SORPTION-ENHANCED STEAM METHANE REFORMING (SE-SMR) - A REVIEW: REACTOR TYPES, CATALYST AND SORBENT CHARACTERIZATION, PROCESS MODELING

被引：16
作者：
Cherbanski, Robert [1 ]
Molga, Eugeniusz [1 ]
机构：
[1] Warsaw Univ Technol, Fac Chem & Proc Engn, Ul Warynskiego 1, PL-00645 Warsaw, Poland
来源：
CHEMICAL AND PROCESS ENGINEERING-INZYNIERIA CHEMICZNA I PROCESOWA | 2018年 / 39卷 / 04期
关键词：
reactive adsorption; adsorptive reactors; reactor modeling; sorption-enhanced reaction process (SERP); steam methane reforming (SMR); FLUIDIZED-BED REACTORS; TRICKLE FLOW REACTOR; DIMENSIONAL 2-FLUID MODEL; SITU CO2 REMOVAL; HYDROGEN-PRODUCTION; HIGH-TEMPERATURE; CARBON-DIOXIDE; H-2; PRODUCTION; FLY ASHES; PROCESS PERFORMANCE;
D O I：
10.24425/122961
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
In this review, research carried out on sorption-enhanced steam methane reforming (SESMR) process is presented and discussed. The reactor types employed to carry out this process, fixed packed bed and fluidized bed reactors, are characterized as well as their main operating conditions indicated. Also the concepts developed and investigations performed by the main research groups involved in the subject are summarized. Next the catalysts and CO2 sorbents developed to carry out SE-SMR are characterized and the relationships describing the reaction and sorption kinetics are collected. A general approach to model the process is presented as well as results obtained for a calculation example, which demonstrate the main properties of SE-SMR.
引用
收藏
页码：427 / 448
页数：22
相关论文
共 89 条
[1]  
Agar DW, 2005, INTEGRATED CHEMICAL PROCESSES: SYNTHESIS, OPERATION, ANALYSIS, AND CONTROL, P203, DOI 10.1002/3527605738.ch7
[2]   Hydrogen by sorption enhanced methane reforming: A grain model to study the behavior of bi-functional sorbent-catalyst particles [J].
Aloisi, Ilaria ;
Jand, Nader ;
Stendardo, Stefano ;
Foscolo, Pier Ugo .
CHEMICAL ENGINEERING SCIENCE, 2016, 149 :22-34
[3]  
[Anonymous], REACTIVE ADSORPTION
[4]  
[Anonymous], 2012, Energy Technology Perspectives 2012: Pathways to a Clean Energy System
[5]   Hydrogen from methane in a single-step process [J].
Balasubramanian, B ;
Ortiz, AL ;
Kaytakoglu, S ;
Harrison, DP .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (15-16) :3543-3552
[6]   Sorption-enhanced Fischer-Tropsch synthesis with continuous adsorbent regeneration in GTL technology: Modeling and optimization [J].
Bayat, M. ;
Hamidi, M. ;
Dehghani, Z. ;
Rahimpour, M. R. .
JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2014, 20 (03) :858-869
[7]   An appraisal of the heat transfer properties of metallic open-cell foams for strongly exo-/endo-thermic catalytic processes in tubular reactors [J].
Bianchi, Enrico ;
Heidig, Tobias ;
Visconti, Carlo Giorgio ;
Groppi, Gianpiero ;
Freund, Hannsjoerg ;
Tronconi, Enrico .
CHEMICAL ENGINEERING JOURNAL, 2012, 198 :512-528
[8]   Sorption-enhanced reaction process [J].
Carvill, BT ;
Hufton, JR ;
Anand, M ;
Sircar, S .
AICHE JOURNAL, 1996, 42 (10) :2765-2772
[9]   Simulation of Methane Steam Reforming Enhanced by in Situ CO2 Sorption Using K2CO3-Promoted Hydrotalcites for H2 Production [J].
Chanburanasiri, Naruewan ;
Ribeiro, Ana M. ;
Rodrigues, Alirio E. ;
Laosiripojana, Navadol ;
Assabumrungrat, Suttichai .
ENERGY & FUELS, 2013, 27 (08) :4457-4470
[10]   Hydrogen Production via Sorption Enhanced Steam Methane Reforming Process Using Ni/CaO Multifunctional Catalyst [J].
Chanburanasiri, Naruewan ;
Ribeiro, Ana M. ;
Rodrigues, Alirio E. ;
Arpornwichanop, Amornchai ;
Laosiripojana, Navadol ;
Praserthdam, Piyasan ;
Assabumrungrat, Suttichai .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (24) :13662-13671
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