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