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4.7 A single equilibrium stage in a distillation column is shown in Fig. E4.7. The model that describes this stage is dt dHx1 RA +44 +44 +a, Assume that the molar holdup H in the stage is constant and that constant molal overflow occurs. Thus, Li-L and V. =リ. (a) Linearize the resulting model and introduce deviation variables. (b) For constant liquid and vapor flow rates, derive the four transfer functions relating outputs x and y, to inputs x and y2. Place it in standard form. 0 xo V1 V. 1 Figure E4.7

4.7 A single equilibrium stage in a distillation column is shown in Fig. E4.7. The model that describes this stage is dt dHx1 RA +44 +44 +a, Assume that the molar holdup H in the stage is constant and that constant molal overflow occurs. Thus, Li-L and V. =リ. (a) Linearize the resulting model and introduce deviation variables. (b) For constant liquid and vapor flow rates, derive the four transfer functions relating outputs x and y, to inputs x and y2. Place it in standard form. 0 xo V1 V. 1 Figure E4.7

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
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4.7 A single equilibrium stage in a distillation column is shown in Fig. E4.7. The model that describes this stage is dt dHx1 RA +44 +44 +a, Assume that the molar holdup H in the stage is constant and that constant molal overflow occurs. Thus, Li-L and V. =リ. (a) Linearize the resulting model and introduce deviation variables. (b) For constant liquid and vapor flow rates, derive the four transfer functions relating outputs x and y, to inputs x and y2. Place it in standard form. 0 xo V1 V. 1 Figure E4.7
Transcribed Image Text:4.7 A single equilibrium stage in a distillation column is shown in Fig. E4.7. The model that describes this stage is dt dHx1 RA +44 +44 +a, Assume that the molar holdup H in the stage is constant and that constant molal overflow occurs. Thus, Li-L and V. =リ. (a) Linearize the resulting model and introduce deviation variables. (b) For constant liquid and vapor flow rates, derive the four transfer functions relating outputs x and y, to inputs x and y2. Place it in standard form. 0 xo V1 V. 1 Figure E4.7
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