The hydrogen permeation and stability of tubular palladium alloy (Pd-23%Ag) composite membranes have been investigated at elevated temperatures and pressures. In our analysis we differentiate between dilution of hydrogen by other gas components, hydrogen depletion along the membrane length, concentr
Influence of steam and carbon dioxide on the hydrogen flux through thin Pd/Ag and Pd membranes
β Scribed by F.C. Gielens; R.J.J. Knibbeler; P.F.J. Duysinx; H.D. Tong; M.A.G. Vorstman; J.T.F. Keurentjes
- Publisher
- Elsevier Science
- Year
- 2006
- Tongue
- English
- Weight
- 687 KB
- Volume
- 279
- Category
- Article
- ISSN
- 0376-7388
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β¦ Synopsis
The influence of CO 2 and steam on the H 2 permeation behavior of high-flux Pd/Ag alloy and Pd membranes has been determined. The membranes -fabricated with microsystem technology (MEMS technology) -are 1.0 and 0.5 m thick; the thin membranes will reveal inhibitive effects more strongly than relatively thick membranes. The H 2 flux through the membranes has been studied for periods of more than 80 h during and after addition of CO 2 or H 2 O to the feed. Measurements have been carried out at 623, 673 and 723 K.
The largest flux reductions found are 70 and 69% at 623 K for H 2 O and CO 2 , respectively. After stopping the steam addition the H 2 permeance restores to its original value. After stopping the CO 2 addition the H 2 permeance increases, but to a value lower than before the CO 2 addition. Surprisingly large time constants have been found for the transient permeance behavior. The inhibitive effect caused by the addition of CO 2 is almost certainly caused by the formation of CO and H 2 O by the reverse water gas shift (WGS) reaction. Besides by adsorption of CO 2 , CO and H 2 O, a far stronger inhibitive effect is caused by carbon, which is formed by the dissociation of CO and CO 2 .
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