van der Zee F P, Villaverde S, García P A, Fdz-Polanco F
Department of Chemical Engineering and Environmental Technology, Faculty of Sciences, University of Valladolid, Paseo Prado de la Magdalena s/n, 47005 Valladolid, Spain.
Bioresour Technol. 2007 Feb;98(3):518-24. doi: 10.1016/j.biortech.2006.02.011. Epub 2006 Apr 19.
Introduction of a limited amount of oxygen to anaerobic bioreactors is proposed as a simple technique to lower the level of sulfide in the biogas. This paper presents the results of a bioreactor study and of batch experiments that were performed to obtain better insight into the fate of sulfur compounds and oxygen during micro-aerobic sulfide oxidation. Introduction of a low airflow (0.7-0.9 m(3)m(-3)d(-1), corresponding to an O(2)/S molar ratio of 8-10) to a fluidized bed reactor fed with low-sulfate vinasse was sufficient to reduce the biogas H(2)S-content to an undetectable level. Sulfide was initially oxidized to elemental sulfur, thiosulfate and - most probably - polysulfide. Significant sulfate production did not occur. Bioreactor sludge sampled from the reactor after three weeks' micro-aerobic operation was much faster in oxidizing sulfur than bioreactor sludge sampled during fully anaerobic reactor operation. The reaction proceeded faster with increasing O(2)/sulfide ratios.
向厌氧生物反应器中引入少量氧气被认为是一种降低沼气中硫化物含量的简单技术。本文介绍了一项生物反应器研究和批次实验的结果,这些实验旨在更好地了解微需氧硫化物氧化过程中硫化合物和氧气的去向。向装有低硫酸盐酒糟的流化床反应器中引入低气流(0.7 - 0.9 m³m⁻³d⁻¹,对应O₂/S摩尔比为8 - 10)足以将沼气中的H₂S含量降低到检测不到的水平。硫化物最初被氧化为元素硫、硫代硫酸盐,很可能还有多硫化物。没有产生大量的硫酸盐。在微需氧运行三周后从反应器中采集的生物反应器污泥氧化硫的速度比在完全厌氧反应器运行期间采集的生物反应器污泥快得多。随着O₂/硫化物比例的增加,反应进行得更快。