{"id":6647,"date":"2026-08-16T22:28:07","date_gmt":"2026-08-16T14:28:07","guid":{"rendered":"\/jase\/?post_type=tkuisotope&#038;p=6647"},"modified":"2026-08-23T16:40:27","modified_gmt":"2026-08-23T08:40:27","slug":"multi-objective-optimization-of-mixed-membrane-reactors-for-autothermal-reforming-of-methane","status":"publish","type":"tkuisotope","link":"\/jase\/?tkuisotope=multi-objective-optimization-of-mixed-membrane-reactors-for-autothermal-reforming-of-methane","title":{"rendered":"Multi-objective Optimization of Mixed Membrane Reactors for Autothermal Reforming of Methane"},"content":{"rendered":"\n<div class=\"wp-block-tkuwpbs5-bs5-row row article-info\">\n<div class=\"wp-block-tkuwpbs5-bs5-column col-md-3 align-self-start\">\n<p><i class=\"fa fa-folder\" aria-hidden=\"true\"><\/i>&nbsp;<a href=\"\/jase\/?page_id=6588\" data-type=\"page\" data-id=\"807\">2018<\/a><\/p>\n<\/div>\n\n\n\n<div class=\"wp-block-tkuwpbs5-bs5-column col-md-3 align-self-start\">\n<p><i class=\"fa fa-folder-open\" aria-hidden=\"true\"><\/i>&nbsp;<a href=\"\/jase\/?page_id=6626\" data-type=\"page\" data-id=\"4630\">Volume 21, Issue 3<\/a><\/p>\n<\/div>\n\n\n\n<div class=\"wp-block-tkuwpbs5-bs5-column col-md-6 align-self-start\">\n<div class=\"wp-block-tkuwpbs5-bs5-div dv_publish\" data-aos=\"normal\"><div class=\"wp-block-post-date\"><time datetime=\"2026-08-16T22:28:07+08:00\">2026-08-16<\/time><\/div><\/div>\n<\/div>\n<\/div>\n\n\n\n<div class=\"wp-block-tkuwpbs5-bs5-row row\">\n<div class=\"wp-block-tkuwpbs5-bs5-column col-md-5 align-self-start\">\n<div class=\"wp-block-tkuwpbs5-bs5-div au-ol\" data-aos=\"normal\">\n<p>Hsuan Chang<a href=\"mailto:nhchang@mail.tku.edu.tw\"><i class=\"fa fa-envelope\"><\/i><\/a>, Yih-Hung Chen, Yun-Tsz Chen, Chii-Dong Ho<\/p>\n\n\n\n<p style=\"font-size:14px\">Department of Chemical and Materials Engineering, Tamkang University, Tamsui, Taiwan 251, R.O.C.<\/p>\n<\/div>\n\n\n\n<div class=\"wp-block-tkuwpbs5-bs5-div\" style=\"margin-top:var(--wp--preset--spacing--40)\" data-aos=\"normal\">\n<p>Received:\u00a0December 18, 2017<br>Accepted:\u00a0March 9, 2018<br>Publication Date:\u00a0August 16, 2018<\/p>\n<\/div>\n<\/div>\n\n\n\n<div class=\"wp-block-tkuwpbs5-bs5-column col-md-7 align-self-start clk=\u5716\u7247\"><img decoding=\"async\" src=\"\/jase\/wp-content\/uploads\/2026\/08\/21_3_20.jpg\" class=\"img-fluid img-fluid mx-auto d-block\" alt=\"\u4e0a\u50b3\u5716\u7247\">\n\n\n<p class=\"has-text-align-center\">Schematic illustrations of (a) membrane reactor (MR) and (b) mixed membrane reactor (MMR) for autothermal reforming (ATR) of methane.<\/p>\n<\/div>\n<\/div>\n\n\n\n<p class=\"has-small-font-size\"><i class=\"fab fa-creative-commons\"><\/i>&nbsp;<strong>Copyright&nbsp;<\/strong>The Author(s). This is an open access article distributed under the terms of the&nbsp;<a rel=\"noreferrer noopener\" href=\"https:\/\/creativecommons.org\/licenses\/by\/4.0\/\" target=\"_blank\">Creative Commons Attribution&nbsp;License (CC BY 4.0)<\/a>, which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are cited.<\/p>\n\n\n\n<p>Download Citation:&nbsp; <a href=\"\/jase\/wp-content\/uploads\/2026\/08\/V213.0020.bib\" data-type=\"attachment\" data-id=\"10020\" target=\"_blank\" rel=\"noreferrer noopener\">BibTeX <\/a>| <a href=\"http:\/\/dx.doi.org\/10.6180\/jase.201809_21(3).0020\" target=\"_blank\" rel=\"noreferrer noopener\">http:\/\/dx.doi.org\/10.6180\/jase.201809_21(3).0020<\/a>&nbsp;&nbsp;<\/p>\n\n\n\n<p class=\"btn btn-primary article-btn\"><a href=\"\/jase\/wp-content\/uploads\/2026\/08\/20-10608_0305_V21i3.pdf\" data-type=\"attachment\" data-id=\"10059\" target=\"_blank\" rel=\"noreferrer