Ibrahim Mohammad H A, Steinbüchel Alexander
Institut für Molekulare Mikrobiologie und Biotechnologie, Westfälische Wilhelms-Universität Münster, D-48149 Münster, Germany.
Appl Environ Microbiol. 2009 Oct;75(19):6222-31. doi: 10.1128/AEM.01162-09. Epub 2009 Aug 7.
Industrial production of biodegradable polyesters such as polyhydroxyalkanoates is hampered by high production costs, among which the costs for substrates and for downstream processing represent the main obstacles. Inexpensive fermentable raw materials such as crude glycerol, an abundant by-product of the biodiesel industry, have emerged to be promising carbon sources for industrial fermentations. In this study, Zobellella denitrificans MW1, a recently isolated bacterium, was used for the production of poly(3-hydroxybutyrate) (PHB) from glycerol as the sole carbon source. Pilot-scale fermentations (42-liter scale) were conducted to scale up the high PHB accumulation capability of this strain. By fed-batch cultivation, at first a relatively high cell density (29.9 +/- 1.3 g/liter) was obtained during only a short fermentation period (24 h). However, the PHB content was relatively low (31.0% +/- 4.2% [wt/wt]). Afterwards, much higher concentrations of PHB (up to 54.3 +/- 7.9 g/liter) and higher cell densities (up to 81.2 +/- 2.5 g/liter) were obtained by further fed-batch optimization in the presence of 20 g/liter NaCl, with optimized feeding of glycerol and ammonia to support both cell growth and polymer accumulation over a period of 50 h. A high specific growth rate (0.422/h) and a short doubling time (1.64 h) were attained. The maximum PHB content obtained was 66.9% +/- 7.6% of cell dry weight, and the maximum polymer productivity and substrate yield coefficient were 1.09 +/- 0.16 g/liter/h and 0.25 +/- 0.04 g PHB/g glycerol, respectively. Furthermore, a simple organic solvent extraction process was employed for PHB recovery during downstream processing: self-flotation of cell debris after extraction of PHB with chloroform allowed a convenient separation of a clear PHB-solvent solution from the cells. Maximum PHB recovery (85.0% +/- 0.10% [wt/wt]) was reached after 72 h of extraction with chloroform at 30 degrees C, with a polymer purity of 98.3% +/- 1.3%.
聚羟基脂肪酸酯等可生物降解聚酯的工业生产受到高生产成本的阻碍,其中底物成本和下游加工成本是主要障碍。廉价的可发酵原料,如粗甘油(生物柴油行业的一种丰富副产品),已成为工业发酵中很有前景的碳源。在本研究中,最近分离出的反硝化佐贝氏菌MW1被用于以甘油作为唯一碳源生产聚(3-羟基丁酸酯)(PHB)。进行了中试规模发酵(42升规模)以扩大该菌株的高PHB积累能力。通过分批补料培养,首先在较短的发酵期(24小时)内获得了相对较高的细胞密度(29.9±1.3克/升)。然而,PHB含量相对较低(31.0%±4.2%[重量/重量])。之后,通过在20克/升氯化钠存在下进一步优化分批补料,优化甘油和氨的进料以支持细胞生长和聚合物积累50小时,获得了更高浓度的PHB(高达54.3±7.9克/升)和更高的细胞密度(高达81.2±2.5克/升)。获得了较高的比生长速率(0.422/小时)和较短的倍增时间(1.64小时)。获得的最大PHB含量为细胞干重的66.9%±7.6%,最大聚合物生产率和底物产率系数分别为1.09±0.16克/升/小时和0.25±0.04克PHB/克甘油。此外,在下游加工过程中采用了简单的有机溶剂萃取工艺来回收PHB:用氯仿萃取PHB后细胞碎片的自浮选使得能够方便地将澄清的PHB-溶剂溶液与细胞分离。在30℃下用氯仿萃取72小时后,PHB回收率达到最大值(85.0%±0.10%[重量/重量]),聚合物纯度为98.3%±1.3%。