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The impact of pH control on the volumetric productivity of mixed culture PHA production from fermented molasses

机译:pH控制对发酵糖蜜生产混合培养PHA的容积生产力的影响

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Polyhydroxyalkanoate (PHA) production via mixed microbial cultures (MMCs) can potentially decrease process operational costs as compared to conventional pure culture techniques. However, the volumetric productivity of PHA by MMCs must be augmented to increase its cost competitiveness. For this purpose, a three-stage bioreactor system was operated in this study, with (i) anaerobic fermentation of molasses, (ii) culture selection, and (iii) PHA accumulation and harvesting stages. In stage2, bioreactor operation with pH control at 8 led to twice the biomass concentration (up to 8 g VSS L-1, where VSS is the volatile suspended solids) as compared to operation without pH control (maximum pH 9). No loss in the specific PHA storage efficiency was observed (PHA content up to 57.5% and PHA storage rate up to 0.27 Cmol PHA Cmol X-1 h(-1), where X is the active biomass), thereby resulting in twice the volumetric PHA production rate. The limited biomass growth at the higher pH level was not due to nutrient limitation, but likely to a shift in the microbial community. It is hypothesized that the increased enrichment of Azoarcus at pH 8 led to higher PHA productivity. pH control in the culture selection stage can lead to enhanced PHA production from MMCs, improving the viability of the process.
机译:与传统的纯培养技术相比,通过混合微生物培养(MMC)生产聚羟基链烷酸酯(PHA)可以潜在地降低过程运营成本。但是,MMC必须提高PHA的体积生产率,以提高其成本竞争力。为此目的,在该研究中操作了三阶段生物反应器系统,其中(i)糖蜜的厌氧发酵,(ii)培养选择,以及(iii)PHA积累和收获阶段。在阶段2中,与没有pH控制(最大pH 9)相比,将pH控制在8的生物反应器操作导致生物质浓度的两倍(高达8 g VSS L-1,其中VSS是挥发性悬浮固体)。没有观察到特定PHA储存效率的损失(PHA含量最高为57.5%,PHA储存速率最高为0.27 Cmol PHA Cmol X-1 h(-1),其中X是活性生物质),从而导致两倍的体积PHA生产率。在较高pH值下有限的生物量生长不是由于营养限制,而是可能导致微生物群落的转移。据推测,在pH 8时,偶氮菌的富集度增加导致PHA生产率提高。在培养物选择阶段控制pH值可以提高MMC产生PHA的产量,从而提高工艺的可行性。

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