2018
DOI: 10.1016/j.jenvman.2017.06.061
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Control of dissolved CH4 in a municipal UASB reactor effluent by means of a desorption – Biofiltration arrangement

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Cited by 26 publications
(16 citation statements)
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“…One of the main advantages of UASB system is represented by the production of methane and therefore the feasibility of energy recovery. This aspect contributes to the significant widespread of these reactors in low–middle-income countries [ 13 , 14 ]. This is a crucial aspect since water sanitation and energy production are inserted in the Sustainable Development Goals (SDGs) of the United Nations (SDG 6 and SDG 7, respectively) [ 15 ].…”
Section: Introductionmentioning
confidence: 99%
“…One of the main advantages of UASB system is represented by the production of methane and therefore the feasibility of energy recovery. This aspect contributes to the significant widespread of these reactors in low–middle-income countries [ 13 , 14 ]. This is a crucial aspect since water sanitation and energy production are inserted in the Sustainable Development Goals (SDGs) of the United Nations (SDG 6 and SDG 7, respectively) [ 15 ].…”
Section: Introductionmentioning
confidence: 99%
“…In this case, the waste gas had a CH 4 content of 22% v/v , above the minimum content of 20% v/v recommended for combustion and heat production (Browell et al 2009). Compared with Huete et al (2018), the better D-H 2 S desorption performance reported by Santo (2017) (pKa 1 ), and by the lower HLR considered in this study (0.10-1.00 m 3 m −2 min −1 ). In a demonstration-scale desorption chamber packed with electrical corrugated pipe (diameter = 35 cm; packed height = 1.0 m), Machado (2018) found D-H 2 S and D-CH 4 desorption efficiencies of 87-90% and 75-82%, respectively, at G/L ratios in the range of 2.3-4.0, and HLR of 0.15-0.27 m 3 m −2 min −1 .…”
Section: Packed Desorption Chambermentioning
confidence: 49%
“…The waste gas had an H 2 S content of approximately 420 ppm. The low D-H 2 S desorption could be associated with the pH of the UASB reactor effluent, which was 8.0 ± 0.3 during the experiments (Huete et al 2018), and with the HLR considered in this study (0.85-1.70 m 3 m −2 min −1 ).…”
Section: Packed Desorption Chambermentioning
confidence: 70%
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