A scheme based on the friction theory (f-theory) is introduced for the visc
osity prediction of mixtures composed of hydrogen and natural gas (hythane)
. In the f-theory the viscosity is separated into a dilute gas viscosity an
d a friction contribution term. The mixture friction coefficients are estim
ated with mixing rules based on pure-component friction coefficients. Becau
se hythane mainly contains hydrogen and methane, the pure friction coeffici
ents of these components are obtained with f-theory models directly fitted
to these two components, while the friction coefficients of the other compo
nents are obtained with a general f-theory model. For the dilute gas viscos
ity term, the simple mixing rule of Wilke is capable of an accurate estimat
ion of the dilute gas viscosity. Using this f-theory scheme in conjunction
with the Peng-Robinson and Soave-Redlich-Kwong EOSs, the viscosities of fou
r hythane mixtures have been predicted within or close to experimental unce
rtainty (+/-1.0%), which is satisfactory for most industrial applications.
This scheme is of a predictive character, because only properties and param
eters of the pure compounds are required. This work further shows the appli
cation of the f-theory for viscosity predictions and its application to ind
ustrial processes.