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嗜氢假单胞菌利用乳清生产聚羟基脂肪酸酯

Polyhydroxyalkanoate production from whey by Pseudomonas hydrogenovora.

作者信息

Koller Martin, Bona Rodolfo, Chiellini Emo, Fernandes Elizabeth Grillo, Horvat Predrag, Kutschera Christoph, Hesse Paula, Braunegg Gerhart

机构信息

Institute of Biotechnology and Biochemical Engineering, Graz University of Technology, Petersgasse 12, A-8010 Graz, Austria.

出版信息

Bioresour Technol. 2008 Jul;99(11):4854-63. doi: 10.1016/j.biortech.2007.09.049. Epub 2007 Nov 28.

Abstract

Whey permeate from dairy industry was hydrolyzed enzymatically to cleave its main carbon source, lactose, to glucose and galactose. The hydrolysis products were chosen as carbon sources for the production of poly-3-hydroxybutyric acid (PHB) by Pseudomonas hydrogenovora. In shaking flask experiments, the utilization of whey permeate as a cheap substrate was compared to the utilization of pure glucose and galactose for bacterial growth under balanced conditions as well as for the production of PHB under nitrogen limitation. After determination of the inhibition constant Ki for sodium valerate on biomass production (Ki=1.84 g/l), the biosynthesis of PHA co-polyesters containing 3-hydroxybutyrate (3HB) and 3-hydroxyvalerate (3HV) units from hydrolyzed whey permeate and valerate was investigated. The application of hydrolyzed whey permeate turned out to be advantageous compared with the utilization of pure sugars. Therefore, fermentation under controlled conditions in a bioreactor was performed with hydrolyzed whey permeate to obtain detailed kinetic data (maximum specific growth rate, mu max=0.291/h, maximum polymer concentration, 1.27 g/l PHB), values for molecular mass distribution (weight average molecular weight Mw=353.5 kDa, polydispersity index PDI=3.8) and thermo analytical data. The fermentation was repeated with co-feeding of valerate (maximum specific growth rate, mu(max)=0.201/h, maximum polymer concentration, 1.44 g/l poly-(3HB-co-21%-3HV), weight average molecular weight M(w)=299.2 kDa, polydispersity index PDI=4.3).

摘要

对乳制品工业中的乳清渗透液进行酶水解,以将其主要碳源乳糖分解为葡萄糖和半乳糖。选择水解产物作为嗜氢假单胞菌生产聚-3-羟基丁酸酯(PHB)的碳源。在摇瓶实验中,比较了在平衡条件下乳清渗透液作为廉价底物用于细菌生长以及在氮限制条件下用于生产PHB时,与纯葡萄糖和半乳糖的利用情况。在测定戊酸钠对生物量生产的抑制常数Ki(Ki = 1.84 g/l)后,研究了由水解乳清渗透液和戊酸酯生物合成含3-羟基丁酸酯(3HB)和3-羟基戊酸酯(3HV)单元的PHA共聚酯。结果表明,与使用纯糖相比,应用水解乳清渗透液具有优势。因此,在生物反应器中在受控条件下用水解乳清渗透液进行发酵,以获得详细的动力学数据(最大比生长速率,μm max = 0.291/h,最大聚合物浓度,1.27 g/l PHB)、分子量分布值(重均分子量Mw = 353.5 kDa,多分散指数PDI = 3.8)和热分析数据。用戊酸酯共进料重复发酵(最大比生长速率,μ(max)=0.201/h,最大聚合物浓度,1.44 g/l聚(3HB-co-21%-3HV),重均分子量M(w)=299.2 kDa,多分散指数PDI = 4.3)。

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