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3-110 Complete the blank cells in the following table of properties of refrigerant-134a. In the last column, describe the condition of refrigerant-134a as compressed liquid, saturated mixture, superheated vapor, or insufficient information, and, if applicable, give the quality. T, °C U, m/kg u, kJ/kg Phase description and quality (if applicable) P, kPa 320 -12 1000 39.37 40 1.17794 0.0700 180 200 249

3-110 Complete the blank cells in the following table of properties of refrigerant-134a. In the last column, describe the condition of refrigerant-134a as compressed liquid, saturated mixture, superheated vapor, or insufficient information, and, if applicable, give the quality. T, °C U, m/kg u, kJ/kg Phase description and quality (if applicable) P, kPa 320 -12 1000 39.37 40 1.17794 0.0700 180 200 249

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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3-110 Complete the blank cells in the following table of properties of refrigerant-134a. In the last column, describe the condition of refrigerant-134a as compressed liquid, saturated mixture, superheated vapor, or insufficient information, and, if applicable, give the quality. T, °C U, m/kg u, kJ/kg Phase description and quality (if applicable) P, kPa 320 -12 1000 39.37 40 1.17794 180 0.0700 200 249
Transcribed Image Text:3-110 Complete the blank cells in the following table of properties of refrigerant-134a. In the last column, describe the condition of refrigerant-134a as compressed liquid, saturated mixture, superheated vapor, or insufficient information, and, if applicable, give the quality. T, °C U, m/kg u, kJ/kg Phase description and quality (if applicable) P, kPa 320 -12 1000 39.37 40 1.17794 180 0.0700 200 249
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