Hydrogen production by steam-gasification of petroleum coke using concentrated solar power - II - Reactor design, testing, and modeling

被引:160
作者
Z'Graggen, A
Haueter, P
Trommer, D
Romero, M
de Jesus, JC
Steinfeld, A [1 ]
机构
[1] ETH, Swiss Fed Inst Technol, Dept Mech & Proc Engn, CH-8092 Zurich, Switzerland
[2] CIEMAT, E-28040 Madrid, Spain
[3] Intevep SA, PDVSA, Ctr Invest & Apoyo Tecnol Petroleos Venezuela, Caracas 1070A, Venezuela
[4] Paul Scherrer Inst, Solar Technol Lab, CH-5232 Villigen, Switzerland
关键词
D O I
10.1016/j.ijhydene.2005.06.011
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 solar chemical reactor technology for the steam-gasification of petcoke is presented. The reactor features a continuous vortex flow of steam laden with petcoke particles confined to a cavity receiver and directly exposed to concentrated solar radiation. A 5 kW prototype reactor tested in a high-flux solar furnace in the range 1300-1800 K yielded up to 87% petcoke conversion in a single pass of 1 s residence time. The solar-to-chemical energy conversion efficiency attained 9% without accounting for the product's sensible heat, and 20% when the sensible heat is recovered for steam generation and pre-heating. A steady-state process model that couples radiative heat transfer with the reaction kinetics is validated with experimental data and used for optimization and scale-up of the reactor design. (c) 2005 Intemational Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:797 / 811
页数:15
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