Application of eggshell as catalyst for low rank coal gasification: Experimental and kinetic studies

被引:18
作者
Fan, Shumin [1 ]
Xu, Li-Hua [1 ]
Kang, Tae-Jin [1 ]
Kim, Hyung-Taek [1 ]
机构
[1] Ajou Univ, Dept Energy Syst Res, Suwon 16499, South Korea
关键词
Catalytic steam gasification; Low rank coal; Egg shell catalyst; Kinetics; H-2-rich syngas; FLUID-SOLID REACTIONS; RANDOM PORE MODEL; STEAM GASIFICATION; GAS-PRODUCTION; REACTIVITY; BIODIESEL; TEMPERATURES; CHARS; OIL; BED;
D O I
10.1016/j.joei.2016.07.008
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
The objective of this research was to study effects of waste eggshells (ES) as a catalyst on the gasification of Indonesian sub-bituminous Komisi Pemilihan Umum (KPU) coal in a fixed-bed reactor under atmospheric pressure at three temperatures (700, 800, and 900 degrees C). With the ES catalyst, the highest H-2 yield of 1.24 mol-/mol-C (64 vol%) was obtained, an 80% increase compared with that of raw coal gasification without catalyst (0.69 mol-/mol-C). In addition, a CO yield of 0.34 mol-/mol-C was obtained, which is 31% higher than that of raw coal gasification (0.26 mol-/mol-C). Compared to raw coal gasification without catalyst, the ES catalytic gasification had higher syngas yield and reactivity. Through comparison, the best model for describing the reactivity of KPU coal with ES catalyst was the RPM (Random pore model) among the three gas solid reaction models adopted in this research. The RPM could adequately describe the conversion rate, giving an accurate prediction and explanation of the rate change during gasification. Rational kinetic parameters were determined from the RPM, which provided a basis for design and operation of a realistic system. (C) 2016 Energy Institute. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:696 / 703
页数:8
相关论文
共 21 条
[1]   Preparation of calcium-phosphate bioceramics from natural resources [J].
Balazsi, Csaba ;
Weber, Ferenc ;
Kover, Zsuzsanna ;
Horvath, Eniko ;
Nemeth, Csaba .
JOURNAL OF THE EUROPEAN CERAMIC SOCIETY, 2007, 27 (2-3) :1601-1606
[2]  
BHATIA SK, 1980, AICHE J, V26, P379, DOI 10.1002/aic.690260308
[3]   A RANDOM PORE MODEL FOR FLUID-SOLID REACTIONS .2. DIFFUSION AND TRANSPORT EFFECTS [J].
BHATIA, SK ;
PERLMUTTER, DD .
AICHE JOURNAL, 1981, 27 (02) :247-254
[4]   Transesterification of waste frying oil for synthesizing biodiesel by KOH supported on coconut shell activated carbon in packed bed reactor [J].
Buasri, Achanai ;
Chaiyut, Nattawut ;
Loryuenyong, Vorrada ;
Rodklum, Chao ;
Chaikwan, Techit ;
Kumphan, Nanthakrit ;
Jadee, Kritsanapong ;
Klinklom, Pathravut ;
Wittayarounayut, Wittaya .
SCIENCEASIA, 2012, 38 (03) :283-288
[5]   Improved reactivity of large coal particles by K2CO3 addition during steam gasification [J].
Coetzee, Sansha ;
Neomagus, Hein W. J. P. ;
Bunt, John R. ;
Everson, Raymond C. .
FUEL PROCESSING TECHNOLOGY, 2013, 114 :75-80
[6]   POWDERED EGGSHELL - A PILOT-STUDY ON A NEW BONE SUBSTITUTE FOR USE IN MAXILLOFACIAL SURGERY [J].
DUPOIRIEUX, L ;
POURQUIER, D ;
SOUYRIS, F .
JOURNAL OF CRANIO-MAXILLOFACIAL SURGERY, 1995, 23 (03) :187-194
[7]   Kinetic models comparison for steam gasification of different nature fuel chars [J].
Fermoso, J. ;
Arias, B. ;
Pevida, C. ;
Plaza, M. G. ;
Rubiera, F. ;
Pis, J. J. .
JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2008, 91 (03) :779-786
[8]   COMPARISON OF ZONE-REACTION MODEL AND UNREACTED-CORE SHRINKING MODEL IN SOLID-GAS REACTIONS .1. ISOTHERMAL ANALYSIS [J].
ISHIDA, M ;
WEN, CY .
CHEMICAL ENGINEERING SCIENCE, 1971, 26 (07) :1031-&
[9]   USE OF CATALYSTS IN COAL-GASIFICATION [J].
JOHNSON, JL .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1976, 14 (01) :131-152
[10]   Sorption enhanced steam hydrogasification of coal for synthesis gas production with in-situ CO2 removal and self-sustained hydrogen supply [J].
Liu, Zhongzhe ;
Park, Chan S. ;
Norbeck, Joseph M. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (17) :7016-7025