Hydrogen production by steam-gasification of carbonaceous materials using concentrated solar energy - IV. Reactor experimentation with vacuum residue

被引:46
作者
Z'Graggen, A. [1 ]
Haueter, P. [1 ]
Maag, G. [1 ]
Romero, M. [2 ]
Steinfeld, A. [1 ,3 ]
机构
[1] ETH, Dept Mech & Proc Engn, CH-8092 Zurich, Switzerland
[2] Ctr Invest Energet Medioambientales & Tecnol CIEM, Madrid 28040, Spain
[3] Paul Scherrer Inst, Solar Technol Lab, CH-5232 Villigen, Switzerland
关键词
solar; energy; gasification; pyrolysis; vacuum residue; hydrogen; syngas; reactor;
D O I
10.1016/j.ijhydene.2007.10.038
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
The combined pyrolysis and steam-gasification of petroleum vacuum residue was performed using a 5-kW aerosol-flow solar chemical reactor tested in a high-flux solar furnace in the temperature range 1420-1567 K. The feedstock was continuously injected as a liquid spray at 423 K into the reactor's cavity along with a coaxial steam flow at a H2O/C molar ratio in the 1.1-7.2 range, and directly exposed to concentrated solar radiation at concentration ratios exceeding 1800 suns. The degree of chemical conversion after a single pass of 1-s residence time attained 50% at 1472 K, producing high quality syngas of composition 68% H-2, 15% CO, 14% CO2, and 2% CH4. The process performance indicators, namely, carbon conversion and energy efficiency were generally inferior to those obtained for the solar steam-gasification of petcoke under comparable operating conditions. (C) 2007 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:679 / 684
页数:6
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