Hot fluid "C= 2562 J/kg.k, Pr=51.3, µu = 5.22E-3 Pa.s, k = 0.260 W/m.K" flows at 1.3 kg/min inside a 3-mm diameter, thin-walled tube. The tube is coiled and submerged in a water bath maintained at 23°C. The fluid experiences a temperature drop of 45°C and leaves the tube at 35°C. What is the required length of the tube "m"? Neglect heat transfer enhancement associated with the coiling. Assume fully developed flow, if turbulent flow use Dittus-Boelter equation: Nu = 0.023 Re Pr. 0.8

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Chapter7: Forced Convection Inside Tubes And Ducts
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Hot fluid "C= 2562 J/kg.k , Pr=51.3, µ = 5.22E-3 Pa.s, k = 0.260 W/m.K" flows at 1.3
kg/min inside a 3-mm diameter, thin-walled tube. The tube is coiled and submerged in
a water bath maintained at 23°C. The fluid experiences a temperature drop of 45°C and
leaves the tube at 35°C. What is the required length of the tube "m"? Neglect heat
transfer enhancement associated with the coiling. Assume fully developed flow, if turbulent
flow use Dittus-Boelter equation: Nu = 0.023 Re Pr.
Transcribed Image Text:Hot fluid "C= 2562 J/kg.k , Pr=51.3, µ = 5.22E-3 Pa.s, k = 0.260 W/m.K" flows at 1.3 kg/min inside a 3-mm diameter, thin-walled tube. The tube is coiled and submerged in a water bath maintained at 23°C. The fluid experiences a temperature drop of 45°C and leaves the tube at 35°C. What is the required length of the tube "m"? Neglect heat transfer enhancement associated with the coiling. Assume fully developed flow, if turbulent flow use Dittus-Boelter equation: Nu = 0.023 Re Pr.
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