specific mass, ρ

1.293 kg∙m⁻³

dynamic viscosity, μ

1.8102 N∙s∙m⁻²

velocity input—boundary

u

1.0 s∙m⁻¹

v

0.0 s∙m⁻¹

velocity input—chimney output

u

0.0 s∙m⁻¹

v

1.3 s∙m⁻¹