Hydrogen production via biomass gasification: simulation and performance analysis under different gasifying agents

被引:23
|
作者
Safarian, Sahar [1 ]
Unnthorsson, Runar [1 ]
Richter, Christiaan [1 ]
机构
[1] Univ Iceland, Fac Ind Engn Mech Engn & Comp Sci, Hjardarhagi 6, IS-107 Reykjavik, Iceland
来源
BIOFUELS-UK | 2022年 / 13卷 / 06期
关键词
Hydrogen production; biomass gasification; water-gas shift reactor; process simulation; gasifying agents; AIR-STEAM GASIFICATION; FLUIDIZED-BED; GASIFIER; ENERGY; POWER; COMBUSTION; SYSTEM; COAL; BIOETHANOL; PARAMETERS;
D O I
10.1080/17597269.2021.1894781
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
This study develops a new simulation model by ASPEN Plus for gasification integrated with water-gas shift reactors and product recovery unit for hydrogen production. Timber and wood waste (T&WW) as a lignocellulosic biomass was also considered as the input feedstock to the system. Then, the model is applied to investigate the effect of two agents of air and a mixture of air-steam under different operating conditions of temperature and steam to biomass ratio (SBR). The results reveal that the produced hydrogen through the air-steam gasification is at the highest points for all studied temperatures and it would be maximum (44.37 kmol/hr per 1 ton T&WWs) at 700 degrees C. The hydrogen production efficiency (HPE) can be also raised, stemming from the growth of H-2. It values 39.2% at SBR = 0.1 that grows to 70% at SBR = 0.9. The optimum SBR lies between 0.7-0.8 that specific mass flow rate of hydrogen would be higher than 0.1 kg(hydrogen)/kg(T&WW).
引用
收藏
页码:717 / 726
页数:10
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