Determination of the optimal rate for the microaerobic treatment of several H2S concentrations in biogas from sludge digesters

被引:26
作者
Diaz, I. [1 ]
Lopes, A. C. [2 ]
Perez, S. I. [1 ]
Fdz-Polanco, M. [1 ]
机构
[1] Univ Valladolid, Dept Chem Engn & Environm Technol, Escuela Ingn Ind, E-47011 Valladolid, Spain
[2] Univ Fed Ceara, Dept Hydraul & Environm Technol, BR-60451970 Fortaleza, Ceara, Brazil
关键词
biogas; dose control; H2S removal; microaerobic; optimal O-2 rate; ANAEROBIC-DIGESTION; SULFIDE REMOVAL; OXYGENATION;
D O I
10.2166/wst.2011.648
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The treatment of H2S in the biogas produced during anaerobic digestion has to be carried out to ensure the efficient long-lasting use of its energetic potential. The microaerobic removal of H2S was studied to determine the treatment capacity at low and high H2S concentrations in the biogas (0.33 and 3.38% v/v) and to determine the optimal O-2 rate that achieved a concentration of H2S of 150 mg/Nm(3) or lower. Research was performed in pilot-plant scale digesters of sewage sludge, with 200 L of working volume, in mesophilic conditions with a hydraulic retention time of 20 d. O-2 was supplied at different rates to the headspace of the digester to create the microaerobic conditions. The treatment successfully removed H2S from the biogas with efficacies of 97% for the low concentration and 99% for the highest, in both cases achieving a concentration below 150 mg/Nm(3). An optimal O-2 rate of 6.4 NLO2/Nm(3) of biogas when treating the biogas was found with 0.33% (v/v) of H2S and 118 NLO2/Nm(3) of biogas for the 3.38% (v/v) concentration. This relation may be employed to control the H2S content in the biogas while optimising the O-2 supply.
引用
收藏
页码:233 / 238
页数:6
相关论文
共 16 条
[1]   A review of biogas purification processes [J].
Abatzoglou, Nicolas ;
Boivin, Steve .
BIOFUELS BIOPRODUCTS & BIOREFINING-BIOFPR, 2009, 3 (01) :42-71
[2]  
[Anonymous], 2008, BIOGAS WASTE RENEWAB
[3]  
Clesceri L, 1998, STANDARD METHODS EXA
[4]   Effect of oxygen dosing point and mixing on the microaerobic removal of hydrogen sulphide in sludge digesters [J].
Diaz, I. ;
Perez, S. I. ;
Ferrero, E. M. ;
Fdz-Polanco, M. .
BIORESOURCE TECHNOLOGY, 2011, 102 (04) :3768-3775
[5]   Performance evaluation of oxygen, air and nitrate for the microaerobic removal of hydrogen sulphide in biogas from sludge digestion [J].
Diaz, I. ;
Lopes, A. C. ;
Perez, S. I. ;
Fdz-Polanco, M. .
BIORESOURCE TECHNOLOGY, 2010, 101 (20) :7724-7730
[6]   Hydrogen sulphide removal in the anaerobic digestion of sludge by micro-aerobic processes: pilot plant experience [J].
Fdz-Polanco, M. ;
Diaz, I. ;
Perez, S. I. ;
Lopes, A. C. ;
Fdz-Polanco, F. .
WATER SCIENCE AND TECHNOLOGY, 2009, 60 (12) :3045-3050
[7]   Industrial applications of new sulphur biotechnology [J].
Janssen, AJH ;
Ruitenberg, R ;
Buisman, CJN .
WATER SCIENCE AND TECHNOLOGY, 2001, 44 (08) :85-90
[8]   BIOLOGICAL SULFIDE OXIDATION IN A FED-BATCH REACTOR [J].
JANSSEN, AJH ;
SLEYSTER, R ;
VANDERKAA, C ;
JOCHEMSEN, A ;
BONTSEMA, J ;
LETTINGA, G .
BIOTECHNOLOGY AND BIOENGINEERING, 1995, 47 (03) :327-333
[9]   Use of microaerobic conditions for the improvement of anaerobic digestion of solid wastes [J].
Jenicek, P. ;
Keclik, F. ;
Maca, J. ;
Bindzar, J. .
WATER SCIENCE AND TECHNOLOGY, 2008, 58 (07) :1491-1496
[10]   Advantages of anaerobic digestion of sludge in microaerobic conditions [J].
Jenicek, P. ;
Koubova, J. ;
Bindzar, J. ;
Zabranska, J. .
WATER SCIENCE AND TECHNOLOGY, 2010, 62 (02) :427-434