Simulation of Olive Pomace Gasification for Hydrogen Production Using Aspen Plus: Case Study Lebanon

被引:0
|
作者
Matta, Georges [1 ]
Semaan, Daniella [1 ]
Harb, Rita [1 ]
机构
[1] Holy Spirit Univ Kaslik, Sch Engn, Dept Chem & Petr Engn, POB 446, Jounieh, Lebanon
关键词
hydrogen; gasification; dual fluidized bed gasifier; biomass; renewable energy; Aspen Plus; sensitivity analysis; FLUIDIZED-BED GASIFIER; STEAM GASIFICATION; SHIFT REACTION; BIOMASS; GAS; CATALYST; METHANE; SYNGAS; YIELD;
D O I
10.3390/en17071621
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 is a renewable energy source gaining attention for its potential to replace fossil fuels. Biomass gasification can produce hydrogen-rich gas, offering an environmentally friendly fuel for power generation, transportation, and industry. Hydrogen is a promising energy carrier due to its high energy density, low greenhouse gas emissions, and versatility. This study aims to develop a hydrogen generation plant using a dual fluidized bed gasifier, which employs steam as a gasifying agent, to convert olive pomace waste from the Lebanese olive oil industry into hydrogen. The process is simulated using Aspen Plus and Fortran coding, and it includes a drying unit, gasification unit, gas cleaning unit, steam methane reformer unit, water-gas shift reactor unit, and a pressure swing adsorption unit. The generated gas composition is verified against previous research. Sensitivity analyses are conducted to investigate the impacts of the steam-to-biomass ratio (STBR) and gasification temperature on gas composition, demonstrating a valid STBR range of 0.5 to 1 and a reasonable gasification temperature range of 700 degrees C to 800 degrees C. Further sensitivity analyses assess the impact of reformer temperature and the steam-to-carbon ratio (S/C) on the gas composition leaving the steam methane reformer.
引用
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页数:26
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