Faculty of Engineering and Architecture, Kore University of Enna, Cittadella Universitaria, Enna, Italy.
Faculty of Engineering and Architecture, Kore University of Enna, Cittadella Universitaria, Enna, Italy.
Sci Total Environ. 2020 Feb 10;703:135508. doi: 10.1016/j.scitotenv.2019.135508. Epub 2019 Nov 16.
Residues from production of olive oil are generated yearly in great amounts, both in liquid and solid forms. Different waste treatment systems were proposed in literature, to minimize environmental pollution while raising the energy recovery. Anaerobic digestion is one of the available routes to recover energy from waste via production of biogas while reducing organic load and pollutants to the environment. The use of farming and agro industrial wastes as co-substrate in anaerobic digestion can induce benefits related to the simultaneous treatment of different wastes. In particular, co-digestion can significantly enhance the process stability as well as the bio-methane generation. This work aims at reviewing the latest achievements in anaerobic digestion of olive mill residues, focusing on the aspects that can mostly favor the process, principally from a technical but also from an economical point of view. For the mono-digestion processes, methane yields up to 419 L kg were reported for olive mill wastewaters (Calabrò et al. 2018), while a production of 740 L kg was achieved when digesting olive mill solid waste together with olive mill wastewater and milk whey (Battista et al. 2015). An increase up to 143% in the methane yield was also reported when the feedstock was subjected to a 5 days aeration before digesting it in a semi-continuous stirred tank reactor (González-González and Cuadros 2015).
橄榄油生产过程中会产生大量的液体和固体残渣。文献中提出了不同的废物处理系统,以尽量减少环境污染,同时提高能源回收。厌氧消化是通过生产沼气从废物中回收能源的一种方法,同时减少有机负荷和污染物对环境的影响。将农业和农业工业废物作为共底物用于厌氧消化可以诱导与同时处理不同废物相关的好处。特别是,共消化可以显著提高过程稳定性和生物甲烷的生成。这项工作旨在回顾橄榄油厂废物的厌氧消化的最新成果,重点关注最有利于该过程的方面,主要从技术角度,同时也从经济角度来看。对于单消化过程,据报道,橄榄油厂废水的甲烷产率高达 419 L kg(Calabrò 等人,2018 年),而当将橄榄油厂固体废物与橄榄油厂废水和乳清一起消化时,产率达到 740 L kg(Battista 等人,2015 年)。当原料在半连续搅拌槽式反应器中消化前先进行 5 天曝气时,甲烷产率也增加了 143%(González-González 和 Cuadros 2015 年)。