Literature DB >> 20402480

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

Alessio Caravella1, Francesco Scura, Giuseppe Barbieri, Enrico Drioli.   

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.

Entities:  

Year:  2010        PMID: 20402480     DOI: 10.1021/jp1006582

Source DB:  PubMed          Journal:  J Phys Chem B        ISSN: 1520-5207            Impact factor:   2.991


  4 in total

Review 1.  Recent Advances in Pd-Based Membranes for Membrane Reactors.

Authors:  Alba Arratibel Plazaola; David Alfredo Pacheco Tanaka; Martin Van Sint Annaland; Fausto Gallucci
Journal:  Molecules       Date:  2017-01-01       Impact factor: 4.411

Review 2.  Thermodynamic Aspects in Non-Ideal Metal Membranes for Hydrogen Purification.

Authors:  Stefano Bellini; Yu Sun; Fausto Gallucci; Alessio Caravella
Journal:  Membranes (Basel)       Date:  2018-09-16

3.  Mass Transfer Coefficient in Multi-Stage Reformer/Membrane Modules for Hydrogen Production.

Authors:  Diego Barba; Mauro Capocelli; Marcello De Falco; Giovanni Franchi; Vincenzo Piemonte
Journal:  Membranes (Basel)       Date:  2018-11-14

4.  Hydrogen Production via Steam Reforming: A Critical Analysis of MR and RMM Technologies.

Authors:  Giovanni Franchi; Mauro Capocelli; Marcello De Falco; Vincenzo Piemonte; Diego Barba
Journal:  Membranes (Basel)       Date:  2020-01-03
  4 in total

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