Strong Roughening of Spontaneous Imbibition Fronts Z. Sadjadi 1, H. Rieger 1 S. Grüner 2, P. Huber 2 1 Theoretical Physics, Saarland University 2 Experimental.

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Strong Roughening of Spontaneous Imbibition Fronts Z. Sadjadi 1, H. Rieger 1 S. Grüner 2, P. Huber 2 1 Theoretical Physics, Saarland University 2 Experimental Physics, Saarland University ComPhys11, Leipzig

Imbibition: Displacement of one fluid by another immiscible fluid in a porous matrix Ink in paper towel Physical processes involved: Oil-air interface in an artificial microstructure

Spontaneous imbibition in nanoporous Vycor glass [S. Grüner, P. Huber (2010)] Network of nano-pores R 0 ~ 5 ∙10 -9 m Lightscattering Experiment: front height front width

Lucas-Washburn law for spontaneous capillary rise PLPL Lucas-Washburn Capillary / Laplace Pressure:

Height evolution of imbibition front in nano-porous Vycor glass h(t) ~ t 1/2 - Lucas-Washburn as expected since on average

Kinetic Roughening: Standard scaling Height difference fluctuations:

Roughness of the imbibition front Front Width / Roughness Height difference fluctuations   const. (time independent)

Theory Interface roughening, KPZ Cellular automata: Directed percolation depinning Microscopic simulations (lattice Boltzmann) Phase Field Models … Models with surface tension in the imbibition front display a growing correlation length and a roughening exponent  << 0.5 independent pores with constant (not ok) radius:  = 1/2 independent pores with randomly varying (ok) radius:  = ¼ lattice gas model with in porous medium with high porosity (not ok):   0.5 Ergo: Theoretical description must contain A) pore aspects B) network aspects

Pore network model with quenched disorder Pipe radii: Boundary conditions: p i = 0 for bottom node layer p meniscus = p laplace = 2  /r  Liquid reservoir in contact with lower system boundary Network of cylindrical pipes with random diameter (<10nm) Hagen- Poiseuille mass balance at each node i  Compute all node pressures p i (t) Integrate for step  t: Filling height in each pipe: Rules at junctions / collisions

Time evolution snapshots: Define height h(x,t) at lateral coordinate x: Average over all menisci in column x

Computer simulation results (disorder averaged): „Finite size scaling“: No dependence on lateral size Lucas- Washburn Kinetic Roughening  = 0.45  0.02 Height- difference Fluctuations C(l,t) for fixed t Correlation length  =O(1)

Conclusion Roughening of imbibition front in vycor glass  = 0.46  0.01 … … in pore network model  = 0.45  Absence of lateral correlations  uncorrelated meniscus propagation Low porosity materials, pore aspect ratio > 2: New (?) universality class Expected crossover for pore aspect ratio < 1: hydrodynamics in junctions important, influence of surface tension within imbibition front important

Titel

Imbibition: theory Phase field models (Alava et al.) Directed percolation Depinning (DPD) Lattice gas model (Tarjus et al)

Lattice gas model for an aero-gel   0.5 BUT: High porosity  surface tension relevant  lateral correlations