MATHEMATICAL MODELLING OF STEAM METHANE REFORMING IN A MEMBRANE REACTOR - PRELIMINARY RESULTS
1National Research and Development Institute for Cryogenics and Isotopic Technologies - ICIT Rm. Valcea, code 240050 - Rm. Valcea, Uzinei 4, CP7 Raureni, Valcea, Romania, phone: 0040 250 736979, fax: 0040 250 732746 e-mail:
This e-mail address is being protected from spambots. You need JavaScript enabled to view it
Steam methane reforming is one of the important reactions for production of hydrogen. It accounts for roughly about 48 % of hydrogen produced globally. It is considered that the development of a membrane-based separation process can open up the possibility of increasing the conversion of the reforming process. In this paper a mathematical modeling of a two-dimensional, pseudo-homogeneous and stationary membrane reactor for methane steam reforming was developed in order to obtain some preliminary results regarding the methane conversion. Sievert's law was used to describe the mechanism of hydrogen permeation across the membrane and a CFD code (COMSOL Multiphysics) was applied to analyze the steam methane reforming. KEYWORDS: methane reforming, membrane reactor, multiphysics simulation. |