@afeilberg noticed my original units for ka (mtc) were wrong.
I think this is correct now in a49ad9fb807a9db6bed3001a621572088cc34264, which has:
# Common term, mass transfer into liquid phase (g/s)
#g/s 1/s m3(t) ----g/m3(g)-----
g2l = ka * vt * (ccg - ccl / hc)
Note that we need vt = total volume in this expression, because I assume the specific interface area rolled into ka is m2(interface)/m3(total) where total volume = volume of packed medium or reactor.
We might be able to simplify a bit by using compound concentrations instead of mass as state variables (this should be a separate issue) but then we need to include the ratio of gas to total volume I guess.
@afeilberg noticed my original units for ka (mtc) were wrong. I think this is correct now in a49ad9fb807a9db6bed3001a621572088cc34264, which has:
Note that we need
vt
= total volume in this expression, because I assume the specific interface area rolled intoka
is m2(interface)/m3(total) where total volume = volume of packed medium or reactor. We might be able to simplify a bit by using compound concentrations instead of mass as state variables (this should be a separate issue) but then we need to include the ratio of gas to total volume I guess.