Date palm waste gasification in downdraft gasifier and simulation using ASPEN HYSYS

被引:68
作者
Bassyouni, M. [1 ,2 ]
ul Hasan, Syed Waheed [1 ]
Abdel-Aziz, M. H. [1 ,3 ]
Abdel-hamid, S. M. -S. [2 ]
Naveed, Shahid [4 ]
Hussain, Ahmed [5 ]
Ani, Farid Nasir [6 ]
机构
[1] King Abdulaziz Univ, Dept Chem & Mat Engn, Rabigh 21911, Saudi Arabia
[2] Higher Technol Inst, Dept Chem Engn, Tenth Of Ramdan City, Egypt
[3] Univ Alexandria, Fac Engn, Dept Chem Engn, Alexandria, Egypt
[4] Punjab Inst Contemporary Sci, Lahore, Pakistan
[5] King Abdulaziz Univ, Dept Nucl Engn, Jeddah 21589, Saudi Arabia
[6] Univ Teknol Malaysia, Fac Mech Engn, Johor Baharu 81310, Malaysia
关键词
Biomass gasification; Downdraft gasifier; ASPEN HYSYS; Simulation; Steam to biomass ratio; BIOMASS GASIFICATION; REDUCTION REACTIONS; STEAM GASIFICATION; EQUILIBRIUM; HYDROGEN;
D O I
10.1016/j.enconman.2014.08.061
中图分类号
O414.1 [热力学];
学科分类号
070201 [理论物理];
摘要
The present research aims to study the simulation of date palm waste gasification using ASPEN HYSYS. A steady state simulation of downdraft gasifier firing date palm leaves has been developed. The model is able to predict syngas composition with sound accuracy and can be used to find optimal operating conditions of the gasifier. Biomass is defined as an unconventional hypothetical solid component in HYSYS. A set of six reactor models simulates various reaction zones of the downdraft gasifier in accordance with its hydrodynamics. Biomass decomposition into constituents in the pyrolysis zone is modeled with a conversion reactor. The combustion of char and volatiles in the combustion zone are modeled with equilibrium and Gibbs reactor models respectively. The gasification zone is modeled with a Gibbs and equilibrium reactor. The results of simulation are validated against experimental results of a parametric variability study on a lab scale gasifier. The proportion of synthesis gas increase as temperature increases (concentration, molar fraction, and partial pressure). CO2 and CH4 in the product gases were also found to decrease with increasing temperature. At 800 degrees C, the exit gas reaches a stable molar composition (H-2=56.27%, CO=21.71%, CO2=18.24%, CH4=3.78%). Increasing steam to biomass ratio increases CO2 and H-2 at the expense of CO, governed by shift reaction. Steam induction increases the methane contents, thereby improves the heating value of the product gas. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:693 / 699
页数:7
相关论文
共 36 条
[1]
The Peak of the Oil Age - Analyzing the world oil production Reference Scenario in World Energy Outlook 2008 [J].
Aleklett, Kjell ;
Hook, Mikael ;
Jakobsson, Kristofer ;
Lardelli, Michael ;
Snowden, Simon ;
Soderbergh, Bengt .
ENERGY POLICY, 2010, 38 (03) :1398-1414
[2]
Alkoaik F. N., 2011, Middle East Journal of Scientific Research, V7, P972
[3]
[Anonymous], 2010, CO2 EM FUEL COMB HIG
[4]
Production of biodiesel using high free fatty acid feedstocks [J].
Atadashi, I. M. ;
Aroua, M. K. ;
Aziz, A. R. Abdul ;
Sulaiman, N. M. N. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2012, 16 (05) :3275-3285
[5]
Physico-mechanical properties of chemically treated polypropylene rice straw bio-composites [J].
Bassyouni, M. ;
Taha, I. ;
Abdel-hamid, Shereen M-S ;
Steuernagel, L. .
JOURNAL OF REINFORCED PLASTICS AND COMPOSITES, 2012, 31 (05) :303-312
[6]
Conversion of carbon dioxide and methane in biomass synthesis gas for liquid fuels production [J].
Chattanathan, Shyamsundar Ayalur ;
Adhikari, Sushil ;
Taylor, Steven .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (23) :18031-18039
[7]
Status and barriers of advanced biofuel technologies: A review [J].
Cheng, Jay J. ;
Timilsina, Govinda R. .
RENEWABLE ENERGY, 2011, 36 (12) :3541-3549
[8]
Doherty W., 2008, SIMULATION CIRCULATI
[9]
The effect of air preheating in a biomass CFB gasifier using ASPEN Plus simulation [J].
Doherty, Wayne ;
Reynolds, Anthony ;
Kennedy, David .
BIOMASS & BIOENERGY, 2009, 33 (09) :1158-1167
[10]
Emun F., 2008, COMPUTER AIDED CHEM