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Q4/ Air at 0°C and 1 atm flows at a velocity of 6 m/s across a rectangular plate at a uniform temperature of 120 °C. If the dimension of the plate perpendicular to flow is 3 m and plate in the flow direction is 1.5 m, find: a) local heat transfer coefficient at the trailing edge b) the average heat transfer coefficient for the entire plate c) convective heat transfer from the plate. Given v 19.21 × 106 m²/s, k= 0.03 w/ m.k, pr=0.7 (2

Q4/ Air at 0°C and 1 atm flows at a velocity of 6 m/s across a rectangular plate at a uniform temperature of 120 °C. If the dimension of the plate perpendicular to flow is 3 m and plate in the flow direction is 1.5 m, find: a) local heat transfer coefficient at the trailing edge b) the average heat transfer coefficient for the entire plate c) convective heat transfer from the plate. Given v 19.21 × 106 m²/s, k= 0.03 w/ m.k, pr=0.7 (2

Introduction to Chemical Engineering Thermodynamics
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
Problem 1.1P
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Q4/ Air at 0°C and 1 atm flows at a velocity of 6 m/s across a rectangular plate at a uniform temperature of 120 °C. If the dimension of the plate perpendicular to flow is 3 m and plate in the flow direction is 1.5 m, find: a) local heat transfer coefficient at the trailing edge b) the average heat transfer coefficient for the entire plate c) convective heat transfer from the plate. Given v 19.21 × 106 m²/s, k= 0.03 w/ m.k, pr=0.7 (2
Transcribed Image Text:Q4/ Air at 0°C and 1 atm flows at a velocity of 6 m/s across a rectangular plate at a uniform temperature of 120 °C. If the dimension of the plate perpendicular to flow is 3 m and plate in the flow direction is 1.5 m, find: a) local heat transfer coefficient at the trailing edge b) the average heat transfer coefficient for the entire plate c) convective heat transfer from the plate. Given v 19.21 × 106 m²/s, k= 0.03 w/ m.k, pr=0.7 (2
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