首页> 外文期刊>Applied biochemistry and biotechnology, Part A. enzyme engineering and biotechnology >Synthesis of polyhydroxyalkanoate (PHA) from excess activated sludge under various oxidation-reduction potentials (ORP) by using acetate and propionate as carbon sources.
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Synthesis of polyhydroxyalkanoate (PHA) from excess activated sludge under various oxidation-reduction potentials (ORP) by using acetate and propionate as carbon sources.

机译:以乙酸盐和丙酸盐为碳源,在各种氧化还原电位(ORP)下,由过量的活性污泥合成聚羟基链烷酸酯(PHA)。

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Accumulation of poly hydroxyalkanoate (PHA) from excess activated sludge (EAS) was monitored and controlled via the oxidation-reduction potential (ORP) adjusting process. The ORP was adjusted and controlled by only regulating the gas-flow rate pumped into the cultural broth in which sodium acetate (C2) and propionate (C3) were used as carbon sources. Productivity of PHA and the PHA compositions at various C2 to C3 ratios were also investigated. When ORP was maintained at +30 mV, 35% (w/w) of PHA of cell dry weight obtained when C2 was used as sole carbon source. The PHA copolymer, poly-(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV), accumulated by EAS with different 3-hydroxyvalarate (3HV) molar fractions ranged from 8% to 78.0% when C2 and C3 was used as sole carbon source, By using ORP to monitor and control the fermentation process instead DO meter, the ORP system provided more precise control to the PHA accumulation process from EAS under low dissolved oxygen (DO) concentrations. Adjusting the C2 to C3 ratios in the media could control the composition such as the 3HV/3HB ratios of the PHBV. Furthermore, it might be an effective way to adjust the 3HV molar fractions in PHBV by controlling the DO concentration via the ORP monitoring system. The 3HV molar fractions in the PHBV declined with increasing ORP from -30 mV to +100 mV by adjusting the gas-flow rate (i.e. the DO concentration). It is concluded that the DO plays a very important role in the synthesis of 3HV subunits in PHBV co-polymer from the EAS. Therefore, a hypothetic metabolic model for PHA synthesis from EAS was proposed to try to explain the results in this study.
机译:通过氧化还原电位(ORP)调节过程来监控过量的活性污泥(EAS)中聚羟基链烷酸酯(PHA)的积累。通过仅调节泵送至使用乙酸钠(C2)和丙酸酯(C3)作为碳源的培养液中的气体流速来调节和控制ORP。还研究了在各种C2与C3比率下PHA和PHA组合物的生产率。当ORP维持在+30 mV时,当C2用作唯一碳源时,可获得35%(w / w)的细胞干重的PHA。当C2和C3用作唯一碳时,EAS具有不同的3-羟基戊酸(3HV)摩尔分数的PHA共聚物聚(3-羟基丁酸酯-co-3-羟基戊酸酯)(PHBV)范围从8%到78.0%来源,通过使用ORP监测和控制发酵过程而不是DO计,ORP系统在低溶解氧(DO)浓度下从EAS提供了对PHA积累过程的更精确控制。调节介质中C2与C3的比例可以控制成分,例如PHBV的3HV / 3HB比例。此外,通过ORP监测系统控制DO的浓度可能是调节PHBV中3HV摩尔分数的有效方法。通过调节气体流速(即DO浓度),PHBV中的3HV摩尔分数随ORP从-30 mV增加到+100 mV而下降。结论是,DO在EAS的PHBV共聚物中合成3HV亚基中起着非常重要的作用。因此,提出了一种由EAS合成PHA的假设代谢模型,以试图解释本研究的结果。

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