Please wait a minute...
J4  2010, Vol. 44 Issue (2): 320-325    DOI: 10.3785/j.issn.1008-973X.2010.02.020
化学工程﹑环境工程     
外循环气升式生物反应器中酯酶生产及应用
沈雪亮1, 范永仙2, 汪钊1
(1. 浙江工业大学 生物与环境工程学院,浙江 杭州 310014; 2. 浙江工业大学 化学工程与材料学院,浙江 杭州 310014)
Esterase fermentation in an external-loop airlift bioreactor and its application in D-lactic acid production
SHEN Xue-liang1, FAN Yong-Xian2, WANG Zhao1
(1. College of Biological and Environmental Engineering, Zhejiang University of Technology, Hangzhou 310014, China;
2. College of Chemical Engineering and Materials Science, Zhejiang University of Technology, Hangzhou 310014, China)
 全文: PDF  HTML
摘要:

采用海藻酸钙凝胶包埋法固定根霉(Rhizopus sp. F-16)细胞,在外循环气升式生物反应器(工作体积为10 L,高径比为2.9)中发酵生产酯酶.与游离细胞发酵相比,固定化细胞具有发酵时间短、产酶活力高等优点,其最适通气量为0.70 m3/h,最适装液量为8.75 L,发酵48 h时酯酶活力达41.6 U/g细胞.固定化细胞的适宜作用pH为8.0~9.0,适宜作用温度为45~50 ℃,其酸碱稳定性和热稳定性均比游离细胞明显增强.该固定化细胞可直接用于选择性水解外消旋乳酸乙酯生成D-乳酸,当底物的质量浓度为150 g/L,反应时间为3 h时乳酸乙酯的水解率达43.9%,D-乳酸的光学纯度达95.7%.固定化细胞性状稳定,可重复利用,连续降解6批乳酸乙酯的平均水解率为43.3%,D-乳酸的光学纯度平均为95.4%.

Abstract:

The cells of Rhizopus sp. F-16 were immobilized by being entrapped into calcium alginate gels. The immobilized cells were cultivated in an external-loop airlift bioreactor (working volume 10 L and height-to-diameter ratio 2.9) for the production of esterase. The fermentation term of immobilized cells was shortened and the activity of esterase was improved compared with free cells. The optimum air flow rate and liquid volume for the fermentation of immobilized cells were 0.70 m3/h and 8.75 L, respectively. The esterase activity reached 41.6 U/g cell after 48 h fermentation. The suitable reaction pH value and the temperature of immobilized cells were 8.0~9.0 and 45~50 ℃, respectively. The acidic and alkali stability and the thermal stability of immobilized cells were both enhanced than free cells. The immobilized cells can hydrolyze racemic ethyl lactate enantioselectively to produce D-lactic acid. When the substrate mass concentration was 150 g/L, the hydrolysis yield of ethyl lactate was 43.9% and the optical purity of D-lactic acid reached 95.7% after 3 h reaction. The immobilized cells were quite stable and can be repeatedly used for at least 6 batches of resolution reaction. The average hydrolysis yield of ethyl lactate was 43.3%, and the average optical purity of D-lactic acid was 95.4%.

出版日期: 2010-03-09
:  TQ 925  
通讯作者: 汪钊,男,教授.     E-mail: hzwangzhao@163.com
作者简介: 沈雪亮(1977—),女,浙江杭州人,副教授,从事生物工程研究.
服务  
把本文推荐给朋友
加入引用管理器
E-mail Alert
RSS
作者相关文章  

引用本文:

沈雪亮, 范永仙, 汪钊. 外循环气升式生物反应器中酯酶生产及应用[J]. J4, 2010, 44(2): 320-325.

CHEN Xue-Liang, FAN Yong-Xian, HONG Zhao. Esterase fermentation in an external-loop airlift bioreactor and its application in D-lactic acid production. J4, 2010, 44(2): 320-325.

