Modeling and Simulation of the Hydrogenation of α-Methylstyrene on Catalytically Active Metal Foams as Tubular Reactor Packing

Table 1

Simulation parameters.

Parameter	Symbol	Value	Unit
Volumetric flow rate liquid		10⋯40	mL min^−1
Volumetric flow rate gas		50⋯200	mL min^−1
Mass fraction of AMS		20	wt. %
Inlet pressures		1, 10	Bar
Initial temperatures		393, 313	K
Reactor length		0.5	m
Reactor diameter		0.017	m
Pore density of foams		30	PPI
Number of collocation points		50	—
Number of finite elements		1	—