Dipl. Ing. Matthias Mayerhofer Technische Universität München ...
Dipl. Ing. Matthias Mayerhofer Technische Universität München ...
Dipl. Ing. Matthias Mayerhofer Technische Universität München ...
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VIII Notation<br />
Notation<br />
ΔH [Kj/mol] Enthalpy (or Heat) of Vaporization<br />
Τ [s] Residence Time<br />
C* [-] Number of atoms of carbon in hydrocarbons<br />
D [-] Metal Dispersion<br />
dp [mm] Particle Diameter<br />
dp [mbar] Pressure Drop<br />
F [-] Mole fraction of each component in the product gas<br />
Kapp,tar [mTb,wet³/kgh] Apparent kinetic constant for tar elimination<br />
LHV [Kj/Kg] Lower Heating Value<br />
M [-] Molar density of gas<br />
MM [g/mol] Molar mass of the noble metal<br />
MN [mol/h] Molar feed rate of carbon to the reactor<br />
P [bar] Pressure<br />
Q [mTb,wet³/h] Gas flow rate at the inlet of the catalytic bed<br />
Q [1/h] Volumetric flow rate of gas<br />
QV_N [kg/h] Gas Flow<br />
S/B [-] Steam/Biomass ratio<br />
St [mol/mol] Stoichiometric Ratio<br />
SV [1/h] Space Velocity<br />
T [°C] Temperature<br />
T [-] Fraction of tar (or tar model compound) that reacted<br />
Tb [°C] Temperature in the center of the catalytic bed<br />
tspc [kgh/mTb,wet³] Critical space time