noopener\">Download PDF<\/a><\/p>\n\n\n\n<div style=\"height:24px\" aria-hidden=\"true\" class=\"wp-block-spacer\"><\/div>\n\n\n\n<p>Autothermal reforming (ATR) of methane, which supplies the heat for endothermic steam reforming by internal combustion of methane, is an important process for synthetic gas production. The axial-distributed feeding of oxygen via a packed bed inert membrane reactor (MR) can reduce the peak temperature and improve the reactor performance. A modified MR, called mixed membrane reactor (MMR), combines permeable membrane tube wall and non-permeable tube wall provides extra degrees of freedom for reactor design and operation. For MR and MMR, this study presents the ternary-objective optimization analysis for maximizing hydrogen production rate, non-combustion selectivity and conversion of methane, using a 1D pseudo-homogeneous reactor model and the NSGA-II algorithm. Compared to MR, MMR can be operated under significantly higher oxygen permeation flux without violating the maximum temperature constraint. The non-combustion selectivity and conversion of methane of MR and MMR are close, however, the hydrogen production rate of MMR can be as high as 200% of MR.<\/p>\n\n\n\n<p><em>Keywords:&nbsp;Methane Reforming; Membrane Reactor; Mixed Membrane Reactor; Multi-objective Optimization<\/em><\/p>\n\n\n\n<div style=\"height:2rem\" aria-hidden=\"true\" class=\"wp-block-spacer\"><\/div>\n\n\n\n<div class=\"wp-block-tkuwpbs5-bs5-div ref_ol\" data-aos=\"normal\">\n<ol>\n<li>[1] Ulber, D., &#8220;A Guide to Methane Reforming,&#8221; Chemical Engineering, January, pp. 40-46 (2015).<\/li>\n<li>[2] Rice, S. F. and Mann, D. P., Autothermal Reforming of Natural Gas to Synthesis Gas, SAND2007-2331, Sandia National Laboratories, U.S. Department of Commerce (2007).<\/li>\n<li>[3] Marcano, J. G. S. and Tsotsis, T. T., Catalytic Membranes and Membrane Reactors, Wiley-VCH Verlag GmbH, Weinheim Germany (2002).<\/li>\n<li>[4] Coronas, J. and Santamaria, J., &#8220;Catalytic Reactors Based on Porous Ceramic Membranes,&#8221; Catalysis Today, Vol. 51, pp. 377-389 (1999). doi: 10.1016\/S0920-5861(99)00090-5<\/li>\n<li>[5] Rodr\u00edguez, M. L., Ardissone, D. E., Opez, E. L., Pedernera, M. N. and Borio, D. O., &#8220;Reactor Designs for Ethylene Production via Ethane Oxidative Dehydrogenation: Comparison of Performance,&#8221; Industrial and Engineering Chemistry Research, Vol. 50, pp. 2690-2697 (2011). doi: 10.1021\/ie100738q<\/li>\n<li>[6] Rodriguez, M. L., Pedernera, M. N. and Borio, D. O., &#8220;Two Dimensional Modeling of a Membrane Reactor for ATR of Methane,&#8221; Catalysis Today, Vol. 193, pp. 137-144 (2012). doi: 10.1016\/j.cattod.2012.04.010<\/li>\n<li>[7] Coronas, J., Men\u00e9ndez, M. and Santamar\u00eda, J., &#8220;Use of a Ceramic Membrane Reactor for the Oxidative Dehydrogenation of Ethane to Ethylene and Higher Hydrocarbons,&#8221; Industrial and Engineering Chemistry Research, Vol. 34, pp. 4229-4234 (1995). doi: 10.1021\/ie00039a011<\/li>\n<li>[8] \u00c1vila-Neto, C. N., Dantas, S. C., Silva, F. A., Franco, T. V., Romanielo, L. L., Hori, C. E. and Assis, A. J., &#8220;Hydrogen Production from Methane Reforming: Thermodynamic Assessment and Autothermal Reactor Design,&#8221; Journal of Natural Gas Science and Engineering, Vol. 1, pp. 205-215 (2009). doi: 10.1016\/j.jngse.2009.12.003<\/li>\n<li>[9] Sinaei Nobandegani, M., Sardashti Birjandi, M. R., Darbandi, T., Khalilipour, M. M., Shahraki, F. and Mohebbi-Kalhori, D., &#8220;An Industrial Steam Methane Reformer Optimization Using Response Surface Methodology,&#8221; Journal of Natural Gas Science and Engineering, Vol. 36, pp. 540-549 (2016). doi: 10.1016\/j.jngse.2016.10.031<\/li>\n<li>[10] Shahhosseini, H. R., Farsi, M. and Eini, S., &#8220;Multi-objective Optimization of Industrial Membrane SMR to Produce Syngas for Fischer-Tropsch Production Using NSGA-II and Decision Makings,&#8221; Journal of Natural Gas Science and Engineering, Vol. 32, pp. 222-238 (2016). doi: 10.1016\/j.jngse.2016.04.005<\/li>\n<li>[11] Deb, K., Patap, A., Agarwal, S. and Meyarivan, T., &#8220;A Fast and Elitist Multiobjective Genetic Algorithm: NSGA-II,&#8221; IEEE Transactions on Evolutionary Computation, Vol. 6, pp. 182-197 (2002). doi: 10.1109\/4235.996017<\/li>\n<li>[12] De Groote, A. M. and Froment, G. F., &#8220;Simulation of the Catalytic Partial Oxidation of Methane to Synthesis Gas,&#8221; Applied Catalysis A: General, Vol. 138, pp. 245-264 (1996). doi: 10.1016\/0926-860X(95)00299-5<\/li>\n<li>[13] Ergun, S., &#8220;Fluid Flow through Packed Columns,&#8221; Chem. Eng. Prog., Vol. 48, pp. 89-94 (1952).<\/li>\n<li>[14] Xu, J. and Froment, G. F., &#8220;Methane Steam Reforming, Methanation and Water-gas Shift: I. Intrinsic Kinetics,&#8221; AIChE Journal, Vol. 35, pp. 88-96 (1989). doi: 10.1002\/aic.690350109<\/li>\n<li>[15] Mallada, R., Pedernera, M., Men\u00e9ndez, M. and Santamaria, J., &#8220;Synthesis of Maleic Anhydride in an Inert Membrane Reactor. Effect of Reactor Configuration,&#8221; Industrial and Engineering Chemistry Research, Vol. 39, pp. 620-625 (2000). doi: 10.1021\/ie9905310<\/li>\n<li>[16] Pedernera, M., Mallada, R., Men\u00e9ndez, M. and Santamaria, J., &#8220;Simulation of an Inert Membrane Reactor for the Synthesis of Maleic Anhydride,&#8221; AICHE Journal, Vol. 46, pp. 2489-2498 (2000). doi: 10.1002\/aic.690461215<\/li>\n<li>[17] Rodriguez, M. L., Ardissone, D. E., Lemonidou, A. A., Heracleous, E., L\u00f3pez, E., Pedernera, M. N. and Borio, D. O., &#8220;Simulation of a Membrane Reactor for the Catalytic Oxidehydrogenation of Ethane,&#8221; Industrial and Engineering Chemistry Research, Vol. 48, pp. 1090-1095 (2009). doi: 10.1021\/ie800564v<\/li>\n<li>[18] Froment, G. F. and Bischoff, K. B., Chemical Reactor Analysis and Design, Wiley, New York, USA (1990).<\/li>\n<\/ol>\n<\/div>\n\n\n\n<p><\/p>\n","protected":false},"author":3,"template":"wp-custom-template-detail-4-aricles","meta":{"_uag_custom_page_level_css":""},"categories":[1361,6,1364],"tags":[1417],"acf":[],"uagb_featured_image_src":[],"uagb_author_info":{"display_name":"\u6797\u923a\u6db5","author_link":"\/jase\/?author=3"},"uagb_comment_info":0,"uagb_excerpt":"&nbsp;Copyright&nbsp;The Author(s). This is an open access article distributed under the terms of the&nbsp;Creative Commons Attribution&nbsp;License (CC BY 4.0), which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are cited. Download Citation:&nbsp; BibTeX | http:\/\/dx.doi.org\/10.6180\/jase.201809_21(3).0020&nbsp;&nbsp; Download PDF Autothermal reforming (ATR) of methane, which supplies the heat for endothermic&hellip;","_links":{"self":[{"href":"\/jase\/index.php?rest_route=\/wp\/v2\/tkuisotope\/6647"}],"collection":[{"href":"\/jase\/index.php?rest_route=\/wp\/v2\/tkuisotope"}],"about":[{"href":"\/jase\/index.php?rest_route=\/wp\/v2\/types\/tkuisotope"}],"author":[{"embeddable":true,"href":"\/jase\/index.php?rest_route=\/wp\/v2\/users\/3"}],"wp:attachment":[{"href":"\/jase\/index.php?rest_route=%2Fwp%2Fv2%2Fmedia&parent=6647"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"\/jase\/index.php?rest_route=%2Fwp%2Fv2%2Fcategories&post=6647"},{"taxonomy":"post_tag","embeddable":true,"href":"\/jase\/index.php?rest_route=%2Fwp%2Fv2%2Ftags&post=6647"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}