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TRAN:010117Centered faces J=3Ci/2-Ci+1/2 force C1=48/13, C2=36/13, J=54/13 with every residual 0

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Transport Centered Conservative Face FluxTransport Discrete Steady Cell Residual

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Mixed review

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TRAN:010118Linear sorption R=3 sends the inlet step at 1/6 m/day, so L=2 m breaks through at 12 d

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Transport Linear Sorption RetardationTransport Advective Front Breakthrough

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Mixed review

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TRAN:010219Power-law n=1/2 pipe has |wall tau|=4 Pa, umax=1/75, Ubar=0.008, Q=8pi e-7, ratio 5/3

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Transport Power Law Pipe ConstitutiveTransport Power Law Flowrate Ratio

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Momentum transport and viscous flowTransport Phenomena · Mixed review

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TRAN:010220Bingham channel G=2, tau_y=1 yields a plug u=1/4 on |y|<=1/2 and Ubar=5/24

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Transport Bingham Yield PlugTransport Bingham Channel Discharge

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Momentum transport and viscous flowTransport Phenomena · Mixed review

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TRAN:010221Inner-driven Couette a=1,b=2,Omega=3 has A=-1,B=4, inner torque 32pi, power 96pi

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Transport Circular Couette StokesTransport Viscous Dissipation Torque Power

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Momentum transport and viscous flowTransport Phenomena · Mixed review

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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 deg

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Transport Periodic Thermal PenetrationTransport Harmonic Surface Flux Lead

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Energy transport and convection-conduction couplingTransport Phenomena · Mixed review

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TRAN:010323Given Couette u=Uy/h with both walls at T0, viscous heating peaks at 0.1 K and each wall removes 20 W/m2

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Transport Couette Viscous DissipationTransport Two Wall Heat Removal

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Energy transport and convection-conduction couplingTransport Phenomena · Mixed review

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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 12

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Transport Two Compartment MembraneTransport Unequal Volume Inventory

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Species transport, diffusion, and convectionTransport Phenomena · Mixed review

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TRAN:010425Taylor–Aris Deff=3.083333333e-6 turns a unit pulse at t=100 into centroid 1 m, sigma 0.024832774, peak 16.06515163

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Transport Taylor Aris DispersivityTransport Longtime Pulse Moments

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Species transport, diffusion, and convectionTransport Phenomena · Mixed review

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TRAN:010426A diffusion-limited sphere with R0=1 mm lasts 2500 s and is at R=0.5 mm at 1875 s

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Transport Quasisteady Dissolving SphereTransport R Squared Shrinkage Law

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Species transport, diffusion, and convectionTransport Phenomena · Mixed review

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TRAN:010527Two-film absorption with kG=0.1, kL=0.2, H=2 has 1/KG=20, N=0.4, and 50/50 resistances

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Transport Two Film Overall CoefficientTransport Interfacial Resistance Split

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Boundary layers and interfacial transfer coefficientsTransport Phenomena · Mixed review

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TRAN:010528Higbie contact tc=4 s averages kL=1.784124116e-5 and uptake 7.136496465e-5

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Transport Higbie Instantaneous FluxTransport Penetration Average Factor Two

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Boundary layers and interfacial transfer coefficientsTransport Phenomena · Mixed review

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TRAN:010629Zero-current ambipolar salt flux is 1.2e-4 with junction +0.019709862 V

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Transport Ambipolar DiffusivityTransport Zero Current Junction Potential

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Multicomponent and coupled transportTransport Phenomena · Mixed review

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TRAN:010630Wet-surface balance closes at Ts=20 with N=0.005 and q=200=Lambda N

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Transport Wet Surface Energy MassTransport Interface Temperature Root

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Multicomponent and coupled transportTransport Phenomena · Mixed review

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TRAN:010631Thin-EDL electroosmosis cancels at dp/dx=280 with zero mean and wall shear 0.014 Pa

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Transport Helmholtz Smoluchowski SlipTransport EO Poiseuille Superposition

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Multicomponent and coupled transportTransport Phenomena · Mixed review

