We elucidate in this paper the influence of inertia of the imbibing liquid
with special attention to the printing of paper. This is used to explain th
e observed differences between the absorption properties of fluids into lar
ge and small pores in paper coating structures. Without invoking arbitrary
changes of the assumed constants in Lucas-Washbum (Washburn 1921) it has be
en hitherto impossible to describe the retarded imbibition seen when absorb
ing into highly porous structures containing large pores, for example in ma
tt papers or coatings derived from very steep particle size distribution pi
gments.
We verify the differential effect between coarse and fine pores in a networ
k model by the computational network simulator Pore-Cor where, uniquely, Bo
sanquet's equation (Bosanquet 1923), which describes both inertial and visc
ous capillarity, was incorporated together with mass balance calculations a
t each feature entry on a timestep of 1 ns. We apply the findings to compre
ssed coating pigment samples of different porosities determined independent
ly by mercury porosimetry. This is used to demonstrate the sensitivity of a
bsorption rate and potential for separation of fluid(s) into differential p
ore sizes based on viscosity, fluid density and pore size distribution dete
rmined by the proportion of fine pores present up to a size equal to a Bosa
nquet-defined optimum. In a network, like a porous paper coating layer, it
is proposed that for low viscosity wetting fluids the smaller features cont
inue to fill sequentially according to this inertial preference to the init
ial exclusion of larger pores. The proportion of excluded pore volume after
imbibition is a function of the available fluid volume which, to define th
is regime, must be less than the total available pore volume of the sample.