Abstract
Dense palladium-based membrane reactors represent as an alternative solution to the conventional systems for pure hydrogen production, assuring important benefits in terms of efficiency and compactness. As a main scope, this chapter will give an overview on the general classification of the membranes, paying particular attention to the palladium-based membranes and their applications, pointing out the most important benefits and the drawback due to their use. Finally, the application of palladium-based membranes in the area of the membrane reactors will be illustrated and such reaction processes in the issue of hydrogen production will be discussed.
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Abbreviations
- AASR:
-
Acetic acid steam reforming
- BESR:
-
Bioethanol steam reforming
- CVD:
-
Chemical vapour deposition
- ELP:
-
Electroless plating deposition
- EP:
-
Electroplating
- ESR:
-
Ethanol steam reforming
- EVD:
-
Electrochemical vapour deposition
- FBR:
-
Fixed bed reactor
- GSR:
-
Glycerol steam reforming
- HTR:
-
High temperature reactor
- IUPAC:
-
International Union of Pure and Applied Chemistry
- LTR:
-
Low temperature reactor
- ML:
-
Molecular layering
- MR:
-
Membrane reactor
- MS:
-
Magnetron sputtering
- MSR:
-
Methane steam reforming
- PEMFC:
-
Proton exchange membrane fuel cell
- POM:
-
Partial oxidation of methane
- PSA:
-
Pressure swing adsorption
- PVD:
-
Physical vapour deposition
- SRM:
-
Methanol steam reforming
- WGS:
-
Water gas shift
- WHSV:
-
Weight hourly space velocity
- D :
-
Diffusion coefficient
- d p :
-
Pore diameter
- E a :
-
Apparent activation energy
- G :
-
Geometrical factor
- J :
-
Flux or permeation rate
- \( J_{{{\text{H}}_{2} ,{\text{Sieverts} {-} {\text{Fick}}}}} \) :
-
Hydrogen flux through the membrane according to Sieverts–Fick law
- \( J_{{{\text{H}}_{2} }} \) :
-
Hydrogen flux through the membrane
- J i :
-
Flux of the i-species across the membrane
- J m :
-
Mass flux
- M i :
-
Molecular weight of the i-species
- n :
-
Dependence factor of the hydrogen flux on the hydrogen partial pressure
- p :
-
Pressure
- \( Pe_{{{\text{H}}_{2} }}^{0} \) :
-
The pre-exponential factor
- \( Pe_{{{\text{H}}_{2} }} \) :
-
The hydrogen permeability
- \( p_{{{\text{H}}_{2} ,{\text{perm}}}} \) :
-
Hydrogen partial pressures at the permeate side
- \( p_{{{\text{H}}_{2} ,{\text{ret}}}} \) :
-
Hydrogen partial pressures at the retentate side
- R :
-
Universal gas constant
- T :
-
Absolute temperature
- X :
-
Coordinate perpendicular to the transport barrier
- \( \Updelta H_{{298\,{\text{K}}}}^{\circ } \) :
-
Enthalpy variation in standard conditions
- Δp i :
-
Pressure difference of species
- α :
-
Ideal separation factor or selectivity
- δ :
-
Membrane thickness
- ϕ pore :
-
Pore diameter
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© 2011 Springer-Verlag London Limited
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Basile, A., Iulianelli, A., Longo, T., Liguori, S., De Falco, M. (2011). Pd-based Selective Membrane State-of-the-Art. In: De De Falco, M., Marrelli, L., Iaquaniello, G. (eds) Membrane Reactors for Hydrogen Production Processes. Springer, London. https://doi.org/10.1007/978-0-85729-151-6_2
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DOI: https://doi.org/10.1007/978-0-85729-151-6_2
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