Simulation of sorption enhanced staged gasification of biomass for hydrogen production in the presence of calcium oxide

被引:53
作者
Li, Bin [1 ]
Mbeugang, Christian Fabrice Magoua [1 ]
Liu, Dongjing [1 ]
Zhang, Shu [2 ]
Wang, Shuang [1 ]
Wang, Qian [1 ]
Xu, Zhixiang [1 ]
Hu, Xun [3 ]
机构
[1] Jiangsu Univ, Sch Energy & Power Engn, Zhenjiang 212013, Jiangsu, Peoples R China
[2] Nanjing Forestry Univ, Coll Mat Sci & Engn, Nanjing 210037, Peoples R China
[3] Univ Jinan, Sch Mat Sci & Engn, Jinan 250022, Peoples R China
基金
中国国家自然科学基金;
关键词
Biomass steam gasification; H-2; production; Sorption enhanced staged gasification; Calcium oxide; Simulation; Aspen plus; STEAM-GASIFICATION; FLUIDIZED-BED; RICH GAS; LIGNOCELLULOSIC BIOMASS; SYNGAS PRODUCTION; SHIFT REACTION; PYROLYSIS; COAL; CAO; TEMPERATURE;
D O I
10.1016/j.ijhydene.2020.07.121
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
A novel two-step sorption enhanced staged gasification of biomass for H-2 production was proposed and studied using Aspen Plus software. An equilibrium model based on Gibbs free energy minimization was developed and validated. The results showed that the two-step process was more advantageous for H-2 production compared with the conventional steam gasification and the one-step process. The independent control of each stage could realize a high temperature steam gasification in the first stage and a subsequent lower temperature steam reforming in the second stage, which thus promoted the gasification of biomass and benefited the water gas shift (WGS) reaction to produce more H-2. Meanwhile, the in situ CO2 absorption of CaO in the second stage could enrich the H-2 concentration in the product gas, and also further shifted the WGS reaction equilibrium to convert more CO to H-2. With further introduction of catalyst for steam methane reforming (SMR), highpurity H-2 with the concentration of 99.7 vol% and yield of 142.8 g/kg daf biomass could be achieved. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:26855 / 26864
页数:10
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