Dimethyl Sulfide Removal from Synthetic Waste Gas Using a Flat Poly(dimethylsiloxane)-Coated Composite Membrane Bioreactor

2003 ◽  
Vol 37 (18) ◽  
pp. 4228-4234 ◽  
Author(s):  
Inge De Bo ◽  
Jeroen Heyman ◽  
Jochen Vincke ◽  
Willy Verstraete ◽  
Herman Van Langenhove
Desalination ◽  
2002 ◽  
Vol 148 (1-3) ◽  
pp. 281-287 ◽  
Author(s):  
Inge De Bo ◽  
Herman Van Langenhove ◽  
Jeroen Heyman

1989 ◽  
Vol 52 (2) ◽  
pp. 229-239 ◽  
Author(s):  
Lucio D'ilario ◽  
Maurizio M. Steffan

2019 ◽  
Vol 39 (1) ◽  
pp. 13304 ◽  
Author(s):  
Arwa Lagha ◽  
Abdelmottaleb Ouederni ◽  
Hédi Ben Abdallah

2011 ◽  
Vol 5 (4) ◽  
pp. 604-609 ◽  
Author(s):  
Lihui Zhang ◽  
Guomin Cao ◽  
Yulei Fei ◽  
Hong Ding ◽  
Mei Sheng ◽  
...  

2006 ◽  
Vol 26 (6) ◽  
pp. 527-542 ◽  
Author(s):  
E. H. Lock ◽  
A. V. Saveliev ◽  
L. A. Kennedy

2013 ◽  
Vol 295-298 ◽  
pp. 1110-1114
Author(s):  
Yi Yuan ◽  
Yong Huang ◽  
Xiang Li ◽  
Liang Wang

An anaerobic membrane bioreactor (UBF) with a total capacity of 3L was employed for treatment of sulfide and nitrate containing wastewater with elemental sulfur as terminal product. The effect of HRT and pH on substrate removal and elemental sulfur accumulation was researched when S/N ratio at 2.5. The influent concentration of S2-/HS-and NO3--N were 110mg•L-1and 20mg•L-1, respectively, during autotrophic denitrification. When HRT was between 7.41h and 6.83h and pH was between 6 and 7.5, HRT and pH has no effect on NO3--N and sulfide removal ratios, and at 97% and 100%, respectively, but elemental sulfur accumulation ratio was increased to 61% with HRT shorten. And low pH (pH at 7) was conducive to elemental sulfur accumulation with the ratio up to 62%. But further to reduce the pH would lead marginal increase in elemental sulfur accumulation ratio at 65%.


1989 ◽  
Vol 53 (1) ◽  
pp. 1-7 ◽  
Author(s):  
Lucio D'ilario ◽  
Maurizio M. Steffan

2014 ◽  
Vol 8 (1) ◽  
pp. 142-149 ◽  
Author(s):  
Jian Guan ◽  
Yuan Xiao ◽  
Jimin Song ◽  
Junhe Miao

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