2016
DOI: 10.1016/j.jece.2016.08.016
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Review of odour abatement in sewer networks

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Cited by 47 publications
(11 citation statements)
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“…Generally, the performance data of odorant removal in AC adsorption were less reported than the relevant biotechnologies, 19 kinds of odorants were investigated by AC adsorption in the lab and/or field tests, H 2 S and methyl mercaptan are well removed by AC, however, dimethyl disulfide was poorly removed since its generation from the breakdown of methyl mercaptan on AC systems [104]. Moreover, the removal of benzene, xylene, toluene, TCE and PCE reduced with the active lifetime decreased of the AC systems.…”
Section: Comparison Of Different Odor Removal Performancementioning
confidence: 99%
“…Generally, the performance data of odorant removal in AC adsorption were less reported than the relevant biotechnologies, 19 kinds of odorants were investigated by AC adsorption in the lab and/or field tests, H 2 S and methyl mercaptan are well removed by AC, however, dimethyl disulfide was poorly removed since its generation from the breakdown of methyl mercaptan on AC systems [104]. Moreover, the removal of benzene, xylene, toluene, TCE and PCE reduced with the active lifetime decreased of the AC systems.…”
Section: Comparison Of Different Odor Removal Performancementioning
confidence: 99%
“…The activated carbon is a popular filter material with excellent gas sequestration ability because of its high surface area, microporous structure, surface chemistry, etc. (Shammay et al, 2016;Suresh and Bandosz, 2018). Nevertheless, the adsorption is a transfer process of pollutants from the gas phase to the solid phase, which requires a post-treatment to mineralize the adsorbed pollutants (Jo and Yang, 2009;Thevenet et al, 2014).…”
Section: General Overview Of the Current Control Techniques For The R...mentioning
confidence: 99%
“…This reflects a greater capacity to retain high volumes of sewage that may begin to putrefy-should conditions favour that-e.g., at pumping station tanks, or in the directional-change parts of syphon transitions. 1880 µg/m 3 Australian sewers [7] 29,000 µg/m 3 Pumping station waste gas [31] 3770 ± 1100 µg/m 3 Upstream of a siphon, Sydney, winter [32] 11,198 ± 2951 µg/m 3 Upstream of a siphon, Sydney, summer [32] 357 ± 160 µg/m 3 Pump stations wet well, Sydney, winter [32] 1162 ± 521 µg/m 3 Pump stations wet well, Sydney, summer [32] 1102 ± 34.4 µg/m 3 Inlet (downstream of a siphon), Sydney, winter [32] 4625.1 ± 148 µg/m 3 Inlet (downstream of a siphon), Sydney, summer [32] Methyl mercaptan CH 3 SH 0.0003-38 µg/m 3 Sewer [30] 7000 µg/m 3 Pumping station waste gas [31] 293 µg/m 3 Australian sewers [7] 856 ± 78.6 µg/m 3 Upstream of a siphon, Sydney, winter [32] 1290.5 ± 434 µg/m 3 Upstream of a siphon, Sydney, summer [32] 74.…”
Section: Malodorous Gases In the Sewer Systemmentioning
confidence: 99%