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For an air-water-vapour mixture of dry bulb temperature 65°C and wet bulb temperature 35°C was determined under conditions such that the radiation co-efficient can be neglected. The total pressure was 1 atm. Compute the humidity of the air. The data given are: latent heat of wet bulb temperature = 2,41,9300 J/kg, Y'w=0.0365 kg H2O/kg dry air, pAir = 1.060 kg/m²,Hair = 1.95 × 10° kg/m-s, DAB = 2.58 × 10$ m²/s

For an air-water-vapour mixture of dry bulb temperature 65°C and wet bulb temperature 35°C was determined under conditions such that the radiation co-efficient can be neglected. The total pressure was 1 atm. Compute the humidity of the air. The data given are: latent heat of wet bulb temperature = 2,41,9300 J/kg, Y'w=0.0365 kg H2O/kg dry air, pAir = 1.060 kg/m²,Hair = 1.95 × 10° kg/m-s, DAB = 2.58 × 10$ m²/s

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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For an air-water-vapour mixture of dry bulb temperature 65°C and wet bulb temperature 35°C was determined under conditions such that the radiation co-efficient can be neglected. The total pressure was 1 atm. Compute the humidity of the air. The data given are: latent heat of wet bulb temperature = 2,41,9300 J/kg, Y'w= 0.0365 kg H2O/kg dry air, Pair = 1.060 kg/m²,µAir = 1.95 × 10³ kg/m-s, DAB = 2.58 × 10$ m²/s
Transcribed Image Text:For an air-water-vapour mixture of dry bulb temperature 65°C and wet bulb temperature 35°C was determined under conditions such that the radiation co-efficient can be neglected. The total pressure was 1 atm. Compute the humidity of the air. The data given are: latent heat of wet bulb temperature = 2,41,9300 J/kg, Y'w= 0.0365 kg H2O/kg dry air, Pair = 1.060 kg/m²,µAir = 1.95 × 10³ kg/m-s, DAB = 2.58 × 10$ m²/s
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