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Batch Distillation: Simulation, Optimal Design, And Control (Series in Chemical and Mechanical Engineering)
 
 
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Batch Distillation: Simulation, Optimal Design, And Control (Series in Chemical and Mechanical Engineering) [Hardcover]

Urmila Diwekar (Author)

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Book Description

1560323248 978-1560323242 August 1, 1995 1
Introducing various operating modes in detail, Batch Distillation: Simulation, Optimal Design, And Control examines the challenges involved in a rigorous modeling of batch distillation column dynamics, and describes optimal control problems. The text discusses the design or operation of specialty chemical processes as well as errors and perils associated with numerical models solved by computers. A derived equation is supplied with each model discussed along with a table that breaks down the model into assumptions, composition calculation equations, flow rate equations, heavy duty calculations, and thermodynamic models.

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Inside This Book (learn more)
First Sentence:
Distillation is the oldest separation process and the most widely used unit operation in industry. Read the first page
Key Phrases - Statistically Improbable Phrases (SIPs): (learn more)
maximum distillate problem, vapor boilup rate, shortcut method equations, reflux mode, collocation model, differential material balance equation, multicomponent batch distillation columns, batch distillation operation, holdup effects, average distillate composition, binary azeotropic systems, reboiler dynamics, maximum principle formulation, constant reflux operation, plate holdup, condenser holdup, flowrate calculations, optimal reflux, residue curve map, batch rectification, total reflux condition, purity constraint, total reflux operation, binary batch distillation, reflux policy
Key Phrases - Capitalized Phrases (CAPs): (learn more)
Chemical Engineering Science, New York, Academic Press, Heat Duty Calculations Condenser Duty, Journal of Numerical Analysis, Numerische Mathematik, Industrial Engineering Chemistry Fundamentals, Englewood Cliffs, John Wiley, New Jersey, New Mexico, Quaternary System, Sandia National Laboratory, Thermodynamics Models Equilibrium Relations, Department of Computer Science, Equations Number Differential Material Balance Equations, Indian Institute of Technology, Integration Termination Criterion, The Underwood Equation, Thermodynamics Correlations Equilibrium Relations
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