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a cable of radius conductivity k density or u and specific heat moves through a furnace with velocity u and leaves at
a cable of radius conductivity k density or u and specific heat moves with velocity u through a furnace and leaves at
a thin wire of diameter d specific heat conductivity k and density p c u moves with velocity u through a furnace of
a wire of diameter d is formed into a circular loop of radius the loop rotates with constant angular velocity z one
a wire of radius moves with a velocity through a furnace of length l it enters the furnace at where it is heated by
hot water at flows downward from a faucet of radius at a rate the water is cooled by convection as it flows the ambient
heat is removed by convection from an electronic package using a single fin of circular cross section of interest is
a constant area fin of length and cross-sectional area generates heat at a volumetric rate 2l ac qc half the fin is
the cross-sectional area of a fin is and its circumference is along its upper half surface heat is exchanged by
radiation is used to heat a hollow sphere of inner radius i outer radius r and conductivity k due to the thermal
a hollow shaft of outer radius and inner radius rotates inside a sleeve of inner radius and outer radius frictional
one side of a plate is heated with uniform flux while the other cc side exchanges heat by convection and radiation the
a thin electric element is sandwiched between two plates of conductivity k and thickness l eachthe element dissipates a
complete paraphrase all report and changing wordsdo not use google translateabstract an unknown circuit in a black box
consider two-dimensional conduction in the semi-circular cylinder shown the cylinder is heated with uniform flux along
a long hollow cylinder exchanges heat by radiation and convection along its outside surface with an ambient fluid at
write the heat equation and boundary conditions for steady state two-dimensional conduction in the rectangular plate
heat is generated at a rate qc in a spherical shell with inner radius and outer radius heat is added at the outer
a long electric cable generates heat at a rate qc half the cable is buried underground while the other half exchanges
a rectangular plate of length l and height h slides down an inclined surface with a velocity u sliding friction results
consider a semi-circular section of a tube with inside radius and outside radius heat is exchanged by convection along
two large plates of thicknesses and are initially at temperatures and their respective conductivities are and the two
heat is generated at a volumetric rate qccc in a rod of radius and length lhalf the cylindrical surface is insulated
a cable of radius conductivity k and specific heat moves through a furnace with velocity u and leaves at temperature t
radiation is suddenly directed at the surface of a semi-infinite plate of conductivity k and thermal diffusivity d due