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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:
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).
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页码:717 / 726
页数:10
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