Process Dynamics and ControlThis third edition provides chemical engineers with process control techniques that are used in practice while offering detailed mathematical analysis. Numerous examples and simulations are used to illustrate key theoretical concepts. New exercises are integrated throughout several chapters to reinforce concepts. Up-to-date information is also included on real-time optimization and model predictive control to highlight the significant impact these techniques have on industrial practice. And chemical engineers will find two new chapters on biosystems control to gain the latest perspective in the field. |
Contents
INTRODUCTION TO PROCESS CONTROL | 1 |
www wiley comcollegeseborg Second edition Chapter | 14 |
Laplace Transforms 40 | 34 |
Models 103 | 114 |
Control System Instrumentation | 150 |
Dynamic Behavior and Stability | 183 |
Control 237 | 251 |
Control 283 | 289 |
Digital Sampling Filtering and Control | 316 |
Multiloop and Multivariable Control | 341 |
RealTime Optimization | 367 |
Process Monitoring 411 | 386 |
Batch Process Control 429 | 399 |
Instrumentation Symbols 499 | 406 |
Introduction to Plantwide | 414 |
Other editions - View all
Process Dynamics and Control Dale E. Seborg,Thomas F. Edgar,Duncan A. Mellichamp,Francis J. Doyle, III Limited preview - 2016 |
Common terms and phrases
analysis applications approach approximate assume calculated Chapter characteristic chart closed-loop column composition consider constant control loop control system control valve controlled variable delay derivative determine developed deviation discussed disturbance dynamic effect element equal equation error example expressed feed feedback control Figure filter first-order flow rate frequency gain given gives heat important increase indicates input integral limits linear liquid loop manipulated variables mass measurement method nonlinear normal Note obtained occurs operating optimization output pairing parameters performance period phase PID controller plant plot pressure problems process control range reactor referred response result sampling set point shown in Fig shows signal SOLUTION specified stability standard steady-state step step change stream Table tank techniques temperature tion transfer function unit vari variables zero