Performance comparison of two combined SOFC-gas turbine systems

被引:68
作者
Granovskii, Mikhail [1 ]
Dincer, Ibrahim [1 ]
Rosen, Marc A. [1 ]
机构
[1] Univ Ontario, Inst Technol, Fac Engn & Appl Sci, Oshawa, ON L1H 7K4, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
solid oxide fuel cell; energy; exergy; efficiency; hydrogen; gas turbine cycle;
D O I
10.1016/j.jpowsour.2006.11.069
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 necessary step in the use of natural gas (methane) in solid oxide fuel cells (SOFCs) is its preliminary conversion to hydrogen and carbon monoxide. To perform methane conversion within fuel cells and avoid catalyst carbonization the molar ratio between methane and steam (or steam with carbon dioxide) should be 1:2 or higher at the SOFC inlet. In this article two possible technological approaches to provide this desirable ratio in a combined SOFC-gas turbine system are compared. The first approach involves generation of the required steam in the coupled gas turbine cycle. The second (which is more traditional) involves recycling some part of the exhaust gases around the anodes of the SOFC stack. Exergy and energy analyses for the two SOFC-gas turbine systems are conducted to determine their efficiencies and capabilities to generate power at different rates of oxygen conductivity through the SOFC electrolyte (ion conductive membrane), as well as various efficiencies for natural gas conversion to electricity in the SOFC stack. It is determined that with a fixed SOFC stack the scheme with recycling has higher exergy and energy efficiencies (requiring less natural gas for a fixed electricity output) and the scheme with steam generation is associated with a higher capability for power generation. The question of which scheme permits a higher reduction in natural gas consumption (per unit of time), in the case of its implementation instead of a contemporary combined gas turbine-steam power cycle is considered. The greater capability of power generation while retaining high efficiency of fuel consumption in the scheme with steam generation makes its implementation more favorable. This scheme provides a better relative reduction in natural gas consumption (relative to the scheme with exhaust gas recycling) calculated per unit of time which reaches values of about 20%. At higher values of oxygen conductivity and efficiency of natural gas conversion to electricity in the SOFC stack this relative reduction becomes less significant, remaining in the range of 3-8%. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:307 / 314
页数:8
相关论文
共 15 条
[1]  
[Anonymous], ENG THERMODYNAMICS
[2]   Thermodynamic model and parametric analysis of a tubular SOFC module [J].
Campanari, S .
JOURNAL OF POWER SOURCES, 2001, 92 (1-2) :26-34
[3]  
Cengel Y. A., 2005, FUNDAMENTALS THERMAL
[4]   Advances in catalysts for internal reforming in high temperature fuel cells [J].
Dicks, AL .
JOURNAL OF POWER SOURCES, 1998, 71 (1-2) :111-122
[5]   SOFC system and technology [J].
Dokiya, M .
SOLID STATE IONICS, 2002, 152 :383-392
[6]   Conceptual study of a 250 kW planar SOFC system for CHP application [J].
Fontell, E ;
Kivisaari, T ;
Christiansen, N ;
Hansen, JB ;
Pålsson, J .
JOURNAL OF POWER SOURCES, 2004, 131 (1-2) :49-56
[7]  
GRANOVSKII M, 2007, IN PRESS ASME
[8]   Application of oxygen ion-conductive membranes for simultaneous electricity and hydrogen generation [J].
Granovskii, Mikhail ;
Dincer, Ibrahim ;
Rosen, Marc A. .
CHEMICAL ENGINEERING JOURNAL, 2006, 120 (03) :193-202
[9]   Fuel cell materials and components [J].
Haile, SM .
ACTA MATERIALIA, 2003, 51 (19) :5981-6000
[10]   Exergy analysis with a flowsheeting simulator .2. Application; Synthesis gas production from natural gas [J].
Hinderink, AP ;
Kerkhof, FPJM ;
Lie, ABK ;
Arons, JD ;
vanderKooi, HJ .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (20) :4701-4715