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. 2017 Mar 23;7(2):17. doi: 10.3390/membranes7020017
BCC Body centered cubic
dpore Pore diameter
Ea Activation energy
fio Fugacity for i-component
FCC Face centered cubic
FFA Free fatty acid
G Free Gibbs energy
GOSR Glycerol oxidative steam reforming
GSR Glycerol steam reforming
JH2 Hydrogen flux through the membrane
K Equilibrium constant
ki Kinetic constant for i-reaction
LTA Linde-type 5A zeolite
MONG Matter organic non-glycerol
MR Membrane reactor
MW Molecular weight
OGMR Oxygen glycerol molar ratio
P Pressure
pH2,ret Hydrogen partial pressure in the retentate side
pH2,perm Hydrogen partial pressure in the permeate side
PeH2 Hydrogen permeability through the membrane
PeH2o Pre-exponential factor
R Universal ideal gas constant
S Entropy
SRM Steam reforming of methane
T Temperature
TR Traditional reactor
WGS Water gas shift
WGMR Water glycerol molar ratio
WHSV Weight hourly space velocity
δ Palladium thickness
ε Membrane void fraction
τ Tortuosity
∇p Pressure gradient
η Viscosity
νi Stoichiometric coefficient for i-component