Vallero Marcus V G, Camarero Eva, Lettinga Gatze, Lens Piet N L
Sub-department of Environmental Technology, Wageningen University, "Biotechnion" Bomenweg, 2, PO Box 8129, 6700 EV Wageningen, The Netherlands.
Biotechnol Prog. 2004 Sep-Oct;20(5):1382-92. doi: 10.1021/bp034329a.
The feasibility of thermophilic (55-65 degrees C) and extreme thermophilic (70-80 degrees C) sulfate-reducing processes was investigated in three lab-scale upflow anaerobic sludge bed (UASB) reactors fed with either methanol or formate as the sole substrates and inoculated with mesophilic granular sludge previously not exposed to high temperatures. Full methanol and formate degradation at temperatures up to, respectively, 70 and 75 degrees C, were achieved when operating UASB reactors fed with sulfate rich (COD/SO4(2-)=0.5) synthetic wastewater. Methane-producing archaea (MPA) outcompeted sulfate-reducing bacteria (SRB) in the formate-fed UASB reactor at all temperatures tested (65-75 degrees C). In contrast, SRB outcompeted MPA in methanol-fed UASB reactors at temperatures equal to or exceeding 65 degrees C, whereas strong competition between SRB and MPA was observed in these reactors at 55 degrees C. A short-term (5 days) temperature increase from 55 to 65 degrees C was an effective strategy to suppress methanogenesis in methanol-fed sulfidogenic UASB reactors operated at 55 degrees C. Methanol was found to be a suitable electron donor for sulfate-reducing processes at a maximal temperature of 70 degrees C, with sulfide as the sole mineralization product of methanol degradation at that temperature.
在三个实验室规模的上流式厌氧污泥床(UASB)反应器中,研究了嗜热(55 - 65摄氏度)和极端嗜热(70 - 80摄氏度)硫酸盐还原过程的可行性。这些反应器以甲醇或甲酸盐作为唯一底物,并接种先前未暴露于高温的中温颗粒污泥。当运行以富含硫酸盐(化学需氧量/硫酸根离子=0.5)的合成废水为进料的UASB反应器时,分别在高达70和75摄氏度的温度下实现了甲醇和甲酸盐的完全降解。在所有测试温度(65 - 75摄氏度)下,在以甲酸盐为进料的UASB反应器中,产甲烷古菌(MPA)胜过硫酸盐还原细菌(SRB)。相比之下,在温度等于或超过65摄氏度时,在以甲醇为进料的UASB反应器中SRB胜过MPA,而在55摄氏度时,在这些反应器中观察到SRB和MPA之间存在激烈竞争。将温度从55摄氏度短期(5天)提高到65摄氏度是抑制在55摄氏度运行的以甲醇为进料的产硫化物UASB反应器中甲烷生成的有效策略。发现甲醇是最高温度为70摄氏度的硫酸盐还原过程的合适电子供体,在该温度下,硫化物是甲醇降解的唯一矿化产物。