Fundamentals of Heat and Mass Transfer
Fundamentals of Heat and Mass Transfer
7th Edition
ISBN: 9780470501979
Author: Frank P. Incropera, David P. DeWitt, Theodore L. Bergman, Adrienne S. Lavine
Publisher: Wiley, John & Sons, Incorporated
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Chapter 10, Problem 10.63P

A technique for cooling a multichip module involves submerging the module in a saturated fluorocarbon liquid. Vapor generated due to boiling at the module surface is condensed on the outer surface of copper tubing suspended in the vapor space above the liquid. The thin-walled tubing is of diameter D = 10 mm and is coiled in a horizontal plane. It is cooled by water that enters at 285 K and leaves at 315 K. All the heat dissipated by the chips within the module is transferred from a 100 -mm × 100 -mm boiling surface, at which the flux is 10 5 W/m 2 to the fluorocarbon liquid, which is at T sat = 57 ° C . Liquid properties are k l = 0.0537 W/m K , c p , J = 1100 J/kg K , h f g h f g = 84 , 400 J/kg , ρ l = 1619.2 kg/m 3 , ρ υ = 13.4 kg/m 3 , σ = 8.1 × 10 3 N/m , μ l = 440 × 10 6 kg/m s , and P r l = 9 .

Chapter 10, Problem 10.63P, A technique for cooling a multichip module involves submerging the module in a saturated

(a) For the prescribed heat dissipation, what is the required condensation rate (kg/s) and water flow rate (kg/s)?

(b) Assuming fully developed flow throughout the tube, determine the tube surface temperature at the coil inlet and outlet.

(c) Assuming a uniform tube surface temperature of T s = 53.0 ° C , determine the required length of the coil.

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I  need help on this question: (This question requires the use of Roger & Mayhew Steam Property Tables) Saturated steam at 1 atm is condensed on the external surface of a copper tube withan outside diameter 16 mm and tube wall of thickness 0.5 mm. The tube is cooledinternally by water with a mass flow rate of 0.06 kg/s, which in turn is raised intemperature from 15 oC to 60 oC as it flows through the tube.  (Take the heat-transfer coefficient at the condensing side as 10.0 kW/m2K and the isobaric specific heat-capacity of water as 4180 J/kg K.) a) To calculate the heat transfer rate to the cooling water b) To calculate the length of the tube c) Comment on how to enhance heat transfer in this case.
Carbon dioxide (CO:) is used for the gas cooled reactor in shell and tube heat exchanger type steam generator (shown in Figure 2). 90000 kg/h entered to the exchanger under pressure and temperature of 4 bar and 500 °C respectively. The steam saturation temperature is 250 °C when the carbon dioxide leave the generator at 330°C. Presume the formed steam is saturated and dry. Using 25 mm inner diameter and 2 mm wall thickness, a copper tube is designed for CO; mass flow rate of 350000 kg/m'h. Neglect the thermal resistance of the steam side. (a) Determine number of tubes that should be used (b) Determine the length of the tubes Take the following properties for the carbon dioxide: Cp=1.172 KI/kg °C; u=0.0000298 Ns/m²; k=0.043 w/m °C; p=3.26 kg/m² Take k (Copper) = 384 W/m °C Water in (cold fluid) - 250°C CO, (hot fluid) in (f = 500°C) CO, out (2 - 330°C) Steam out (2 250°C)
What are the surface condensing systems? Explain their working.

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Fundamentals of Heat and Mass Transfer

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