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« Previous AbstractExposure assessment for atmospheric ultrafine particles (UFPs) and implications in epidemiologic research    Next AbstractDevelopment of a novel process for the biological conversion of H2S and methanethiol to elemental sulfur »

Water Environ Res


Title:Degradation of methanethiol in a continuously operated upflow anaerobic sludge-blanket reactor
Author(s):Sipma J; van Bree R; Janssen AJ; Arena B; Hulshoff PL; Lettinga G;
Address:"Sub-Department of Environmental Technology of Wageningen University, The Netherlands"
Journal Title:Water Environ Res
Year:2002
Volume:74
Issue:3
Page Number:264 - 271
DOI: 10.2175/106143002x139992
ISSN/ISBN:1061-4303 (Print) 1061-4303 (Linking)
Abstract:"The feasibility of anaerobic treatment of wastewater containing volatile organic sulfur compounds was investigated using biomass originating from an anaerobic wastewater treatment facility treating brewery wastewater. Interest focused mainly on the degradation of methanethiol (MT), an extremely volatile and malodorous sulfur compound. Formation of hydrogen sulfide from methanethiol, dimethyl sulfide (DMS), and dimethyl disulfide (DMDS) was observed. Batch experiments showed that methanethiol was predominantly used by methanogenic bacteria as the sole source of energy and carbon. Methane was formed on MT degradation, and in the presence of 2-bromoethanesulfonic acid (BES), a specific inhibitor of methanogens, MT conversion was strongly inhibited. During the MT degradation, DMS and DMDS were the other primary compounds found. Relatively small quantities of DMS were present; whereas the DMDS concentrations could accumulate as a result of the relatively fast rate at which methanethiol autoxidizes in the presence of minor amounts of molecular oxygen. It was shown that DMS and DMDS could be biologically degraded, resulting in the formation of methane and hydrogen sulfide. In a continuous experiment using a laboratory-scale upflow anaerobic sludge-blanket (UASB) reactor with a volume of 2.0 L, the feasibility of anaerobic treatment of methanethiol was tested. The reactor was operated at a hydraulic residence time (HRT) of 6 hours, temperature of 30 degrees C, and pH of 7.3 to 7.6. The maximal MT conversion efficiency in the continuous experiment was reached after approximately 70 days and exceeded 97% at an influent concentration of 6 mM, corresponding to a MT loading rate of 25 mM/d. The specific MT degradation rate, as determined after 40 days of operation in the UASB, measured 1.1 +/- 0.1 mM MT/g volatile suspended solids.d. These results show that anaerobic treatment of MT-containing waste streams is an interesting alternative for currently used physicochemical treatment methods"
Keywords:"Air Pollutants, Occupational/*metabolism Bacteria, Anaerobic/physiology Biodegradation, Environmental *Bioreactors Odorants Sulfhydryl Compounds/*metabolism Sulfur Compounds/analysis Waste Disposal, Fluid/methods Water Purification/*methods;"
Notes:"MedlineSipma, Jan van Bree, Robbie Janssen, Albert J H Arena, Blaise Hulshoff, Pol Look W Lettinga, Gatze eng 2002/08/02 Water Environ Res. 2002 May-Jun; 74(3):264-71. doi: 10.2175/106143002x139992"

 
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