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912011A Newtonian oil film flows steadily down a rigid plane inclined at (35.0^\circ) above the horizontal.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912012Water flows steadily through a horizontal circular microtube of radius (R=60.0\ \mathrm{{\mu}m}) and length (L=18.0…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912013A Newtonian liquid fills the annular gap between two vertical, coaxial cylinders of radii (R_i=24.0\ \mathrm{mm}) a…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912014A plane slider bearing has width (B=80.0\ \mathrm{mm}) perpendicular to the direction of motion and length (L=120\…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912015Two parallel circular disks of radius (a=75.0\ \mathrm{mm}) squeeze a Newtonian silicone oil film.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912016Air at (20^\circ\mathrm{C}) flows at (U_\infty=12.0\ \mathrm{m\,s^{-1}}) over a smooth flat plate of length (1.20\…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912017An incompressible liquid approaches a porous flat surface with an accelerating external velocity (U_e(x)=Kx^{1/3}),…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912018A two-dimensional inviscid stagnation flow with strain rate (a=38.0\ \mathrm{s^{-1}}) approaches a plane wall at (y…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912019A cold planar sheet is placed in a steady two-dimensional stagnation flow of air whose external velocity is (u_e=ax…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912020A plane catalyst slab of thickness 24 mm generates heat uniformly at 6.0 x 10^5 W m^-3.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912021Saturated steam at 180 degrees C flows through a long steel pipe having an inner radius of 22 mm and an outer radiu…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912022A straight rectangular aluminum fin is attached to a wall maintained at 160 degrees C and extends 60 mm into air at…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912023A cylindrical stainless-steel pin fin of diameter 6.0 mm and length 45 mm projects from a surface at 210 degrees C…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912024A solid copper sphere of diameter 30 mm is initially at a uniform temperature of 240 degrees C and is suddenly susp…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912025A 12 kg aluminum instrument housing, initially uniform at 20 degrees C, is placed in a temperature-controlled liqui…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912026Heat is conducted steadily through a 50 mm thick plane wall with no internal heat generation.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912027A continuous process heats 0.060 kg s^-1 of a liquid from 18 degrees C to 72 degrees C in a well-mixed vessel.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912028A 1.20 m by 0.80 m heated panel consists of a 6.0 mm ceramic layer (thermal conductivity 1.6 W m^-1 K^-1) bonded to…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912029Air at 1 atm flows at 14.0 m/s parallel to a smooth, isothermal plate 1.20 m long and 0.60 m wide.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912030A process oil enters a straight circular tube of inside diameter 18.0 mm and heated length 4.00 m at 35.0°C with a…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912031Water at 22.0°C flows across a single circular cylinder of diameter 12.0 mm and exposed length 0.500 m at a free-st…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912032A 1.50 m high by 0.80 m wide vertical metal panel dissipates 420 W uniformly from one face into still air at 20.0°C…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912033A horizontal steam line of outside diameter 0.160 m and length 8.00 m has an isothermal outer surface at 135°C and…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912034A counterflow double-pipe heat exchanger cools 0.900 kg/s of a liquid process stream from 150°C to a required 85.0°…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912035Hot air at 180°C and 0.620 kg/s is cooled in an unmixed–unmixed crossflow heat exchanger by water entering at 18.0°…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Problem library

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Topic choices for Transport Phenomena are shortened. Search still covers every problem.

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TRAN:010117Centered faces J=3Ci/2-Ci+1/2 force C1=48/13, C2=36/13, J=54/13 with every residual 0

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Transport Centered Conservative Face FluxTransport Discrete Steady Cell Residual

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Mixed review

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TRAN:010118Linear sorption R=3 sends the inlet step at 1/6 m/day, so L=2 m breaks through at 12 d

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Transport Linear Sorption RetardationTransport Advective Front Breakthrough

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Mixed review

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TRAN:010219Power-law n=1/2 pipe has |wall tau|=4 Pa, umax=1/75, Ubar=0.008, Q=8pi e-7, ratio 5/3

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Transport Power Law Pipe ConstitutiveTransport Power Law Flowrate Ratio

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Momentum transport and viscous flowTransport Phenomena · Mixed review

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TRAN:010220Bingham channel G=2, tau_y=1 yields a plug u=1/4 on |y|<=1/2 and Ubar=5/24

