Air gasification characteristics of coir pith in a circulating fluidized bed gasifier

被引:19
|
作者
Sheeba, K. N. [1 ]
Babu, J. Sarat Chandra [1 ]
Jaisankar, S. [2 ]
机构
[1] Natl Inst Technol, Dept Chem Engn, Tiruchirappalli 620015, Tamil Nadu, India
[2] OXFORD Engn Coll, Dept Mech Engn, Tiruchirappalli, Tamil Nadu, India
关键词
Coir pith; Gasification; Equivalence Ratio; Gas yield; Conversion; Hydrogen; HYDROGEN-RICH GAS; BIOMASS GASIFICATION; PILOT-SCALE; TAR; CATALYST;
D O I
10.1016/j.esd.2009.06.002
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The gasification characteristics of coir pith are studied in a circulating fluidized bed gasifier using air as the gasifying medium. The effect of various parameters such as temperature, Equivalence Ratio (ER), and Oxygen/Carbon ratio (O/C) on gas yield, gas composition, gas heating value, carbon conversion, cold gas and overall thermal efficiency is studied. The ERs employed in the study are 0.18, 0.21, 0.24 and 0.31. It has been found that temperature has an influence on the cracking reactions, as indicated by the increased yield of hydrogen. The maximum yield of hydrogen is obtained at a temperature of 1028.6 degrees C, and as the Equivalence Ratio (ER) increased, hydrogen yield decreased. The gas yield also increased with increase in temperature and ER. Also it has been observed that the gas heating value increases with increase in temperature and decrease in ER. Carbon conversion is found to increase with increase in temperature and increase in ER. It is found that the increase in temperature favours both the cold gas thermal and overall thermal efficiencies. Also the cold gas and overall thermal gasification efficiencies decrease with increase in Equivalence Ratio. (C) 2009 International Energy Initiative. Published by Elsevier Inc. All rights reserved.
引用
收藏
页码:166 / 173
页数:8
相关论文
共 50 条
  • [31] Simulation of biomass gasification in a dual fluidized bed gasifier
    He J.
    Göransson K.
    Söderlind U.
    Zhang W.
    Biomass Conversion and Biorefinery, 2012, 2 (1) : 1 - 10
  • [32] CFD simulation for coal gasification in fluidized bed gasifier
    Ramakrishnan, P.
    Singh, Jagadish Kumar
    Sahoo, Abanti
    Mohapatra, Soumya Sanjeeb
    ENERGY, 2023, 281
  • [33] Experimental study of biomass gasification with oxygen-enriched air in fluidized bed gasifier
    Liu, Lingqin
    Huang, Yaji
    Cao, Jianhua
    Liu, Changqi
    Dong, Lu
    Xu, Ligang
    Zha, Jianrui
    SCIENCE OF THE TOTAL ENVIRONMENT, 2018, 626 : 423 - 433
  • [34] Biomass gasification in a circulating fluidized bed
    Li, XT
    Grace, JR
    Lim, CJ
    Watkinson, AP
    Chen, HP
    Kim, JR
    BIOMASS & BIOENERGY, 2004, 26 (02): : 171 - 193
  • [35] Wood gasification in the circulating fluidized bed
    Ising, M
    Hölder, D
    Backhaus, C
    Althaus, W
    BRENNSTOFF-WARME-KRAFT, 1998, 50 (1-2): : 59 - +
  • [36] Biomass gasification in circulating fluidized bed
    Chen, P
    Zhao, ZL
    Wu, CZ
    Zhu, J
    Chen, Y
    Circulating Fluidized Bed Technology VIII, 2005, : 507 - 514
  • [37] Parametric study and exergy analysis of the gasification of sugarcane bagasse in a pressurized circulating fluidized bed gasifier
    Mahapatro, Abinash
    Kumar, Alok
    Mahanta, Pinakeswar
    JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2020, 141 (06) : 2635 - 2645
  • [38] Co-gasification of coal/biomass blends in 50 kWe circulating fluidized bed gasifier
    Mallick, Debarshi
    Mahanta, Pinakeswar
    Moholkar, Vijayanand S.
    JOURNAL OF THE ENERGY INSTITUTE, 2020, 93 (01) : 99 - 111
  • [39] Parametric study and exergy analysis of the gasification of sugarcane bagasse in a pressurized circulating fluidized bed gasifier
    Abinash Mahapatro
    Alok Kumar
    Pinakeswar Mahanta
    Journal of Thermal Analysis and Calorimetry, 2020, 141 : 2635 - 2645
  • [40] Parametric investigation on biomass gasification in a fluidized bed gasifier and conceptual design of gasifier
    Xiong, Qingang
    Yeganeh, Mehdi Mihandoost
    Yaghoubi, Ebrihim
    Asadi, Asgar
    Doranehgard, Mohammad Hossein
    Hong, Kun
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2018, 127 : 271 - 291