An operability level coefficient (OLC) as a useful tool for correlating the performance of membrane reactors

被引:32
作者
Oyama, S. Ted [1 ]
Lim, Hankwon [1 ]
机构
[1] Virginia Polytech Inst & State Univ, Dept Chem Engn 0211, Environm Catalysis & Nanomat Lab, Blacksburg, VA 24061 USA
基金
美国国家科学基金会;
关键词
Operability level coefficient; Damkohler number; Peclet number; Reforming; Hydrogen; Yield enhancement; Conversion enhancement; Correlation; Modeling; Simulation; HYDROGEN-PRODUCTION; SILICA MEMBRANES; STEAM; METHANOL; PERMEABILITY; PRESSURE; CATALYST; DESIGN; SHIFT; DENSE;
D O I
10.1016/j.cej.2009.04.017
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
An operability level coefficient (OLC), defined as the ratio of product permeation and product formation rates, and related to the inverse combination of the Damkohler number and the Peclet number (1/DaPe), is suggested as a useful tool for estimating performances of membrane reactors (MRs) operating as separators in equilibrium-limited reactions. The OLCs for product hydrogen formation in previously reported MRs for methane dry-reforming (MDR), methane steam-reforming (MSR), methanol steam-reforming (MeOHSR), and ethanol steam-reforming (EtOHSR) were correlated with conversion and yield enhancements. For values of OLCs ranging from 0.03 to 0.78, a clear universal trend for increasing conversions and hydrogen yields with increasing OLC was observed for these different types of reforming reactions. The OLC curve calculated from a numerical simulation without adjustable parameters was found to closely approximate experimental data obtained from the MRs, and was shown not to depend on the assumed kinetics. This study confirms that hydrogen selectivity (from the ratio of single-gas permeances) has a substantial influence on conversion and hydrogen yield enhancements in a MR, and demonstrates that a hydrogen selectivity of 100 is sufficient to achieve high performance in a MR. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:351 / 358
页数:8
相关论文
共 38 条
[1]   USE OF A MEMBRANE REACTOR TO IMPROVE SELECTIVITY TO INTERMEDIATE PRODUCTS IN CONSECUTIVE CATALYTIC REACTIONS [J].
AGARWALLA, S ;
LUND, CRF .
JOURNAL OF MEMBRANE SCIENCE, 1992, 70 (2-3) :129-141
[2]   EFFECT OF REACTION AND PERMEATION RATES ON THE PERFORMANCE OF A CATALYTIC MEMBRANE REACTOR FOR METHYLCYCLOHEXANE DEHYDROGENATION [J].
ALI, JK ;
RIPPIN, DWT .
SEPARATION SCIENCE AND TECHNOLOGY, 1994, 29 (18) :2475-2492
[3]   Synthesis, characterization and gas permeation properties of a silica membrane prepared by high-pressure chemical vapor deposition [J].
Araki, Sadao ;
Mohri, Norito ;
Yoshimitsu, Yuichi ;
Miyake, Yoshikazu .
JOURNAL OF MEMBRANE SCIENCE, 2007, 290 (1-2) :138-145
[4]   A dense Pd/Ag membrane reactor for methanol steam reforming: Experimental study [J].
Basile, A ;
Gallucci, F ;
Paturzo, L .
CATALYSIS TODAY, 2005, 104 (2-4) :244-250
[5]   An analysis of the Peclet and Damkohler numbers for dehydrogenation reactions using molecular sieve silica (MSS) membrane reactors [J].
Battersby, Scott ;
Teixeira, Paula Werneck ;
Beltramini, Jorge ;
Duke, Mikel C. ;
Rudolph, Victor ;
da Costa, Joao C. Diniz .
CATALYSIS TODAY, 2006, 116 (01) :12-17
[6]   MEMBRANE REACTORS FOR CATALYTIC SERIES AND SERIES-PARALLEL REACTIONS [J].
BERNSTEIN, LA ;
LUND, CRF .
JOURNAL OF MEMBRANE SCIENCE, 1993, 77 (2-3) :155-164
[7]  
Birdsell SA, 1997, IECEC-97 - PROCEEDINGS OF THE THIRTY-SECOND INTERSOCIETY ENERGY CONVERSION ENGINEERING CONFERENCE, VOLS 1-4, P1942, DOI 10.1109/IECEC.1997.656723
[8]   WGS reaction in a membrane reactor using a porous stainless steel supported silica membrane [J].
Brunetti, A. ;
Barbieri, G. ;
Drioli, E. ;
Lee, K. -H. ;
Sea, B. ;
Lee, D. -W. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2007, 46 (02) :119-126
[9]   Analysis of intermediate product yield in distributed-feed nonisothermal tubular membrane reactors [J].
Dixon, AG .
CATALYSIS TODAY, 2001, 67 (1-3) :189-203
[10]  
Dixon AG, 2003, INT J CHEM REACT ENG, V1