Page W J, Manchak J, Rudy B
Department of Microbiology, University of Alberta, Edmonton, Canada.
Appl Environ Microbiol. 1992 Sep;58(9):2866-73. doi: 10.1128/aem.58.9.2866-2873.1992.
Azotobacter vinelandii UWD formed polyhydroxyalkanoate (PHA) copolymers containing beta-hydroxybutyrate and beta-hydroxyvalerate (HV) when grown in a medium containing glucose as the primary C source and valerate (pentanoate) as a precursor. Copolymer was not formed when propionate was added to the glucose medium but was formed when heptanoate, nonanoate, or trans-2-pentenoate was present. Optimal levels of HV were formed when valerate was added at the time of maximum PHA synthesis, although HV incorporation was not dependent on glucose catabolism. HV content in the polymer was increased from 17 to 24 mol% by adding 10 to 40 mM valerate to glucose medium, but HV insertion into the polymer occurred at a fixed rate. Similarly, the addition of valerate to a fed-batch culture of strain UWD in beet molasses in a fermentor produced 19 to 22 g of polymer per liter, containing 8.5 to 23 mol% HV after 38 to 40 h. The synthesis of HV in these cultures also occurred at a fixed rate (2.3 to 2.8 mol% h-1), while the maximum PHA production rate was 1.1 g liter-1 h-1. During synthesis of copolymer in batch or fed-batch culture, the yield from conversion of glucose into PHA (YP/S) remained at maximum theoretical efficiency (greater than or equal to 0.33 g of PHA per g of glucose consumed). Up to 45 mol% C source, but the PHA produced amounted to less than 1 g/liter. The combination of 30 mM valerate as a sole C source and 0.5 mM 4-pentenoate increased the HV content in the polymer to 52 mol%.(ABSTRACT TRUNCATED AT 250 WORDS)
棕色固氮菌UWD在以葡萄糖作为主要碳源和戊酸(戊酸盐)作为前体的培养基中生长时,会形成含有β-羟基丁酸酯和β-羟基戊酸酯(HV)的聚羟基脂肪酸酯(PHA)共聚物。当向葡萄糖培养基中添加丙酸时,不会形成共聚物,但当存在庚酸、壬酸或反式-2-戊烯酸时会形成共聚物。当在PHA合成达到最大值时添加戊酸,会形成最佳水平的HV,尽管HV的掺入不依赖于葡萄糖分解代谢。通过向葡萄糖培养基中添加10至40 mM戊酸,聚合物中的HV含量从17 mol%增加到24 mol%,但HV插入聚合物的速率是固定的。同样,在发酵罐中向甜菜糖蜜中的UWD菌株补料分批培养物中添加戊酸,38至40小时后每升产生19至22克聚合物,含有8.5至23 mol%的HV。这些培养物中HV的合成也以固定速率(2.3至2.8 mol% h-1)发生,而最大PHA生产率为1.1 g liter-1 h-1。在分批或补料分批培养共聚物的合成过程中,葡萄糖转化为PHA的产率(YP/S)保持在最大理论效率(每消耗1克葡萄糖产生大于或等于0.33克PHA)。高达45 mol%的碳源,但产生的PHA量小于1克/升。30 mM戊酸作为唯一碳源与0.5 mM 4-戊烯酸的组合将聚合物中的HV含量提高到52 mol%。(摘要截断于250字)