International Science and Technology Cooperation Center for Urban Alternative Water Resources Development, Key Laboratory of Northwest Water Resource, Environment and Ecology, MOE, Engineering Technology Research Center for Wastewater Treatment and Reuse, Shaanxi, China; Key Laboratory of Environmental Engineering, Shaanxi, China; Xi'an University of Architecture and Technology, No. 13 Yanta Road, Xi'an 710055, China.
International Science and Technology Cooperation Center for Urban Alternative Water Resources Development, Key Laboratory of Northwest Water Resource, Environment and Ecology, MOE, Engineering Technology Research Center for Wastewater Treatment and Reuse, Shaanxi, China; Key Laboratory of Environmental Engineering, Shaanxi, China; Xi'an University of Architecture and Technology, No. 13 Yanta Road, Xi'an 710055, China.
Bioresour Technol. 2020 Jul;307:123195. doi: 10.1016/j.biortech.2020.123195. Epub 2020 Mar 17.
Food waste (FW) and cow manure (CM) were co-digested to achieve a stable and high-rate of methane production. The start-up conditions (substrate mixing (FW/CM) ratio, substrate to inoculum ratio, and initial pH) were optimised, and the optimised parameters were experimentally confirmed by batch operation under mesophilic temperatures. To further verify the effects of start-up conditions on the long-term co-digestion process, a semi-continuous dynamic membrane bioreactor was operated for over 300 days with an FW/CM ratio of 2.5. Following the optimised operation scheme, the organic loading rate gradually increased to 11.9 g COD/L/d. Thus, stable anaerobic co-digestion was maintained at FW/CM ratio of 2.5, and a high CH production of 2.71 L CH/L/d and CH yield of 441 mL CH/g VS was achieved. In the long-term operation, the digestate pH was stable at approximately 8.4, which indicated a very favourable anaerobic reaction condition without volatile fatty acid accumulation.
将食物垃圾 (FW) 和牛粪 (CM) 共消化以实现稳定且高速的甲烷生产。优化了启动条件(底物混合 (FW/CM) 比、底物与接种物比和初始 pH 值),并通过中温批式运行实验验证了优化参数。为了进一步验证启动条件对长期共消化过程的影响,使用 FW/CM 比为 2.5 的半连续动态膜生物反应器进行了超过 300 天的运行。在优化的运行方案下,有机负荷率逐渐提高到 11.9 g COD/L/d。因此,在 FW/CM 比为 2.5 的情况下维持了稳定的厌氧共消化,并且实现了 2.71 L CH/L/d 的高 CH 产量和 441 mL CH/g VS 的 CH 产率。在长期运行中,消化液的 pH 值稳定在约 8.4,这表明在没有挥发性脂肪酸积累的情况下,具有非常有利的厌氧反应条件。