合成气
木材气体发生器
流化床
废物管理
环境科学
生物量(生态学)
tar(计算)
中试装置
洗涤器
发生炉煤气
燃烧
燃料气
制浆造纸工业
材料科学
氢
煤
化学
工程类
海洋学
有机化学
计算机科学
程序设计语言
地质学
作者
Andrea Di Carlo,Elisa Savuto,Pier Ugo Foscolo,Alessandro Antonio Papa,Alessandra Tacconi,Luca Del Zotto,Bora Aydin,Enrico Bocci
出处
期刊:Energies
[Multidisciplinary Digital Publishing Institute]
日期:2022-06-15
卷期号:15 (12): 4369-4369
被引量:14
摘要
Biomass gasification is a favourable process to produce a H2-rich fuel gas from biogenic waste materials. In particular, the dual bubbling fluidized bed (DBFB) technology consists of the separation of the combustion chamber, fed with air, from the gasification chamber, fed with steam, allowing to obtain a concentrated syngas stream without N2 dilution. In a previous work, an innovative design of a DBFB reactor was developed and its hydrodynamics tested in a cold model; in this work, the novel gasifier was realized at pilot scale (100 kWth) and operated for preliminary biomass gasification tests. The results showed a high-quality syngas, composed of H2 = 35%, CO = 23%, CO2 = 20%, and CH4 = 11%, as a confirmation of the design efficacy in the separation of the reaction chambers. The dry gas yield obtained was 1.33 Nm3/kg of biomass feedstock and the carbon conversion was 73%. Tars were sampled and measured both in the raw syngas, giving a content of 12 g/Nm3, and downstream from a traditional conditioning system composed of a cyclone and a water scrubber, showing a residual tar content of 3 g/Nm3, mainly toluene. The preliminary tests showed promising results; further gasification tests are foreseen to optimize the main process parameters.
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