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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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Chemical Engineering Problem 1: Prolonged exposure to direct sunlight can cause material in pipe to heat up. Assume the following scenario: two block valves in a pipeline are closed, trapping liquid propane inside. Throughout the day, solar radiation increases the liquid propane temperature from 10 °C to 25 °C. The liquid was had an initial pressure of 10 bar. How much of a pressure increase can we expect from this temperature change? (Alternatively, external fire to the pipeline can cause temperature change) Isothermal compressibility and thermal expansion coefficients for select liquids AP range, Liquid AT range, °℃ B, °C-¹ K, bar¹ B/K, bar/°C 20 to 80 bar gauge 0-2000 28 to 165 27 to 44 25 to 150 0 to 55 Water Fuel oil Silicone oil Carbon dioxide Propane R-134a Ammonia -40 to -18 -183 to 27 -60 to 0 0 to 60 28 to 69 10 to 30 3 to 40 26 to 50 4.5-10-4 N/A 10-3 4.0-10-3 1.56-10-3 2-10-³ 2.47-10-3 3.64-10-5 N/A 1.5-10-4 4-10-4 6.18-10-4 3.09-10-4 3.7.10-4 12.4 9.3 6.7 100 2.5 6.6 6.8
Transcribed Image Text:Chemical Engineering Problem 1: Prolonged exposure to direct sunlight can cause material in pipe to heat up. Assume the following scenario: two block valves in a pipeline are closed, trapping liquid propane inside. Throughout the day, solar radiation increases the liquid propane temperature from 10 °C to 25 °C. The liquid was had an initial pressure of 10 bar. How much of a pressure increase can we expect from this temperature change? (Alternatively, external fire to the pipeline can cause temperature change) Isothermal compressibility and thermal expansion coefficients for select liquids AP range, Liquid AT range, °℃ B, °C-¹ K, bar¹ B/K, bar/°C 20 to 80 bar gauge 0-2000 28 to 165 27 to 44 25 to 150 0 to 55 Water Fuel oil Silicone oil Carbon dioxide Propane R-134a Ammonia -40 to -18 -183 to 27 -60 to 0 0 to 60 28 to 69 10 to 30 3 to 40 26 to 50 4.5-10-4 N/A 10-3 4.0-10-3 1.56-10-3 2-10-³ 2.47-10-3 3.64-10-5 N/A 1.5-10-4 4-10-4 6.18-10-4 3.09-10-4 3.7.10-4 12.4 9.3 6.7 100 2.5 6.6 6.8
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