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Transport Bingham Yield PlugTransport Bingham Channel Discharge

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Momentum transport and viscous flowTransport Phenomena · Mixed review

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TRAN:010221Inner-driven Couette a=1,b=2,Omega=3 has A=-1,B=4, inner torque 32pi, power 96pi

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Transport Circular Couette StokesTransport Viscous Dissipation Torque Power

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Momentum transport and viscous flowTransport Phenomena · Mixed review

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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 deg

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Transport Periodic Thermal PenetrationTransport Harmonic Surface Flux Lead

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Energy transport and convection-conduction couplingTransport Phenomena · Mixed review

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TRAN:010323Given Couette u=Uy/h with both walls at T0, viscous heating peaks at 0.1 K and each wall removes 20 W/m2

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Transport Couette Viscous DissipationTransport Two Wall Heat Removal

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Energy transport and convection-conduction couplingTransport Phenomena · Mixed review

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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 12

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Transport Two Compartment MembraneTransport Unequal Volume Inventory

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Species transport, diffusion, and convectionTransport Phenomena · Mixed review

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TRAN:010425Taylor–Aris Deff=3.083333333e-6 turns a unit pulse at t=100 into centroid 1 m, sigma 0.024832774, peak 16.06515163

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Transport Taylor Aris DispersivityTransport Longtime Pulse Moments

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Species transport, diffusion, and convectionTransport Phenomena · Mixed review

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TRAN:010426A diffusion-limited sphere with R0=1 mm lasts 2500 s and is at R=0.5 mm at 1875 s

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Transport Quasisteady Dissolving SphereTransport R Squared Shrinkage Law

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Species transport, diffusion, and convectionTransport Phenomena · Mixed review

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TRAN:010527Two-film absorption with kG=0.1, kL=0.2, H=2 has 1/KG=20, N=0.4, and 50/50 resistances

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Transport Two Film Overall CoefficientTransport Interfacial Resistance Split

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Boundary layers and interfacial transfer coefficientsTransport Phenomena · Mixed review

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TRAN:010528Higbie contact tc=4 s averages kL=1.784124116e-5 and uptake 7.136496465e-5

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Transport Higbie Instantaneous FluxTransport Penetration Average Factor Two

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Boundary layers and interfacial transfer coefficientsTransport Phenomena · Mixed review

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TRAN:010629Zero-current ambipolar salt flux is 1.2e-4 with junction +0.019709862 V

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Transport Ambipolar DiffusivityTransport Zero Current Junction Potential

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Multicomponent and coupled transportTransport Phenomena · Mixed review

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TRAN:010630Wet-surface balance closes at Ts=20 with N=0.005 and q=200=Lambda N

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Transport Wet Surface Energy MassTransport Interface Temperature Root

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Multicomponent and coupled transportTransport Phenomena · Mixed review

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TRAN:010631Thin-EDL electroosmosis cancels at dp/dx=280 with zero mean and wall shear 0.014 Pa

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Transport Helmholtz Smoluchowski SlipTransport EO Poiseuille Superposition

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Multicomponent and coupled transportTransport Phenomena · Mixed review

