TRAN:010117Centered faces J=3Ci/2-Ci+1/2 force C1=48/13, C2=36/13, J=54/13 with every residual 0View access optionsTransport Centered Conservative Face FluxTransport Discrete Steady Cell ResidualLocal conservation laws, constitutive fluxes, and scalingTransport Phenomena · Mixed review—
TRAN:010118Linear sorption R=3 sends the inlet step at 1/6 m/day, so L=2 m breaks through at 12 dView access optionsTransport Linear Sorption RetardationTransport Advective Front BreakthroughLocal conservation laws, constitutive fluxes, and scalingTransport Phenomena · Mixed review—
TRAN:010219Power-law n=1/2 pipe has |wall tau|=4 Pa, umax=1/75, Ubar=0.008, Q=8pi e-7, ratio 5/3View access optionsTransport Power Law Pipe ConstitutiveTransport Power Law Flowrate RatioMomentum transport and viscous flowTransport Phenomena · Mixed review—
TRAN:010220Bingham channel G=2, tau_y=1 yields a plug u=1/4 on |y|<=1/2 and Ubar=5/24View access optionsTransport Bingham Yield PlugTransport Bingham Channel DischargeMomentum transport and viscous flowTransport Phenomena · Mixed review—
TRAN:010221Inner-driven Couette a=1,b=2,Omega=3 has A=-1,B=4, inner torque 32pi, power 96piView access optionsTransport Circular Couette StokesTransport Viscous Dissipation Torque PowerMomentum transport and viscous flowTransport Phenomena · Mixed review—
TRAN:010322A 10 K harmonic surface on y>0 with delta=0.1 m has 1% depth 0.460517 m and a 282.842712 W/m2 flux that leads 45 degView access optionsTransport Periodic Thermal PenetrationTransport Harmonic Surface Flux LeadEnergy transport and convection-conduction couplingTransport Phenomena · Mixed review—
TRAN:010323Given Couette u=Uy/h with both walls at T0, viscous heating peaks at 0.1 K and each wall removes 20 W/m2View access optionsTransport Couette Viscous DissipationTransport Two Wall Heat RemovalEnergy transport and convection-conduction couplingTransport Phenomena · Mixed review—
TRAN:010424Unequal tanks 1 L / 3 L with kA=0.4 L/min meet C1=6, C2=2 at t=(15/8)ln 3 and conserve inventory 12View access optionsTransport Two Compartment MembraneTransport Unequal Volume InventorySpecies transport, diffusion, and convectionTransport Phenomena · Mixed review—
TRAN:010425Taylor–Aris Deff=3.083333333e-6 turns a unit pulse at t=100 into centroid 1 m, sigma 0.024832774, peak 16.06515163View access optionsTransport Taylor Aris DispersivityTransport Longtime Pulse MomentsSpecies transport, diffusion, and convectionTransport Phenomena · Mixed review—
TRAN:010426A diffusion-limited sphere with R0=1 mm lasts 2500 s and is at R=0.5 mm at 1875 sView access optionsTransport Quasisteady Dissolving SphereTransport R Squared Shrinkage LawSpecies transport, diffusion, and convectionTransport Phenomena · Mixed review—
TRAN:010527Two-film absorption with kG=0.1, kL=0.2, H=2 has 1/KG=20, N=0.4, and 50/50 resistancesView access optionsTransport Two Film Overall CoefficientTransport Interfacial Resistance SplitBoundary layers and interfacial transfer coefficientsTransport Phenomena · Mixed review—
TRAN:010528Higbie contact tc=4 s averages kL=1.784124116e-5 and uptake 7.136496465e-5View access optionsTransport Higbie Instantaneous FluxTransport Penetration Average Factor TwoBoundary layers and interfacial transfer coefficientsTransport Phenomena · Mixed review—
TRAN:010629Zero-current ambipolar salt flux is 1.2e-4 with junction +0.019709862 VView access optionsTransport Ambipolar DiffusivityTransport Zero Current Junction PotentialMulticomponent and coupled transportTransport Phenomena · Mixed review—
TRAN:010630Wet-surface balance closes at Ts=20 with N=0.005 and q=200=Lambda NView access optionsTransport Wet Surface Energy MassTransport Interface Temperature RootMulticomponent and coupled transportTransport Phenomena · Mixed review—
TRAN:010631Thin-EDL electroosmosis cancels at dp/dx=280 with zero mean and wall shear 0.014 PaView access optionsTransport Helmholtz Smoluchowski SlipTransport EO Poiseuille SuperpositionMulticomponent and coupled transportTransport Phenomena · Mixed review—
TRAN:9912001A Newtonian oil of density 860 kg/m^3 and viscosity 0.145 Pa s flows steadily through a horizontal rectangular duct…View problem statementConservation ScalingTransport Phenomena Problem SolvingLocal conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation—
TRAN:9912002Two infinite parallel plates are separated by a 4.00 mm layer of an incompressible Newtonian liquid with viscosity…View access optionsConservation ScalingTransport Phenomena Problem SolvingLocal conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation—
TRAN:9912003Water at 20 degrees C, with density 998 kg/m^3 and viscosity 1.002 x 10^-3 Pa s, flows steadily down a straight cir…View access optionsConservation ScalingTransport Phenomena Problem SolvingLocal conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation—
TRAN:9912004A cylindrical journal of radius 49.5 mm rotates concentrically inside a fixed bearing of radius 50.0 mm and length…View access optionsConservation ScalingTransport Phenomena Problem SolvingLocal conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation—
TRAN:9912005A rigid sphere of diameter 0.80 mm and density 2550 kg/m^3 is released from rest in a large, quiescent tank contain…View access optionsConservation ScalingTransport Phenomena Problem SolvingLocal conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation—
TRAN:9912006Air at 25 degrees C, with density 1.184 kg/m^3 and viscosity 1.85 x 10^-5 Pa s, flows at 12.0 m/s past a fixed smoo…View access optionsConservation ScalingTransport Phenomena Problem SolvingLocal conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation—
TRAN:9912007A Newtonian liquid of density 920 kg/m^3 and viscosity 0.185 Pa s forms a steady laminar film flowing down a vertic…View access optionsConservation ScalingTransport Phenomena Problem SolvingLocal conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation—
TRAN:9912008A Newtonian liquid film of density 1050 kg/m^3 and viscosity 0.095 Pa s drains steadily down a flat plate inclined…View access optionsConservation ScalingTransport Phenomena Problem SolvingLocal conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation—
TRAN:9912009A viscous Newtonian liquid of density 1120 kg/m^3 and viscosity 0.340 Pa s coats the outside of a stationary vertic…View access optionsConservation ScalingTransport Phenomena Problem SolvingLocal conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation—