3. Water at 300 K and a flow rate of 5 kg/s enters a black, thin-walled tube, which passes through a large furnace whose walls and air are at a temperature of 700 K. The diameter and length of the tube are 0.25 m and 8 m, respectively. Convection coefficients associated with water flow through the tube and airflow over the tube misare 300 W/m² K and 50 W/m² K, respectively. of . . Ignore water tube wall thickness and resistance. Water -Tube, D = 0.25 m L = 8 m, &= 1 Air T=700 K m = 5 kg/s Tm,i = 300 K Tm.o Furnace, Tur = 700 K 1940 1

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
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3.
Water at 300 K and a flow rate of 5 kg/s enters a black,
thin-walled tube, which passes through a large furnace
whose walls and air are at a temperature of 700 K. The
ot be diameter and length of the tube are 0.25 m and 8 m,
respectively. Convection coefficients associated with
water flow through the tube and airflow over the tube
mist are 300 W/m² K and 50 W/m². K, respectively.
Ignore water tube wall thickness and resistance.
Water
m = 5 kg/s
100Tm,i = 300 K
vilu
-Tube, D = 0.25 m
L=8m, & 1
Air
T=700 K
Imo
Furnace, Tur 700 K
1537
Ignore radiation between the tube and its surrounding, i.e.,
only consider the convection from the hot air as far as
external heat transfer is concerned, please calculate the outlet
temperature of the water flow, Tm.o
Transcribed Image Text:3. Water at 300 K and a flow rate of 5 kg/s enters a black, thin-walled tube, which passes through a large furnace whose walls and air are at a temperature of 700 K. The ot be diameter and length of the tube are 0.25 m and 8 m, respectively. Convection coefficients associated with water flow through the tube and airflow over the tube mist are 300 W/m² K and 50 W/m². K, respectively. Ignore water tube wall thickness and resistance. Water m = 5 kg/s 100Tm,i = 300 K vilu -Tube, D = 0.25 m L=8m, & 1 Air T=700 K Imo Furnace, Tur 700 K 1537 Ignore radiation between the tube and its surrounding, i.e., only consider the convection from the hot air as far as external heat transfer is concerned, please calculate the outlet temperature of the water flow, Tm.o
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