13. Slurry at a rate of 110 lbm/h and 110 F is pumped through 2 in inside diame- ter pipe. After traveling in a unheated length of the pipe, the slurry enters a 3 ft long heated section where the wall of the pipe is maintained at 190 F. Find the average temperature of the slurry leaving the heated section. Thermal properties of slurry are as follows p= 70 lbm/ft’, µ = 150 lbm/h-ft, c = 0.4 Btu/lbm-F, and k = 0.5 Btu/h-ft·F.

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Chapter6: Forced Convection Over Exterior Surfaces
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the title of the book: Engineering Thermofluids Thermodynamics, Fluid Mechanics, and Heat Transfer by: Mahmoud Massoud

13. Slurry at a rate of 110 lbm/h and 110 F is pumped through 2 in inside diame-
ter pipe. After traveling in a unheated length of the pipe, the slurry enters a 3 ft
long heated section where the wall of the pipe is maintained at 190 F. Find the
average temperature of the slurry leaving the heated section. Thermal properties
of slurry are as follows p= 70 lbm/ft’, µ = 150 lbm/h-ft, c = 0.4 Btu/lbm-F, and k
= 0.5 Btu/h-ft-F.
Transcribed Image Text:13. Slurry at a rate of 110 lbm/h and 110 F is pumped through 2 in inside diame- ter pipe. After traveling in a unheated length of the pipe, the slurry enters a 3 ft long heated section where the wall of the pipe is maintained at 190 F. Find the average temperature of the slurry leaving the heated section. Thermal properties of slurry are as follows p= 70 lbm/ft’, µ = 150 lbm/h-ft, c = 0.4 Btu/lbm-F, and k = 0.5 Btu/h-ft-F.
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