链接本文:

http://www.zjujournals.com/eng/CN/10.3785/j.issn.1008-973X.2010.02.020        http://www.zjujournals.com/eng/CN/Y2010/V44/I2/320

[1]  NORDGRON P, HANG Y D. Purification and characterization of acetyl esterase from Candida guilliermondii[J]. Letters in Applied Microbiology, 2000, 30 (2): 167171.
[2] 施安辉,周波.酯酶的微生物类群、酯化特性及其应用前景[J].中国酿造,2002 (6): 1416.
SHI An-hui, ZHOU Bo. Study on the esterase-producing microflora, esterifying characteristic and application of esterase [J]. China Brewing, 2002(6): 1416.
[3] 皮雄娥,汪钊.微生物酯酶拆分生物素手性中间体的初步研究[J].微生物学通报,2004,31(4):2325.
PI Xiong-e, WANG Zhao. Studies on optical resolution of DL-biotin intermediate by fungal esterase [J]. Microbiology, 2004, 31(4): 2325.
[4] GAVRILESCU M, TUDOSE R Z. Hydrodynamics of non-Newtonian liquids in external-loop airlift bioreactors, part 2: study of the liquid circulation velocity [J]. Bioprocess and Biosystems Engineering, 1998, 18(2): 8389.
[5] AL-QODAH Z, LSFI W. Modeling of antibiotics production in magneto three-phase airlift fermenter [J]. Biochemical Engineering Journal, 2001, 7(1): 716.
[6] XIE D, LIU D, LIU T. Modeling of glycerol production by fermentation in different reactor states [J]. Process Biochemistry, 2001, 36(12): 12251232.
[7] ZHEN Y, WANG Z, CHEN X. α-Amylase production by Bacillus subtilis with dregs in an external-loop airlift bioreactor [J]. Biochemical Engineering Journal, 2000, 5(2): 115121.
[8] ZHEN Y, WANG Z, CHEN X, ZHANG C. Production of extracellular protease from crude substrates with dregs in an external-loop airlift bioreactor with lower ratio of height to diameter [J]. Biotechnology Progress, 2001, 17(2): 273277.
[9] ZHEN Y, CHEN X, WANG Z, et al. Production of validamycins from crude substrates by Streptomyces hygroscopicus in an external-loop airlift bioreactor with a low height-to-diameter ratio [J]. Chinese Journal of Chemical Engineering, 2004, 12(1): 102107.
[10] 金其荣,金丰秋.乳酸衍生物发展应用新动向[J].山西食品工业,2002(3): 27.
JIN Qi-rong, JIN Feng-qiu. New development and application of lactic acid ramification [J]. Shanxi Food Industries,2002(3): 27.
[11] 黄量,戴立信.手性药物的化学与生物学 [M]. 北京: 化学工业出版社, 2002: 204205.
[12] ZHOU S, CAUSEY T B, HASONA A, et al. Production of optically pure D-lactic acid in mineral salts medium by metabolically engineered Escherichia coli W3110 [J]. Applied and Environmental Microbiology, 2003, 69(1): 399407.
[13] TSUJI H, FUKUI I. Enhanced thermal stability of poly(lactide)s in the melt by enantiomeric polymer blending [J]. Polymer,2003,44(10): 28912896.
[14] FUKUSHIMA K, SOGO K, MIURA S, et al. Production of D-lactic acid by bacterial fermentation of rice starch [J]. Macromolecular Bioscience, 2004, 4(11): 10211027.
[15] ISHIDA N, SUZUKI T, TOKUHIRO K, et al. D-lactic acid production by metabolically engineered Saccharomyces cerevisiae[J]. Journal of Bioscience and Bioengineering, 2006, 101(2): 172177.
[16] YANEZ R, ALONSO J L, PARAJO J C. D-Lactic acid production from waste cardboard [J]. Journal of Chemical Technology and Biotechnology. 2005, 80(1): 7684.
[17] TANAKA T, HOSHINA M, TANABE S, et al. Production of D-lactic acid from defatted rice bran by simultaneous saccharification and fermentation [J]. Bioresource Technology, 2006, 97(2): 211217.
[18] 丁子建,柏中中,孙志浩,等.芽孢乳杆菌发酵葡萄糖制备D-乳酸的研究[J].生物加工过程,2004, 2(3): 3036.
DING Zi-Jian, BO Zhong-zhong, SUN Zhi-hao, et al. Study on fermentative production of D()-lactic acid from glucose by Sporolactobacillus sp. [J]. Chinese Journal of Bioprocess Engineering, 2004, 2(3): 3036.
[19] VEERANAGAVAN K. A simple and sensitive method for the estimation of microbial lipase activity [J]. Analytical Biochemistry. 1990, 186(2): 301305.
[20] 张龙翔. 生化实验方法和技术[M].北京:人民教育出版社,1986: 911.

No related articles found!