Simultaneous Removal of Toluene (Model Tar), NH3, and H2S, from Biomass-Generated Producer Gas Using Biochar-Based and Mixed-Metal Oxide Catalysts

被引:29
作者
Bhandari, Pushpak N. [1 ]
Kumar, Ajay [1 ]
Huhnke, Raymond L. [1 ]
机构
[1] Oklahoma State Univ, Biobased Prod & Energy Ctr, Dept Biosyst & Agr Engn, Stillwater, OK 74078 USA
关键词
HOT GAS; HYDROGEN-SULFIDE; GASIFICATION; HYDROTALCITE; AMMONIA; GASIFIER; SULFUR;
D O I
10.1021/ef4016872
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Effectiveness of four catalysts (biochar, activated carbon, acidic surface activated carbon, and mixed metal oxide) was studied for simultaneous removal of toluene, NH3, and H2S from biomass-generated producer gas. NH3 (0.03%), H2S (0.015%), and toluene at a flow rate of 2 mL/h were mixed with a synthetic producer gas composition (H-2: 8.5%, N-2: 58%, CO: 17%, CH4: 2%, and CO2: 11%) and passed over a catalyst bed in a fixed-bed reactor tube maintained at 800 degrees C. Results indicate that simultaneous removal of contaminants from producer gas is feasible using biochar-based catalysts. High surface area mixed metal oxides synthesized using microwave and ultrasonication were also effective for simultaneous removal of contaminants. Among the four catalysts, acidic surface activated carbon resulted in the highest toluene removal efficiency of 97.5% and highest breakthrough time of 145 mm for NH3. For H2S removal, mixed metal oxides resulted in the highest breakthrough time of 105 mm. For simultaneous removal of toluene, H2S and NH3, activated carbon showed good removal capacity (91% toluene removal efficiency; NH3 adsorption capacity of 0.03g-NH3/g-activated carbon; H2S adsorption capacity of 0.008 g-H2S/g-activated carbon), whereas biochar had moderate removal capacity (86% toluene removal efficiency; NH3 adsorption capacity of 0.008 g-NH3/g-biochar; H2S adsorption capacity of 0.008 g-H2S/g-biochar).
引用
收藏
页码:1918 / 1925
页数:8
相关论文
共 39 条
[1]   A regenerable copper-based sorbent for H2S removal from coal gases [J].
Abbasian, J ;
Slimane, RB .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (07) :2775-2782
[2]   Analysis of the relationship between H2S removal capacity and surface properties of unimpregnated activated carbons [J].
Adib, F ;
Bagreev, A ;
Bandosz, TJ .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2000, 34 (04) :686-692
[3]  
[Anonymous], THESIS OKLAHOMA STAT
[4]  
AYALA RE, 1993, Patent No. 5188811
[5]   Biochar as a precursor of activated carbon [J].
Azargohar, R. ;
Dalai, A. K. .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2006, 131 (1-3) :762-773
[6]  
Bhandari P., 2012, ASABE ANN INT M DALL
[7]  
Bhandari PN, 2012, THESIS OKLAHOMA STAT
[8]   A study on wood gasification for low-tar gas production [J].
Bhattacharya, SC ;
Siddique, AHMMR ;
Pham, HL .
ENERGY, 1999, 24 (04) :285-296
[9]  
Bhattacharyya A., 1998, U.S. Patent, Patent No. 5843862
[10]   Kinetic modeling of the effect of H2S and of NH3 on toluene hydrogenation in the presence of a NiMo/Al2O3 hydrotreating catalyst.: Discrimination between homolytic and heterolytic models [J].
Blanchin, S ;
Galtier, P ;
Kasztelan, S ;
Kressmann, S ;
Penet, H ;
Pérot, G .
JOURNAL OF PHYSICAL CHEMISTRY A, 2001, 105 (48) :10860-10866