HEAT:010117Spherical shell r1=1 m, r2=2 m: equal resistances 1/(8π), Q=400π W, T=100(1 m/r) °CView access optionsHeat Spherical Shell Series ResistanceHeat Radial Fourier IntegrationSteady conduction and thermal resistanceHeat Transfer · Mixed review—
HEAT:010118Generating solid cylinder R=1 m: surface flux 4 W/m², Ts=22 °C, Tcenter=23 °CView access optionsHeat Cylinder Generation Surface FluxHeat Radial Poisson Centerline RiseSteady conduction and thermal resistanceHeat Transfer · Mixed review—
HEAT:010219Lump Cth=1000 J/K, hA=10 W/K: T=20+80 e^{-t/100}, time to 40 °C is 100 ln 4 sView access optionsHeat Lumped Capacitance ExponentialHeat Lumped Time And Energy LostFins and transient conductionHeat Transfer · Mixed review—
HEAT:010220Semi-infinite step to 100 °C: η=1, T=100-80 erf 1, surface flux 80000/√π W/m²View access optionsHeat Semi Infinite Erf SimilarityHeat Semi Infinite Surface EnergyFins and transient conductionHeat Transfer · Mixed review—
HEAT:010221Two C=1 lumps with H=G=1: θ1=5e^{-t}+5e^{-3t}, total excess energy 10e^{-t}View access optionsHeat Two Lump Modal DecompositionHeat Two Lump Common Mode EnergyFins and transient conductionHeat Transfer · Mixed review—
HEAT:010322Fully developed laminar tube at constant q'': h=100, Tout=302 K, outlet wall 312 KView access optionsHeat FD Laminar Constant Flux NusseltHeat Tube Energy Balance Wall BulkExternal and internal convectionHeat Transfer · Mixed review—
HEAT:010323Constant wall 400 K internal flow: Tout=375 K, Q=750 W, LMTD=75/ln 4, UA=10 ln 4View access optionsHeat Constant Wall Exponential MeanHeat Internal Flow Lmtd ClosureExternal and internal convectionHeat Transfer · Mixed review—
HEAT:010424Infinite gray plates eps=1/2 and 1/4: network denominator 5 and q''=3 sigma 300^4View access optionsHeat Gray Plate Radiosity NetworkHeat Black Limit Radiation ExchangeThermal radiation and enclosure exchangeHeat Transfer · Mixed review—
HEAT:010425One black shield between black 600/300 plates: Ts=300(17/2)^{1/4} and half the no-shield fluxView access optionsHeat Black Shield Fourth Power BalanceHeat Series Radiation Space ResistancesThermal radiation and enclosure exchangeHeat Transfer · Mixed review—
HEAT:010426Selective solar absorber: T=(4000/sigma)^{1/4}, hotter than gray by sqrt(2)View access optionsHeat Selective Solar Energy BalanceHeat Gray Limit Fourth Root RatioThermal radiation and enclosure exchangeHeat Transfer · Mixed review—
HEAT:010527Parallel-flow exchanger with UA=ln 4: Cr=1/2, epsilon=7/12, Q=140/3 kWView access optionsHeat Parallel Flow Ntu EffectivenessHeat Two Stream Outlet BalanceHeat exchangers and effectiveness methodsHeat Transfer · Mixed review—
HEAT:010528Phase-change cold side at 20 C: NTU=1, epsilon=1-e^{-1}, UA LMTD closesView access optionsHeat Phase Change CR Zero NtuHeat Lmtd UA Product ClosureHeat exchangers and effectiveness methodsHeat Transfer · Mixed review—
HEAT:010529Clean U=1000 plus fouling R=0.001: U_f=500 and the required area doublesView access optionsHeat Fouling Overall CoefficientHeat Fixed Duty Area ScalingHeat exchangers and effectiveness methodsHeat Transfer · Mixed review—
HEAT:010630Three interior FD nodes with unit source: solution (3/2, 2, 3/2) and flux sum 3View access optionsHeat Second Difference Poisson SolveHeat Discrete Flux Source BalanceCoupled modes and numerical heat transferHeat Transfer · Mixed review—
HEAT:010631FTCS on (0,100,0): Fo=1/2 oscillates nonnegatively; Fo=0.6 goes negativeView access optionsHeat Ftcs Three Node MarchHeat Fourier Number Stability BoundCoupled modes and numerical heat transferHeat Transfer · Mixed review—
HEAT:9906001A 12 mm thick copper plate (k = 401 W/m·K) has uniform face temperatures of 85 °C and 22 °C.View problem statementSteady ConductionHeat Transfer Problem SolvingSteady conduction and thermal resistanceHeat Transfer · Calculation—
HEAT:9906002Steady one-dimensional conduction occurs through a 0.025 m thick slab whose thermal conductivity is unknown.View access optionsSteady ConductionHeat Transfer Problem SolvingSteady conduction and thermal resistanceHeat Transfer · Calculation—
HEAT:9906003A laboratory specimen 8.0 cm long and 2.0 cm in diameter is insulated on its curved surface so that heat flows only…View access optionsSteady ConductionHeat Transfer Problem SolvingSteady conduction and thermal resistanceHeat Transfer · Calculation—
HEAT:9906004A 3.0 mm thick polymer film (k = 0.22 W/m·K) covers a 0.80 m² surface.View access optionsSteady ConductionHeat Transfer Problem SolvingSteady conduction and thermal resistanceHeat Transfer · Calculation—
HEAT:9906005Two large parallel plates, each 1.20 m × 0.90 m, are separated by a 4.0 mm air gap (k_air = 0.028 W/m·K).View access optionsSteady ConductionHeat Transfer Problem SolvingSteady conduction and thermal resistanceHeat Transfer · Calculation—
HEAT:9906006A composite plane wall consists of 20 mm of brick (k = 0.72 W/m·K) bonded to 12 mm of plaster (k = 0.48 W/m·K).View access optionsSteady ConductionHeat Transfer Problem SolvingSteady conduction and thermal resistanceHeat Transfer · Calculation—
HEAT:9906007A 15 mm stainless-steel plate (k = 15 W/m·K) is sandwiched between two 8.0 mm aluminum plates (k = 177 W/m·K).View access optionsSteady ConductionHeat Transfer Problem SolvingSteady conduction and thermal resistanceHeat Transfer · Calculation—
HEAT:9906008Two 10 mm copper plates (k = 385 W/m·K) are pressed together over a 0.050 m² interface.View access optionsSteady ConductionHeat Transfer Problem SolvingSteady conduction and thermal resistanceHeat Transfer · Calculation—
HEAT:9906009A 6.0 mm aluminum wall (k = 204 W/m·K) joins a 9.0 mm steel wall (k = 42 W/m·K) over an area of 0.30 m².View access optionsSteady ConductionHeat Transfer Problem SolvingSteady conduction and thermal resistanceHeat Transfer · Calculation—