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912011A Newtonian oil film flows steadily down a rigid plane inclined at (35.0^\circ) above the horizontal.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912012Water flows steadily through a horizontal circular microtube of radius (R=60.0\ \mathrm{{\mu}m}) and length (L=18.0…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912013A Newtonian liquid fills the annular gap between two vertical, coaxial cylinders of radii (R_i=24.0\ \mathrm{mm}) a…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912014A plane slider bearing has width (B=80.0\ \mathrm{mm}) perpendicular to the direction of motion and length (L=120\…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912015Two parallel circular disks of radius (a=75.0\ \mathrm{mm}) squeeze a Newtonian silicone oil film.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912016Air at (20^\circ\mathrm{C}) flows at (U_\infty=12.0\ \mathrm{m\,s^{-1}}) over a smooth flat plate of length (1.20\…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912017An incompressible liquid approaches a porous flat surface with an accelerating external velocity (U_e(x)=Kx^{1/3}),…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912018A two-dimensional inviscid stagnation flow with strain rate (a=38.0\ \mathrm{s^{-1}}) approaches a plane wall at (y…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912019A cold planar sheet is placed in a steady two-dimensional stagnation flow of air whose external velocity is (u_e=ax…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912020A plane catalyst slab of thickness 24 mm generates heat uniformly at 6.0 x 10^5 W m^-3.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912021Saturated steam at 180 degrees C flows through a long steel pipe having an inner radius of 22 mm and an outer radiu…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912022A straight rectangular aluminum fin is attached to a wall maintained at 160 degrees C and extends 60 mm into air at…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912023A cylindrical stainless-steel pin fin of diameter 6.0 mm and length 45 mm projects from a surface at 210 degrees C…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912024A solid copper sphere of diameter 30 mm is initially at a uniform temperature of 240 degrees C and is suddenly susp…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912025A 12 kg aluminum instrument housing, initially uniform at 20 degrees C, is placed in a temperature-controlled liqui…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912026Heat is conducted steadily through a 50 mm thick plane wall with no internal heat generation.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912027A continuous process heats 0.060 kg s^-1 of a liquid from 18 degrees C to 72 degrees C in a well-mixed vessel.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912028A 1.20 m by 0.80 m heated panel consists of a 6.0 mm ceramic layer (thermal conductivity 1.6 W m^-1 K^-1) bonded to…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912029Air at 1 atm flows at 14.0 m/s parallel to a smooth, isothermal plate 1.20 m long and 0.60 m wide.

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912030A process oil enters a straight circular tube of inside diameter 18.0 mm and heated length 4.00 m at 35.0°C with a…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912031Water at 22.0°C flows across a single circular cylinder of diameter 12.0 mm and exposed length 0.500 m at a free-st…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912032A 1.50 m high by 0.80 m wide vertical metal panel dissipates 420 W uniformly from one face into still air at 20.0°C…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912033A horizontal steam line of outside diameter 0.160 m and length 8.00 m has an isothermal outer surface at 135°C and…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912034A counterflow double-pipe heat exchanger cools 0.900 kg/s of a liquid process stream from 150°C to a required 85.0°…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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TRAN:9912035Hot air at 180°C and 0.620 kg/s is cooled in an unmixed–unmixed crossflow heat exchanger by water entering at 18.0°…

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Conservation ScalingTransport Phenomena Problem Solving

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Local conservation laws, constitutive fluxes, and scalingTransport Phenomena · Calculation

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Problem results

TRAN:9912001A Newtonian oil of density 860 kg/m^3 and viscosity 0.145 Pa s flows steadily through a horizontal rectangular duct…

TRAN:9912002Two infinite parallel plates are separated by a 4.00 mm layer of an incompressible Newtonian liquid with viscosity…

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…

TRAN:9912004A cylindrical journal of radius 49.5 mm rotates concentrically inside a fixed bearing of radius 50.0 mm and length…

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…

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…

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…

TRAN:9912008A Newtonian liquid film of density 1050 kg/m^3 and viscosity 0.095 Pa s drains steadily down a flat plate inclined…

TRAN:9912009A viscous Newtonian liquid of density 1120 kg/m^3 and viscosity 0.340 Pa s coats the outside of a stationary vertic…

TRAN:9912010An incompressible Newtonian liquid of density 980 kg/m^3 and viscosity 0.060 Pa s flows steadily between two fixed,…

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Problem results

TRAN:9912001A Newtonian oil of density 860 kg/m^3 and viscosity 0.145 Pa s flows steadily through a horizontal rectangular duct…

TRAN:9912002Two infinite parallel plates are separated by a 4.00 mm layer of an incompressible Newtonian liquid with viscosity…

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…

TRAN:9912004A cylindrical journal of radius 49.5 mm rotates concentrically inside a fixed bearing of radius 50.0 mm and length…

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…

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…

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…

TRAN:9912008A Newtonian liquid film of density 1050 kg/m^3 and viscosity 0.095 Pa s drains steadily down a flat plate inclined…

TRAN:9912009A viscous Newtonian liquid of density 1120 kg/m^3 and viscosity 0.340 Pa s coats the outside of a stationary vertic…

TRAN:9912010An incompressible Newtonian liquid of density 980 kg/m^3 and viscosity 0.060 Pa s flows steadily between two fixed,…