Introduction to Heat Transfer
6th Edition
ISBN: 9780470501962
Author: Frank P. Incropera, David P. DeWitt, Theodore L. Bergman, Adrienne S. Lavine
Publisher: Wiley, John & Sons, Incorporated
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Question
Chapter 1, Problem 1.28P
(a)
To determine
Rate of heat loss from steam line.
(b)
To determine
Annual cost of heat loss from line.
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A pipe 30 m long with an outer diameter of 75 mm is used to deliver steam at a rate of 2000 kg / hour. The vapor pressure is 198.53 kPa entering the pipe with a quality of 98%. The pipe needs to be insulated with a thermal conductivity of 0.2 W / (m K) so that the quality of the steam will only slightly decrease to 95%. The outer surface temperature of the insulation is assumed to be 25 ° C. Ignore resistance conductive of the pipe material and it is assumed that there is no pressure drop in the pipe.
a. Determine the enthalpy of incoming vapor = AnswerkJ / kg.
b. Determine the enthalpy of steam coming out = AnswerkJ / kg.
c. Determine the vapor heat change / loss along the flow = Answerwatt.
d. Specify the minimum required insulation thickness = Answercm.
A pipe 30 m long with an outer diameter of 75 mm is used to deliver steam at a rate of 1500 kg / hour. The vapor pressure is 198.53 kPa entering the pipe with a quality of 98%. The pipe needs to be insulated with a thermal conductivity of 0.2 W / (m K) so that the quality of the steam will only slightly decrease to 95%. The outer surface temperature of the insulation is assumed to be 25 ° C. Ignore resistance conductive of the pipe material and it is assumed that there is no pressure drop in the pipe.
a. Determine the enthalpy of incoming vapor = Answer
kJ / kg.
b. Determine the enthalpy of steam coming out = Answer
kJ / kg.
c. Determine the vapor heat change / loss along the flow = Answer
watt.
d. Specify the minimum required insulation thickness = Answer
cm.
An uninsulated 100-mm diameter steam pipe runs for 25-meters inside a room whose walls and air are at a temperature of 25C .The superheated steam inside the pipe maintains the temperature at the pipe surface at 150C. If the natural convection heat transfer coefficient of the air outside the pipe is 10 W/(m^2)(k)and the surface emissivity is 0.8, compute for the total thermal resistance at the outside surface of the pipe in K/W.
Chapter 1 Solutions
Introduction to Heat Transfer
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