Enhancing biomass gasification: A comparative study of catalyst applications in updraft and modifiable-downdraft fixed bed reactors

被引:5
作者
Yesilova, Nazlican [1 ]
Tezer, Ozgun [2 ]
Ongen, Atakan [1 ,3 ]
Ayol, Azize [4 ]
机构
[1] Istanbul Univ Cerrahpasa, Dept Environm Engn, Istanbul, Turkiye
[2] Dokuz Eylul Univ, Grad Sch Nat & Appl Sci, Dept Environm Engn, TR-35390 Izmir, Turkiye
[3] Istanbul Univ Cerrahpasa, Environm & Earth Sci Applicat & Res Ctr, Istanbul, Turkiye
[4] Dokuz Eylul Univ, Dept Environm Engn, TR-35390 Izmir, Turkiye
关键词
Biomass; Catalyst; Gasification; Hydrogen; Renewable energy; RICH GAS-PRODUCTION; STEAM CO-GASIFICATION; HYDROGEN-PRODUCTION; SEWAGE-SLUDGE; GASIFIER PERFORMANCE; SYNGAS PRODUCTION; H-2/CO RATIO; PYROLYSIS; RESIDUES; BIOCHAR;
D O I
10.1016/j.ijhydene.2024.05.075
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
This study aims to investigate the effects of different catalysts on biomass gasification. Therefore, red mud (RM) and Aluminum - Nickel alloy were used as catalysts with biomass mixture (BM) for the lab-scale gasification studies by using an updraft and a modifiable-downdraft fixed bed reactor. The maximum volumetric percentage of H 2 , ranging from 51% to 65%, was achieved at 900 degrees C in both gasifiers. Al - Ni catalyst significantly boosted H 2 content, reaching 65% in the updraft gasifier at 900 degrees C with 0.05 L/min dry air. H 2 /CO ratio varied from 2 to 4 for BM, while catalyst use expanded the range to 1.6 - 7 with the Al - Ni catalyst demonstrating the most effective performance. In general, it was seen that RM increased the H 2 component in the syngas between 1 and 7 vol% at 900 degrees C in updraft gasifier. In the modifiable-downdraft reactor, on the contrary, H 2 concentration in the syngas decreased by 2 - 6% with the addition of RM.
引用
收藏
页码:290 / 303
页数:14
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