College of Biosystems Engineering and Food Science, Zhejiang University, Hangzhou 310058, China; Biological Engineering Department, Agricultural Engineering Research Institute, Agricultural Research Center, Giza, Egypt.
State Key Laboratory of Pollution Control and Resources Reuse, College of Environmental Science and Engineering, Tongji University, Shanghai 200092, China; Department of Agricultural Engineering, Faculty of Agriculture, Suez Canal University, Ismailia 41522, Egypt.
Bioresour Technol. 2022 Jul;355:127239. doi: 10.1016/j.biortech.2022.127239. Epub 2022 Apr 27.
Biohythane production through one-stage anaerobic digestion of sulfate-rich hydrolyzed tofu processing residue has been hampered by high HS production. Herein, two-stage anaerobic digestion was investigated with the addition of molybdate (MoO; 0.24-3.63 g/L) and ferric chloride (FeCl; 0.025-5.4 g/L) to the dark fermentation stage (DF) to improve biohythane production. DF supplemented with 1.21 g/L MoO increased hydrogen yield by 14.6% over the control (68.39 ml/g-VS), while FeCl had no effect. Furthermore, the maximum methane yields of methanogenic fermentation were 524.8 and 521.6 ml/g-VS with 3.63 g/L MoO and 0.6 g/L FeCl compared to 466.07 ml/g-VS of the control. The maximum yields of biohythane and energy were 796.7 ml/g-VS and 21.8 MJ/kg-VS with 0.6 g/L FeCl when the sulfate removal efficiency was 66.7%, and HS content was limited at 0.08%. Therefore, adding 0.6 g/L FeCl is the most beneficial in improving energy recovery and sulfate removal with low HS content.
通过一阶段厌氧消化富含硫酸盐的水解豆腐加工残余物生产生物甲烷受到高 H2S 产量的阻碍。本文研究了两段式厌氧消化,在暗发酵阶段(DF)添加钼酸盐(MoO;0.24-3.63 g/L)和氯化铁(FeCl;0.025-5.4 g/L),以提高生物甲烷的产量。DF 中添加 1.21 g/L MoO 使氢气产量比对照(68.39 ml/g-VS)提高了 14.6%,而 FeCl 则没有效果。此外,添加 3.63 g/L MoO 和 0.6 g/L FeCl 的产甲烷发酵的最大甲烷产量分别为 524.8 和 521.6 ml/g-VS,而对照的最大甲烷产量为 466.07 ml/g-VS。当硫酸盐去除效率为 66.7%,H2S 含量限制在 0.08%时,添加 0.6 g/L FeCl 可使生物甲烷和能量的最大产量分别达到 796.7 ml/g-VS 和 21.8 MJ/kg-VS。因此,添加 0.6 g/L FeCl 最有利于在低 H2S 含量下提高能量回收和硫酸盐去除。