h | : | Heat amount based value | |
theo | : | Theory | |
b | : | Reactant packed bed | |
eva | : | Evaporator | |
c | : | Contact surface with CaCl2 and SiC | |
l | : | Contact surface with SUS and heat exchange fluid | |
Q | : | Averaged volumetric power density | [W/L] |
t | : | Elapsed time | [s] |
Cp | : | Heat capacity | [J/kg/K] |
ρ | : | Density | [kg/m3] |
ΔT | : | Temperature difference | [K] |
T | : | Temperature | [K] |
F | : | Fluid flow rate | [m3/s] |
V | : | Volume | [m3] |
X | : | Conversion ratio | [-] |
ΔH | : | Amount of heat | [kJ/mol] |
P | : | Pressure | [kPa] |
ρM | : | Mol/volume | [mol/m3] |
ε | : | Porosity | [-] |
Cp,M | : | Heat capacity per mol | [J/mol/K] |
λ | : | Thermal conductivity | [W/m/K] |
k | : | Reaction rate coefficient | [1/s] |
1/h | : | Contact thermal resistance | [K·m2/W] |
u | : | Flow velocity | [m/s] |