Modeling of autothermal methane steam reforming: Comparison of reactor configurations

被引:31
作者
Murmura, M. A. [1 ]
Diana, M. [1 ]
Spera, R. [1 ]
Annesini, M. C. [1 ]
机构
[1] Sapienza Univ Roma, Dipartimento Ingn Chim Mat Ambiente, Via Eudossiana 18, I-00184 Rome, Italy
关键词
Methane; Thermally coupled; Autothermal; Steam reforming; Modeling; MIXED MATRIX MEMBRANES; FIXED-BED REACTORS; HYDROGEN-PRODUCTION; CERAMIC MEMBRANES; PURE HYDROGEN; SIMULATION; KINETICS; GAS; BA0.5SR0.5CO0.8FE0.2O3-DELTA; COMBUSTION;
D O I
10.1016/j.cep.2016.08.019
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In the present work, two systems for the coupling of methane steam reforming and methane combustion have been studied and compared. In the first system considered, the two reactions are thermally coupled but take place in separate volumes. Particular attention has been placed on the choice of operating conditions in order to maximize the efficiency and safety of the process. The second system considered consists in a modification of the process of autothermal reforming, distributing the oxygen feed to the reactor along its axis. The results obtained have been compared with the performance of a reactor in which the oxidation reaction is carried out by injecting oxygen in different points along the reactor. The performance of the two systems has been compared with that of an autothermal reformer, in which the entire oxygen feed is mixed with steam and methane entering the reactor. The analysis of the different systems has focused on the temperature profiles that develop within the reactors, the amount of hydrogen produced per mole of methane fed, and the possibility of carrying out the process without entering flammability limits. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:125 / 135
页数:11
相关论文
共 31 条
[1]   A comparative study of two different configurations for exothermic-endothermic heat exchanger reactor [J].
Bayat, M. ;
Rahimpour, M. R. ;
Taheri, M. ;
Pashaei, M. ;
Sharifzadeh, S. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2012, 52 :63-73
[2]   Energy and mass intensities in hydrogen upgrading by a membrane reactor [J].
Brunetti, Adele ;
Drioli, Enrico ;
Barbieri, Giuseppe .
FUEL PROCESSING TECHNOLOGY, 2014, 118 :278-286
[3]   Mathematical Modeling of Hydrogen Production via Methanol-Steam Reforming with Heat-Coupled and Membrane-Assisted Reactors [J].
Chein, Rei-Yu ;
Chen, Yen-Cho ;
Chung, Jacob Nan-Chu .
CHEMICAL ENGINEERING & TECHNOLOGY, 2014, 37 (11) :1907-1918
[4]   Zeolite-Filled Porous Mixed Matrix Membranes for Air Separation [J].
Chen, Jung-Tsai ;
Shih, Chien-Chung ;
Fu, Ywu-Jang ;
Huang, Shu-Hsien ;
Hu, Chien-Chieh ;
Lee, Kueir-Rarn ;
Lai, Juin-Yih .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (07) :2781-2789
[5]   Design of adiabatic fixed-bed reactors for the partial oxidation of methane to synthesis gas. Application to production of methanol and hydrogen-for-fuel-cells [J].
de Smet, CRH ;
de Croon, MHJM ;
Berger, RJ ;
Marin, GB ;
Schouten, JC .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (16) :4849-4861
[6]   Autothermal Reforming of Methane with Integrated CO2 Capture in a Novel Fluidized Bed Membrane Reactor. Part 1: Experimental Demonstration [J].
Gallucci, F. ;
Annaland, M. Van Sint ;
Kuipers, J. A. M. .
TOPICS IN CATALYSIS, 2008, 51 (1-4) :133-145
[7]   Analysis of a novel reverse-flow reactor concept for autothermal methane steam reforming [J].
Glöckler, B ;
Kolios, G ;
Eigenberger, G .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (3-6) :593-601
[8]   Dual-membrane reactor for methane oxidative coupling and dry methane reforming: Reactor integration and process intensification [J].
Godini, H. R. ;
Xiao, S. ;
Kim, M. ;
Goerke, O. ;
Song, S. ;
Wozny, G. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2013, 74 :153-164
[9]   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
[10]   Modeling of a catalytic autothermal methane reformer for fuel cell applications [J].
Hoang, DL ;
Chan, SH .
APPLIED CATALYSIS A-GENERAL, 2004, 268 (1-2) :207-216