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钯基膜的 Sieverts 定律经验指数:纯氢气渗透中的临界分析。

Sieverts law empirical exponent for Pd-based membranes: critical analysis in pure H2 permeation.

机构信息

Institute on Membrane Technology (ITM-CNR), National Research Council, c/o The University of Calabria, Cubo 17C, Via Pietro Bucci, 87036 Rende CS, Italy.

出版信息

J Phys Chem B. 2010 May 13;114(18):6033-47. doi: 10.1021/jp1006582.

Abstract

In this paper, the physical meaning of the Sieverts-type driving force exponent n is analyzed for hydrogen permeation through Pd-based membranes by considering a complex model involving several elementary permeation steps (adsorption on the membrane surface on the feed side, desorption from the surface on the permeate side, diffusion through the metal lattice, and the two transition phenomena surface-to-bulk and bulk-to-surface). First, the characteristic driving force of each step is evaluated, showing that adsorption and desorption singularly considered and the adsorption and desorption considered at the same time are characterized by driving forces depending on the ratio of feed and permeate hydrogen pressure. On the contrary, the diffusion step is found to present a driving force that is composed of two terms, one which corresponds to the original Sieverts law (with an exponent of 0.5) and the other which is the product of the pressure difference and a temperature-dependent factor. Then, the characteristic n is evaluated by applying the multistep model to two different membranes from the literature in several cases, (a) considering each permeation step as the only limiting one and (b) considering the overall effect of all steps. The results of the analysis show that for a low temperature and thin membrane thickness, the effect of the surface phenomena is, in general, a decrease of the overall exponent n toward values lower than 0.5, even though, under particular operating conditions, the n theoretical value of the surface phenomena is equal to unity. At a higher temperature and thickness (diffusion-controlled permeation), n tends to 0.5, even though the rapidity of this tendency depends strictly on the membrane diffusional parameters. In this frame, the expression developed for the diffusion step provides a theoretical reason why n values higher than 0.5 are found even for thick membranes and high temperature, where diffusion is the only rate-determining step.

摘要

本文通过考虑一个涉及多个基本渗透步骤的复杂模型(在进料侧的膜表面上的吸附、在渗透侧的表面上的解吸、通过金属晶格的扩散以及两个过渡现象——表面到体和体到表面),分析了 Sieverts 型驱动力指数 n 在通过 Pd 基膜的氢渗透中的物理意义。首先,评估了每个步骤的特征驱动力,表明单独考虑吸附和解吸以及同时考虑吸附和解吸时,特征驱动力取决于进料和渗透氢压力的比值。相反,发现扩散步骤呈现出由两个项组成的驱动力,一个对应于原始 Sieverts 定律(指数为 0.5),另一个是压力差和与温度相关的因素的乘积。然后,通过在几种情况下将多步模型应用于文献中的两种不同的膜,评估特征 n:(a)仅考虑每个渗透步骤作为唯一的限制因素,(b)考虑所有步骤的整体影响。分析结果表明,在低温和薄膜厚度的情况下,表面现象的影响通常会导致整体指数 n 降低到低于 0.5 的值,尽管在特定的操作条件下,表面现象的 n 理论值等于 1。在较高的温度和厚度(扩散控制渗透)下,n 趋于 0.5,尽管这种趋势的速度严格取决于膜的扩散参数。在这个框架内,为扩散步骤开发的表达式提供了一个理论原因,即即使对于厚膜和高温,扩散是唯一的速率决定步骤,也会发现 n 值高于 0.5。

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