Characterization of oxygen transfer conditions and their effects on Phaffia rhodozyma growth and carotenoid production in shake-flask cultures

被引:101
作者
Liu, YS [1 ]
Wu, HY [1 ]
Ho, KP [1 ]
机构
[1] Hong Kong Polytech Univ, Dept Appl Biol & Chem Technol, Kowloon, Hong Kong, Peoples R China
关键词
Phaffia rhodozyma; shake-flask culture; oxygen transfer; dissolved oxygen; yeast growth; carotenoid production;
D O I
10.1016/j.bej.2005.08.031
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
This study characterizes the effects of oxygen transfer on the growth and carotenoid (astaxanthin) production of the red yeast Phaffia rhodozyma in liquid cultures. The yeast culture on a liquid medium at 20 degrees C had a critical dissolved oxygen (DO) concentration of 10% air-saturation (0.8 mg/L) and a maximum specific oxygen uptake rate of 60 mg O-2/g cell h. In 250-mL shake-flasks with 50 ml liquid medium, poor oxygen transfer resulted in constantly lower DO level than the critical DO in the culture. Both the biomass and carotenoid yields increased with the decrease in liquid volume in flasks and the increase in shaker speed, e.g., 8.0 g dw/L biomass and 7.4 mg/L carotenoid with 50 mL liquid at 200 rpm versus 10.7 g dw/L biomass and 15.5 mg/L carotenoid with 20 mL liquid at 250 rpm. The oxygen transfer coefficient (K(L)a) was correlated to shaker speed (N) and liquid volume (V-L) by K(L)a = 0.141N(0.88) (V-L/V-o)(-0.80) based on linear regression of experimental data (R-2 = 0.997, V-o = flask volume). The carotenoid yield showed a strong linear correlation with the oxygen transfer rate (R-2 = 0.989). These results show that oxygen supply is crucial for carotenoid production in R rhodozyma liquid cultures. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:331 / 335
页数:5
相关论文
共 15 条
[1]   CAROTENOIDS OF PHAFFIA-RHODOZYMA, A RED-PIGMENTED FERMENTING YEAST [J].
ANDREWES, AG ;
PHAFF, HJ ;
STARR, MP .
PHYTOCHEMISTRY, 1976, 15 (06) :1003-1007
[2]   OXYGEN ABSORPTION RATES IN SHAKEN FLASKS [J].
AURO, MA ;
HODGE, HM ;
ROTH, NG .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1957, 49 (08) :1237-1238
[3]  
Johnson E A, 1996, Adv Biochem Eng Biotechnol, V53, P119
[4]  
Kanokwaree K, 1997, BIOTECHNOL BIOENG, V55, P520, DOI 10.1002/(SICI)1097-0290(19970805)55:3&lt
[5]  
520::AID-BIT8&gt
[6]  
3.0.CO
[7]  
2-E
[8]   DIFFERENT SHAKE FLASK CLOSURES ALTER GAS-PHASE COMPOSITION AND AJMALICINE PRODUCTION IN CATHARANTHUS-ROSEUS CELL-SUSPENSIONS [J].
LEE, CWT ;
SHULER, ML .
BIOTECHNOLOGY TECHNIQUES, 1991, 5 (03) :173-178
[9]   CHEMICAL-ENGINEERING USE OF CATALYZED SULFITE OXIDATION-KINETICS FOR THE DETERMINATION OF MASS-TRANSFER CHARACTERISTICS OF GAS-LIQUID CONTACTORS [J].
LINEK, V ;
VACEK, V .
CHEMICAL ENGINEERING SCIENCE, 1981, 36 (11) :1747-1768
[10]   Advances in understanding and modeling the gas-liquid mass transfer in shake flasks [J].
Maier, U ;
Losen, M ;
Büchs, J .
BIOCHEMICAL ENGINEERING JOURNAL, 2004, 17 (03) :155-167