Nzeteu Corine Orline, Trego Anna Christine, Abram Florence, O'Flaherty Vincent
1Microbial Ecology Laboratory, Microbiology, School of Natural Sciences and Ryan Institute, National University of Ireland (NUI), Galway, Ireland.
2Microbial Communities Lab, Microbiology, School of Natural Sciences, National University of Ireland (NUI), Galway, Ireland.
Biotechnol Biofuels. 2018 Apr 11;11:108. doi: 10.1186/s13068-018-1101-4. eCollection 2018.
Nowadays, the vast majority of chemicals are either synthesised from fossil fuels or are extracted from agricultural commodities. However, these production approaches are not environmentally and economically sustainable, as they result in the emission of greenhouse gases and they may also compete with food production. Because of the global agreement to reduce greenhouse gas emissions, there is an urgent interest in developing alternative sustainable sources of chemicals. In recent years, organic waste streams have been investigated as attractive and sustainable feedstock alternatives. In particular, attention has recently focused on the production of caproate from mixed culture fermentation of low-grade organic residues. The current approaches for caproate synthesis from organic waste are not economically attractive, as they involve the use of two-stage anaerobic digestion systems and the supplementation of external electron donors, both of which increase its production costs. This study investigates the feasibility of producing caproate from food waste (FW) without the supplementation of external electron donors using a single-phase reactor system.
Replicate leach-bed reactors were operated on a semi-continuous mode at organic loading of 80 g VS FW l and at solid retention times of 14 and 7 days. Fermentation, rather than hydrolysis, was the limiting step for caproate production. A higher caproate production yield 21.86 ± 0.57 g COD l was achieved by diluting the inoculating leachate at the beginning of each run and by applying a leachate recirculation regime. The mixed culture batch fermentation of the FW leachate was able to generate 23 g caproate COD l (10 g caproate l), at a maximum rate of 3 g caproate l day under high H pressure. Lactate served as the electron donor and carbon source for the synthesis of caproate. Microbial community analysis suggested that neither nor which are well-characterised caproate producers in bioreactors systems, were strongly implicated in the synthesis of caproate, but that rather sp. with 99% similarity to and sp likely played key roles in the synthesis of caproate. This finding indicates that the microbial community capable of caproate synthesis could be diverse and may therefore help in maintaining a stable and robust process.
These results indicate that future, full-scale, high-rate caproate production from carbohydrate-rich wastes, associated with biogas recovery, could be envisaged.
如今,绝大多数化学品要么由化石燃料合成,要么从农产品中提取。然而,这些生产方式在环境和经济方面都不可持续,因为它们会导致温室气体排放,还可能与粮食生产产生竞争。由于全球达成了减少温室气体排放的协议,因此迫切需要开发替代的可持续化学品来源。近年来,有机废物流已被研究作为有吸引力且可持续的原料替代品。特别是,最近的注意力集中在从低品位有机残渣的混合培养发酵中生产己酸盐。目前从有机废物合成己酸盐的方法在经济上并不具有吸引力,因为它们涉及使用两级厌氧消化系统和补充外部电子供体,这两者都会增加生产成本。本研究调查了使用单相反应器系统在不补充外部电子供体的情况下从食物垃圾(FW)生产己酸盐的可行性。
重复的渗滤床反应器以半连续模式运行,有机负荷为80 g VS FW l,固体停留时间为14天和7天。发酵而非水解是己酸盐生产的限制步骤。通过在每次运行开始时稀释接种渗滤液并采用渗滤液循环方式,实现了更高的己酸盐产率,即21.86±0.57 g COD l。FW渗滤液的混合培养分批发酵在高H压力下能够以3 g己酸盐l天的最大速率产生23 g己酸盐COD l(10 g己酸盐l)。乳酸用作合成己酸盐的电子供体和碳源。微生物群落分析表明,在生物反应器系统中已得到充分表征的己酸盐生产者 和 均未强烈参与己酸盐的合成,但与 具有99%相似性的 sp.和 sp.可能在己酸盐的合成中起关键作用。这一发现表明,能够合成己酸盐的微生物群落可能是多样的,因此可能有助于维持稳定且强劲的过程。
这些结果表明,未来可以设想从富含碳水化合物的废物中大规模、高速率地生产己酸盐,并回收沼气。