Autothermal Reforming of Ethanol for Hydrogen Production: Modeling and Simulation

被引:7
作者
Wutthithanyawat, Chananchai [1 ]
Srisiriwat, Nawadee
机构
[1] Pathumwan Inst Technol, Dept Instrumentat & Control Engn, Fac Engn, Bangkok 10330, Thailand
来源
ENGINEERING AND MANUFACTURING TECHNOLOGIES | 2014年 / 541-542卷
关键词
Autothermal reforming; Ethanol; Hydrogen production; Modeling; Simulation; REACTOR; METHANE;
D O I
10.4028/www.scientific.net/AMM.541-542.108
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
Autothermal reforming (ATR), which is the combination of endothermic steam reforming and exothermic partial oxidation, is an attractive process to produce hydrogen using for transportation fuel cell because of its moderate size. ATR is considered to be thermally self-sustaining that the external heat source is not required. In order to keep the adiabatic temperature of ATR reactor, the process control strategy needs in understanding the dynamic characteristics of the ATR system. Thus, the modeling and simulation of ATR process for hydrogen production fueled by ethanol is carried out in this work. The open loop responses of the feed and ATR temperatures are simulated by the dynamic models of ATR system. The simulation results showed the predominantly influence of the electrical power of preheater on the feed and ATR temperatures while the air flowrate has an inverse effect on the feed temperature and a direct effect on the ATR temperature. As a result, the match of control loop is very sensible for an effective control strategy in the development of control system design for maintaining the adiabatic temperature of ATR reactor for sustaining the effectiveness of hydrogen production.
引用
收藏
页码:108 / +
页数:2
相关论文
共 14 条
[1]   Thermodynamic and kinetic modelling of an autothermal methanol reformer [J].
Chan, SH ;
Wang, HM .
JOURNAL OF POWER SOURCES, 2004, 126 (1-2) :8-15
[2]  
Chen J., 2007, P 46 IEEE C DEC CONT, P4608
[3]   Optimization of autothermal reactor for maximum hydrogen production [J].
Hagh, BF .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2003, 28 (12) :1369-1377
[4]   Modeling and analysis of autothermal reforming of methane to hydrogen in a fixed bed reformer [J].
Halabi, M. H. ;
de Croon, M. H. J. M. ;
van der Schaaf, J. ;
Cobden, P. D. ;
Schouten, J. C. .
CHEMICAL ENGINEERING JOURNAL, 2008, 137 (03) :568-578
[5]   Autothermal reforming of gasoline for fuel cell applications: Controller design and analysis [J].
Hu, Yongyou ;
Chmielewski, Donald J. ;
Papadias, Dennis .
JOURNAL OF POWER SOURCES, 2008, 182 (01) :298-306
[6]  
Ipsakis D., 2009, P 17 MED C CONTR AUT, P1421
[7]   Autothermal reforming of methane to synthesis gas: Modeling and simulation [J].
Nezhad, M. Zahedi ;
Rowshanzamir, S. ;
Eikani, M. H. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (03) :1292-1300
[8]   Reactor concept for improved heat integration in autothermal methanol reforming [J].
Schildhauer, T. J. ;
Geissler, K. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (12) :1806-1810
[9]   Equilibrium products from autothermal processes for generating hydrogen-rich fuel-cell feeds [J].
Semelsberger, TA ;
Brown, LF ;
Borup, RL ;
Inbody, MA .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2004, 29 (10) :1047-1064
[10]   Evaluation of thermodynamically favourable operating conditions for production of hydrogen in three different reforming technologies [J].
Seo, YS ;
Shirley, A ;
Kolaczkowski, ST .
JOURNAL OF POWER SOURCES, 2002, 108 (1-2) :213-225