CRETUS Institute, Department of Chemical Engineering, Universidade de Santiago de Compostela, 15782, Santiago de Compostela, Galicia, Spain.
CRETUS Institute, Department of Chemical Engineering, Universidade de Santiago de Compostela, 15782, Santiago de Compostela, Galicia, Spain.
J Environ Manage. 2022 Sep 1;317:115433. doi: 10.1016/j.jenvman.2022.115433. Epub 2022 Jun 9.
Medium- and long-chain fatty acids and glycerol contained in the oily fraction of many food-industry effluents are excellent candidates to produce biobased high-value triacylglycerides (TAGs) and polyhydroxyalkanoates (PHAs). The typical process configuration for TAGs recovery from lipid-rich streams always includes two steps (culture enrichment plus storage compounds accumulation) whereas, for PHAs production, an additional pretreatment of the substrate for the obtainment of soluble volatile fatty acids (VFAs) is required. To simplify the process, substrate hydrolysis, culture enrichment, and accumulation (TAG and PHA storage) were coupled here in a single sequencing batch reactor (SBR) operated under the double growth limitation strategy (DGL) and fed in pulses with industrial waste fish oil during the whole feast phase. When the SBR was operated in 12 h cycles, it was reached up to 51 wt % biopolymers after only 6 h of feast (TAG:PHA ratio of 50:51; 0.423 Cmmol/Cmmol). Daily storage compound production was observed to be over 25% higher than the reached when enrichment and accumulation stages were carried in separate operational units. Increasing the feast phase length from 6 to 12 h (18 h cycle) negatively affected the DGL strategy performance and hence system storage capacity, which was recovered after also extending the famine phase in the same proportion (24 h cycle). Besides, the carbon influx during the feast phase was identified as a key operational parameter controlling storage compounds production and, together with the C/N ratio, culture selection. The different cycle configurations tested clearly modulated the total fungal abundances without no significant differences in the size of the bacterial populations. Several PHA and TAG producers were found in the mixed culture although the PHA and TAG productions were poorly associated with the increased relative abundances (RAs) of specific operational taxonomic units (OTUs).
许多食品工业废水中油性部分所含的中链和长链脂肪酸以及甘油是生产生物基高附加值三酰基甘油(TAG)和聚羟基烷酸(PHA)的绝佳候选物。从富含脂质的料流中回收 TAG 的典型工艺配置通常包括两个步骤(培养富集加储存化合物积累),而对于 PHA 的生产,则需要对底物进行额外的预处理,以获得可溶挥发性脂肪酸(VFAs)。为了简化工艺,本文在单个序批式反应器(SBR)中耦合了底物水解、培养富集和积累(TAG 和 PHA 储存),该 SBR 采用双生长限制策略(DGL)运行,并在整个饱食阶段以脉冲方式用工业废鱼油进料。当 SBR 在 12 h 周期运行时,仅在饱食 6 h 后即可达到 51 wt%的生物聚合物(TAG:PHA 比为 50:51;0.423 Cmmol/Cmmol)。与在单独的操作单元中进行富集和积累阶段相比,每天观察到储存化合物的产量增加了 25%以上。将饱食阶段的长度从 6 小时增加到 12 小时(18 h 周期)会对 DGL 策略的性能产生负面影响,从而降低系统的储存能力,这可以通过同样比例地延长饥饿阶段来恢复(24 h 周期)。此外,饱食阶段的碳流入被确定为控制储存化合物生产的关键操作参数,与 C/N 比一起,还控制了培养物的选择。测试的不同周期配置明显调节了总真菌丰度,而细菌种群的大小没有明显差异。尽管 PHA 和 TAG 的产量与特定操作分类单元(OTU)的相对丰度(RA)增加相关性较差,但在混合培养物中发现了几种 PHA 和 TAG 生产者。