Experimental investigation of downdraft biomass gasifier fed by sugarcane bagasse and coconut shells

被引:43
作者
Awais, Muhammad [1 ,2 ]
Li, Wei [1 ]
Munir, Anjum [3 ]
Omar, Muhammad Mubashar [2 ]
Ajmal, Muhammad [4 ]
机构
[1] Jiangsu Univ, Res Ctr Fluid Machinery Engn & Technol, Zhenjiang, Jiangsu, Peoples R China
[2] Univ Agr Faisalabad, Dept Farm Machinery & Power, Faisalabad, Pakistan
[3] Univ Agr Faisalabad, Dept Energy Syst Engn, Faisalabad, Pakistan
[4] Jiangsu Univ, Sch Agr Equipment Engn, Zhenjiang, Jiangsu, Peoples R China
关键词
Biomass gasification; Moisture content; Equivalence ratio; Sugarcane bagasse; Coconut shells; POWER-GENERATION SYSTEM; PRODUCER GAS; RICE HUSK; OPERATIONAL EXPERIENCE; EQUIVALENCE RATIO; BED GASIFICATION; TAR; PERFORMANCE; COMBUSTION; STEAM;
D O I
10.1007/s13399-020-00690-5
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
Biomass gasification is a process of converting solid biomass ingredients into combustible gas, which can be used in electricity generation. A biomass gasifier was designed with 30-40 kg/h downdraft, fabricated, and evaluated using sugarcane bagasse and coconut shells. The effect of equivalence ratio on syngas composition, heating value, syngas yield, gasification efficiency, and tar content was evaluated. Besides, the tar removal efficiency of different cleaning instruments was also evaluated. The investigation revealed that types of biomass feedstock and equivalence ratio have a significant effect on the performance parameter of the gasifier. The average syngas produced from 1 kg of sugarcane bagasse and coconut shells were 3.1 and 2.97 m(3), while the average amount of tar produced from the same fuels was 2.5 and 2.2 g/Nm(3). As ER increased from 0.17 to 0.22, the concentration of carbon monoxide (CO) and hydrogen (H-2) was increased from 14 to 17.9% and 7.5 to 9.6%, respectively. However, the lower calorific value of syngas was increased from 4.4 to 5.4 MJ/Nm(3). Removal efficiency of cleaning instruments is auxiliary filter (45.7%) < wet scrubber (54.2%) < biomass filter (56%) < cyclone separator (60.6%) when sugarcane bagasse was used as a biomass fuel, while for coconut shells, removal efficiencies of the cleaning units were auxiliary filter (52.9%) < cyclone separator (54%) < wet scrubber (59.4%) < biomass filter (65%) respectively.
引用
收藏
页码:429 / 444
页数:16
相关论文
共 53 条
[1]   Bark as feedstock for dual fluidized bed gasifiers-Operability, efficiency, and economics [J].
Ahlstroem, Johan M. ;
Alamia, Alberto ;
Larsson, Anton ;
Breitholtz, Claes ;
Harvey, Simon ;
Thunman, Henrik .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2019, 43 (03) :1171-1190
[2]   Thermogravimetric characterization and gasification of pecan nut shells [J].
Aldana, Hugo ;
Lozano, Francisco J. ;
Acevedo, Joaquin ;
Mendoza, Alberto .
BIORESOURCE TECHNOLOGY, 2015, 198 :634-641
[3]   Tar reduction in biomass producer gas via mechanical, catalytic and thermal methods: A review [J].
Anis, Samsudin ;
Zainal, Z. A. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2011, 15 (05) :2355-2377
[4]  
[Anonymous], 2009, GAS CLEANING DOWNSTR
[5]  
Arun K., 2016, Journal of Chemical and Pharmaceutical Research, V8, P667
[6]   Evaluating removal of tar contents in syngas produced from downdraft biomass gasification system [J].
Awais, Muhammad ;
Li, Wei ;
Arshad, Arfan ;
Haydar, Zeeshan ;
Yaqoob, Nauman ;
Hussain, Sajjad .
INTERNATIONAL JOURNAL OF GREEN ENERGY, 2018, 15 (12) :724-731
[7]  
Basu P, 2010, BIOMASS GASIFICATION AND PYROLYSIS: PRACTICAL DESIGN AND THEORY, P1
[8]   Scale-up of a downdraft gasifier system for commercial scale mobile power generation [J].
Bhoi, Prakashbhai R. ;
Huhnke, Raymond L. ;
Kumar, Ajay ;
Thapa, Sunil ;
Indrawan, Natarianto .
RENEWABLE ENERGY, 2018, 118 :25-33
[9]   State of art of small scale biomass gasification power systems: a review of the different typologies [J].
Bocci, E. ;
Sisinni, M. ;
Moneti, M. ;
Vecchione, L. ;
Di Carlo, A. ;
Villarini, M. .
ATI 2013 - 68TH CONFERENCE OF THE ITALIAN THERMAL MACHINES ENGINEERING ASSOCIATION, 2014, 45 :247-256
[10]  
Brandini A., 1983, Manual del curve de gasificaciOn de la Madera en Centro America y el Caribe, P308