Department of Chemistry, Sapienza University of Rome, P.le Aldo Moro 5, 00185 Rome, Italy.
Department of Chemistry, Sapienza University of Rome, P.le Aldo Moro 5, 00185 Rome, Italy.
N Biotechnol. 2014 Jun 25;31(4):289-96. doi: 10.1016/j.nbt.2013.08.001. Epub 2013 Aug 14.
Polyhydroxyalkanoates (PHA) production with mixed microbial cultures (MMC) has been investigated by means of a sequential process involving three different stages, consisting of a lab-scale sequencing batch reactor for MMC selection, a PHA accumulation reactor and a polymer extraction reactor. All stages were performed under continuous operation for at least 4 months to check the overall process robustness as well as the related variability of polymer composition and properties. By operating both biological stages at high organic loads (8.5 and 29.1 gCOD/Ld, respectively) with a synthetic mixture of acetic and propionic acid, it was possible to continuously produce PHA at 1.43 g/Ld with stable performance (overall, the storage yield was 0.18 COD/COD). To identify the optimal operating conditions of the extraction reactor, two digestion solutions have been tested, NaOH (1m) and NaClO (5% active Cl2). The latter resulted in the best performance both in terms of yield of polymer recovery (around 100%, w/w) and purity (more than 90% of PHA content in the residual solids, on a weight basis). In spite of the stable operating conditions and performance, a large variation was observed for the HV content, ranging between 4 and 20 (%, w/w) for daily samples after accumulation and between 9 and 13 (%, w/w) for weekly average samples after extraction and lyophilization. The molecular weight of the produced polymer ranged between 3.4 × 10(5) and 5.4 × 10(5)g/mol with a large polydispersity index. By contrast, TGA and DSC analysis showed that the thermal polymer behavior did not substantially change over time, although it was strongly affected by the extraction agent used (NaClO or NaOH).
混合微生物培养物(MMC)的聚羟基烷酸酯(PHA)生产已通过涉及三个不同阶段的顺序过程进行了研究,该过程包括用于 MMC 选择的实验室规模的序列批式反应器、PHA 积累反应器和聚合物提取反应器。所有阶段均在连续操作下进行了至少 4 个月,以检查整个过程的稳健性以及聚合物组成和性能的相关变化。通过在高有机负荷(分别为 8.5 和 29.1 gCOD/Ld)下操作两个生物阶段,并使用乙酸和丙酸的合成混合物,可以以 1.43 g/Ld 的稳定性能连续生产 PHA(总体而言,储存产率为 0.18 COD/COD)。为了确定提取反应器的最佳操作条件,已经测试了两种消化溶液,NaOH(1m)和 NaClO(5%有效 Cl2)。后者在聚合物回收产率(约 100%,w/w)和纯度(残留固体中 PHA 含量超过 90%,按重量计)方面均表现出最佳性能。尽管操作条件和性能稳定,但 HV 含量仍存在很大差异,积累后每天的样品含量在 4%至 20%(w/w)之间,提取和冻干后每周平均样品含量在 9%至 13%(w/w)之间。所生产的聚合物的分子量在 3.4×10(5)至 5.4×10(5)g/mol 之间,具有较大的多分散指数。相比之下,TGA 和 DSC 分析表明,尽管受所用提取剂(NaClO 或 NaOH)的强烈影响,但聚合物的热行为并未随时间发生实质性变化。