REVIEW OF SIMULATION METHODS OF THE DISTILLATION COLUMN AND THERMODYNAMIC MODELS IN THE HI DECOMPOSITION SECTION OF THE IODINE-SULFUR PROCESS

被引:10
作者
Guo, Hanfei [1 ]
Zhang, Ping [1 ]
Chen, Songzhe [1 ]
Wang, Laijun [1 ]
Xu, Jingming [1 ]
机构
[1] Tsinghua Univ, Inst Nucl & New Energy Technol, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
Thermodynamic models; Simulation; Iodine-sulfur process; Parameter analysis; Hydrogen production; HI distillation; VAPOR-LIQUID-EQUILIBRIA; EXCESS GIBBS ENERGY; THERMOCHEMICAL HYDROGEN-PRODUCTION; HI-I-2-H2O TERNARY MIXTURES; LOCAL COMPOSITION MODEL; WATER-SPLITTING CYCLE; ELECTROLYTE SYSTEMS; REACTIVE DISTILLATION; HYDRIODIC ACID; PRESSURE;
D O I
10.1080/00986445.2013.790814
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The iodine-sulfur thermochemical water-splitting process (I-S process) is one of the most promising and efficient mass hydrogen production methods without greenhouse gas emissions. To a large extent, distillation in the HI decomposition section of the I-S process affects the efficiency of the entire process. This article summarizes the simulation methods for HI distillation in the iodine-sulfur process, including thermodynamic models, design schemes, and parameter analyses. The performance of the thermodynamic models and heat duties of different flow sheets were compared, and the preferable model and flow sheet are recommended. This study can provide a reference for the selection of thermodynamic models and it is also meaningful for the design and simulation of the HI distillation column.
引用
收藏
页码:751 / 789
页数:39
相关论文
共 66 条
[1]   STATISTICAL THERMODYNAMICS OF LIQUID-MIXTURES - NEW EXPRESSION FOR EXCESS GIBBS ENERGY OF PARTLY OR COMPLETELY MISCIBLE SYSTEMS [J].
ABRAMS, DS ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1975, 21 (01) :116-128
[2]   Vapour reactive distillation process for hydrogen production by HI decomposition from HI-I2-H2O solutions [J].
Belaissaoui, B. ;
Thery, R. ;
Meyer, X. M. ;
Meyer, M. ;
Gerbaud, V. ;
Joulia, X. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2008, 47 (03) :396-407
[3]   EXPERIMENTAL INVESTIGATIONS OF THERMAL HI DECOMPOSITION FROM H2O-HI-I2 SOLUTIONS [J].
BERDHAUSER, C ;
KNOCHE, KF .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1994, 19 (03) :239-244
[4]  
Berry G., 2004, ENCY ENERGY, VCutler J, P253
[5]  
Borgard J., 2003, 1 EUR HYDR EN C GREN
[6]  
Brown LC., 2003, GAA24285
[7]   LOCAL COMPOSITION MODEL FOR EXCESS GIBBS ENERGY OF ELECTROLYTE SYSTEMS .1. SINGLE SOLVENT, SINGLE COMPLETELY DISSOCIATED ELECTROLYTE SYSTEMS [J].
CHEN, CC ;
BRITT, HI ;
BOSTON, JF ;
EVANS, LB .
AICHE JOURNAL, 1982, 28 (04) :588-596
[8]   A LOCAL COMPOSITION MODEL FOR THE EXCESS GIBBS ENERGY OF AQUEOUS-ELECTROLYTE SYSTEMS [J].
CHEN, CC ;
EVANS, LB .
AICHE JOURNAL, 1986, 32 (03) :444-454
[9]   Conceptual design of sulfur-iodine hydrogen production cycle of Korea Institute of Energy Research [J].
Cho, Won-Chul ;
Park, Chu-Sik ;
Kang, Kyoung-Soo ;
Kim, Chang-Hee ;
Bae, Ki-Kwang .
NUCLEAR ENGINEERING AND DESIGN, 2009, 239 (03) :501-507
[10]  
Daniele G., 1960, Gazz. Chim. Ital, V90, P1068