a uniform radial exchange within the tubes, 40 mm in diameter. A flexible construction of the reactor allows scale-down experiments to be carried out with axial velocities between 0.3-2.5 m/s, gassing-in rates of 0-0.5 L/min, k(L)a values of 0.002-0.006 s(-1) and six metal halide lamps inducing photon flux densities in the range of 70-300 mu E/m(2)s. Two model organisms, the green micro-algae Chlorella vulgaris and the bryophyte Physcomitrella patens, were chosen to characterize cell growth and physiology in submerse cultures. Comparative experiments with Chlorella vulgaris in two configurations of the reactor with inserted helical static mixers and plates resulted in maximum growth rates of 1.6 d(-1). No growth enhancement was obtained in the case of helical static mixers at a mean PFD of 150 mu E/m(2)s and an axial velocity of 0.4 m/s. No homogenous flow could be obtained in the case of inserted plates. Physcomitrella patens was successfully cultivated in the reactor (mu = 0.36 d(-1)), whereas average axial velocities of ca. 0.6 m/s guarantee favorable gas transport without contributing to cell damage. This makes tubular photobioreactors a promising production system for the production of glycosylated recombinant proteins derived from moss.
引用
收藏
页码:127 / 135
页数:9
相关论文
共 31 条
[1]   Hydrodynamics and mass transfer in a tubular airlift photobioreactor [J].
Babcock, RW ;
Malda, J ;
Radway, JC .
JOURNAL OF APPLIED PHYCOLOGY, 2002, 14 (03) :169-184
[2]   Commercial production of microalgae: ponds, tanks, tubes and fermenters [J].
Borowitzka, MA .
JOURNAL OF BIOTECHNOLOGY, 1999, 70 (1-3) :313-321
[3]  
Boyd P.J., 1988, Methods in Bryology, P41
[4]   Hydrodynamic aspects and Arthrospira growth in two outdoor tubular undulating row photobioreactors [J].
Carlozzi, P .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 2000, 54 (01) :14-22
[5]  
Cove DJ, 1984, EXPT BIOL BRYOPHYTES, P177
[6]   Design of a photo-bioreactor for modelling purposes [J].
Csögör, Z ;
Herrenbauer, M ;
Perner, I ;
Schmidt, K ;
Posten, C .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1999, 38 (4-6) :517-523
[7]  
CSOGOR Z, 2000, THESIS SHAKER AACHEN
[8]   The moss bioreactor [J].
Decker, EL ;
Reski, R .
CURRENT OPINION IN PLANT BIOLOGY, 2004, 7 (02) :166-170
[9]   A novel airlift photobioreactor with baffles for improved light utilization through the flashing light effect [J].
Degen, J ;
Uebele, A ;
Retze, A ;
Schmid-Staiger, U ;
Trösch, W .
JOURNAL OF BIOTECHNOLOGY, 2001, 92 (02) :89-94
[10]  
GERBSCH N, 1997, THESIS TU BERLIN