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首页> 外文期刊>Journal of Membrane Science >Simulating catalytic membrane reactors using orthogonal collocation with spatial coordinates transformation
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Simulating catalytic membrane reactors using orthogonal collocation with spatial coordinates transformation

机译:使用空间搭配变换正交搭配模拟催化膜反应器

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It is presented in this study a new numerical scheme using orthogonal collocation together with an independent variable (spatial coordinate) transformation, useful for solving the model equations associated to membrane reactors with catalytic membranes. This new scheme takes advantage of a noticeable feature of the concentration profile inside a catalytic membrane: close to the membrane surfaces, this profile becomes steeper and steeper with the Thiele modulus.Using traditional numerical methods for solving the model equations of a catalytic membrane reactor, namely finite differences with equispaced intervals or orthogonal collocation, for example, may lead to imprecise results. In order to illustrate the ability of this new numerical scheme for solving such equations, it is applied to the resolution of a case where an analytical solution is available (a generic A reversible arrow B reaction carried out in a catalytic membrane with perfectly mixed flow pattern in both retentate and permeate sides). Then, the same numerical scheme is used for solving a model describing the cyclohexane dehydrogenation, A reversible arrow B + 3C, carried out in a porous membrane with the same flow pattern as above-and the results are compared with the ones obtained using an adaptive wavelet-based method. For these two models, solutions were also obtained using straight orthogonal collocation and finite differences with homogeneously distributed grid points for the sake of the comparison. The results show that the new numerical approach is useful in dealing with this kind of problems, especially for high Thiele modulus values, showing high accuracy and demanding low computation time. Finally, this new scheme is applied to the resolution of a more complex model: a generic reaction 2Areversible arrowB, carried out in a dense catalytic cylindrical membrane with plug-flow pattern for both retentate and permeate sides. (C) 2004 Elsevier B.V. All rights reserved.
机译:在这项研究中提出了一种使用正交搭配以及自变量(空间坐标)变换的新数值方案,可用于求解与带有催化膜的膜反应器相关的模型方程。这种新方案利用了催化膜内部浓度分布的显着特征:靠近膜表面,该分布随着Thiele模量变得越来越陡。使用传统的数值方法求解催化膜反应器的模型方程,例如,等间隔或正交搭配的有限差异可能会导致结果不精确。为了说明这种新的数值方案求解此类方程式的能力,将其应用于有分析溶液可用的情况的解析(在具有完美混合流型的催化膜中进行的通用A可逆箭头B反应)在渗余物和渗透物两方面)。然后,使用相同的数值方案求解描述环己烷脱氢的模型,在具有与上述相同流型的多孔膜中进行可逆箭头B + 3C,并将结果与​​使用自适应方法获得的结果进行比较。基于小波的方法。对于这两个模型,为了进行比较,还使用直线正交搭配和具有均匀分布网格点的有限差分获得了解决方案。结果表明,新的数值方法对于解决此类问题特别有用,特别是对于高Thiele模量值,显示精度高且计算时间要求低的问题。最后,该新方案适用于更复杂的模型的解析:通用反应2Areversible arrowB,该反应在密实的催化圆柱形膜中进行,对于滞留物和渗透物侧均采用塞流模式。 (C)2004 Elsevier B.V.保留所有权利。

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