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Μγ m = CAP, MY (2) P(t) = = RTƒ Pf.t=0 C₁tRTƒ e MV Y+1 Y-1 (2) (3) My C₁ = COA RTf V+1 2 V-1 +1 (4) -) Using equations (2) & (3) above along with ideal gas flow rate equation for unchoked flow, assuming that these hold for the case of a rupture in a pipe, determine the corresponding variation of mass release rate with time in the first 11 s following pipe failure, presenting the results in both in tabular and graphical forms at 0.5 s intervals. You may assume that post pipe failure, immediate transition of the liquid ammonia occupying the entire volume of the pipe to the gas phase occurs at constant temperature, and that the feed flow into the pipe is terminated immediately after failure using an emergency shutdown valve. In performing your calculations, clearly state any equations used along with the definitions of symbols.

Μγ m = CAP, MY (2) P(t) = = RTƒ Pf.t=0 C₁tRTƒ e MV Y+1 Y-1 (2) (3) My C₁ = COA RTf V+1 2 V-1 +1 (4) -) Using equations (2) & (3) above along with ideal gas flow rate equation for unchoked flow, assuming that these hold for the case of a rupture in a pipe, determine the corresponding variation of mass release rate with time in the first 11 s following pipe failure, presenting the results in both in tabular and graphical forms at 0.5 s intervals. You may assume that post pipe failure, immediate transition of the liquid ammonia occupying the entire volume of the pipe to the gas phase occurs at constant temperature, and that the feed flow into the pipe is terminated immediately after failure using an emergency shutdown valve. In performing your calculations, clearly state any equations used along with the definitions of symbols.

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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y+1 2 Y-1 (₁²₂) +-₁ (2) (3) = MY RT f ,t=0 Pf,t= C₁tRT f e MV m = C, APf Co P(t) = My 2 RTf C₁ = C₂A (4) +1. iv) Using equations (2) & (3) above along with ideal gas flow rate equation for unchoked flow, assuming that these hold for the case of a rupture in a pipe, determine the corresponding variation of mass release rate with time in the first 11 s following pipe failure, presenting the results in both in tabular and graphical forms at 0.5 s intervals. You may assume that post pipe failure, immediate transition of the liquid ammonia occupying the entire volume of the pipe to the gas phase occurs at constant temperature, and that the feed flow into the pipe is terminated immediately after failure using an emergency shutdown valve. In performing your calculations, clearly state any equations used along with the definitions of symbols. Y+1 y-1
Transcribed Image Text:y+1 2 Y-1 (₁²₂) +-₁ (2) (3) = MY RT f ,t=0 Pf,t= C₁tRT f e MV m = C, APf Co P(t) = My 2 RTf C₁ = C₂A (4) +1. iv) Using equations (2) & (3) above along with ideal gas flow rate equation for unchoked flow, assuming that these hold for the case of a rupture in a pipe, determine the corresponding variation of mass release rate with time in the first 11 s following pipe failure, presenting the results in both in tabular and graphical forms at 0.5 s intervals. You may assume that post pipe failure, immediate transition of the liquid ammonia occupying the entire volume of the pipe to the gas phase occurs at constant temperature, and that the feed flow into the pipe is terminated immediately after failure using an emergency shutdown valve. In performing your calculations, clearly state any equations used along with the definitions of symbols. Y+1 y-1
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