Tools

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003 WaSeSS;

005 20210312081412.0;

006 m d ;

007 cr n ;

008 100901s2011 enka sb 001 0 eng d;

010 a| 2010034824;

016 7 a| 0157115152| Uk;

020 a| 9780470975879 (cloth);

020 a| 0470975873 (cloth);

035 a| (WaSeSS)ssib043237494;

042 a| pcc;

049 a| EREEa| NEHH;

050 00 a| TP155.75b| .K56 2011;

082 00 a| 660/.28152| 22;

084 a| 85.032| bcl;

100 1 a| King, Myke,d| 1951-?| UNAUTHORIZED;

245 10 a| Process controlh| [electronic resource] :b| a practical approach /c| Myke King.;

260 a| Chicester, West Sussex :b| Wiley,;

300 a| xv, 400 p. :b| ill. (some col.) ;c| 25 cm.;

504 a| Includes bibliographical references and index.;

505 00 g| Machine generated contents note:g| 1.t| Introduction --g| 2.t| Process Dynamics --g| 2.1.t| Definition --g| 2.2.t| Cascade Control --g| 2.3.t| Model Identification --g| 2.4.t| Integrating Processes --g| 2.5.t| Other Types of Process --g| 2.6.t| Robustness --g| 2.7.t| Laplace Transforms for Processes --t| References --g| 3.t| PID Algorithm --g| 3.1.t| Definitions --g| 3.2.t| Proportional Action --g| 3.3.t| Integral Action --g| 3.4.t| Derivative Action --g| 3.5.t| Versions of Control Algorithm --g| 3.6.t| Interactive PID Controller --g| 3.7.t| Proportional-on-PV Controller --g| 3.8.t| Nonstandard Algorithms --g| 3.9.t| Tuning --g| 3.10.t| Ziegler-Nichols Tuning Method --g| 3.11.t| Cohen-Coon Tuning Method --g| 3.12.t| Tuning Based on Penalty Functions --g| 3.13.t| Manipulated Variable Overshoot --g| 3.14.t| Lambda Tuning Method --g| 3.15.t| IMC Tuning Method --g| 3.16.t| Choice of Tuning Method --g| 3.17.t| Suggested Tuning Method for Self-Regulating Processes;

505 00 g| 3.18.t| Tuning for Load Changes --g| 3.19.t| Tuning for Unconstrained MV Overshoot --g| 3.20.t| PI Tuning Compared to PID Tuning --g| 3.21.t| Tuning for Large Scan Interval --g| 3.22.t| Suggested Tuning Method for Integrating Processes --g| 3.23.t| Implementation of Tuning --g| 3.24.t| Loop Gain --g| 3.25.t| Adaptive Tuning --g| 3.26.t| Initialisation --g| 3.27.t| Anti-Reset Windup --g| 3.28.t| On-Off Control --g| 3.29.t| Laplace Transforms for Controllers --g| 3.30.t| Direct Synthesis --t| References --g| 4.t| Level Control --g| 4.1.t| Use of Cascade Control --g| 4.2.t| Parameters Required for Tuning Calculations --g| 4.3.t| Tight Level Control --g| 4.4.t| Averaging Level Control --g| 4.5.t| Error-Squared Controller --g| 4.6.t| Gap Controller --g| 4.7.t| Impact of Noise on Averaging Control --g| 4.8.t| General Approach to Tuning --g| 4.9.t| Three-Element Level Control --g| 5.t| Signal Conditioning --g| 5.1.t| Instrument Linearisation --g| 5.2.t| Process Linearisation --g| 5.3.t| Constraint Conditioning --g| 5.4.t| Pressure Compensation of Distillation Tray Temperature;

505 00 g| 5.5.t| Pressure Compensation of Gas Flow Measurement --g| 5.6.t| Filtering --g| 5.7.t| Exponential Filter --g| 5.8.t| Higher Order Filters --g| 5.9.t| Nonlinear Exponential Filter --g| 5.10.t| Averaging Filter --g| 5.11.t| Least Squares Filter --g| 5.12.t| Control Valve Characterisation --g| 5.13.t| Equal Percentage Valve --g| 5.14.t| Split-Range Valves --g| 6.t| Feedforward Control --g| 6.1.t| Ratio Algorithm --g| 6.2.t| Bias Algorithm --g| 6.3.t| Deadtime and Lead-Lag Algorithms --g| 6.4.t| Tuning --g| 6.5.t| Laplace Derivation of Dynamic Compensation --g| 7.t| Deadtime Compensation --g| 7.1.t| Smith Predictor --g| 7.2.t| Internal Model Control --g| 7.3.t| Dahlin Algorithm --t| References --g| 8.t| Multivariate Control --g| 8.1.t| Constraint Control --g| 8.2.t| SISO Constraint Control --g| 8.3.t| Signal Selectors --g| 8.4.t| Relative Gain Analysis --g| 8.5.t| Steady State Decoupling --g| 8.6.t| Dynamic Decoupling --g| 8.7.t| MVC Principles --g| 8.8.t| Parallel Coordinates --g| 8.9.t| Enhanced Operator Displays --g| 8.10.t| MVC Performance Monitoring --t| References;

505 00 g| 9.t| Inferential and Analysers --g| 9.1.t| Inferential Properties --g| 9.2.t| Assessing Accuracy --g| 9.3.t| Laboratory Update of Inferential --g| 9.4.t| Analyser Update of Inferential --g| 9.5.t| Monitoring On-stream Analysers --t| Reference --g| 10.t| Combustion Control --g| 10.1.t| Fuel Gas Flow Correction --g| 10.2.t| Measuring NHV --g| 10.3.t| Dual Firing --g| 10.4.t| Inlet Temperature Feedforward --g| 10.5.t| Fuel Pressure Control --g| 10.6.t| Combustion Air Control --g| 10.7.t| Boiler Control --g| 10.8.t| Fired Heater Pass Balancing --g| 11.t| Compressor Control --g| 11.1.t| Polytropic Head --g| 11.2.t| Flow Control (Turbo-Machines) --g| 11.3.t| Flow Control (Reciprocating Machines) --g| 11.4.t| Anti-Surge Control --g| 12.t| Distillation Control --g| 12.1.t| Key Components --g| 12.2.t| Relative Volatility --g| 12.3.t| McCabe-Thiele Diagram --g| 12.4.t| Cut and Separation --g| 12.5.t| Effect of Process Design --g| 12.6.t| Basic Controls --g| 12.7.t| Pressure Control --g| 12.8.t| Level Control --g| 12.9.t| Tray Temperature Control;

505 00 g| 12.10.t| Pressure Compensated Temperature --g| 12.11.t| Inferentials --g| 12.12.t| First-Principle Inferentials --g| 12.13.t| Feedforward on Feed Rate --g| 12.14.t| Feed Composition Feedforward --g| 12.15.t| Feed Enthalpy Feedforward --g| 12.16.t| Decoupling --g| 12.17.t| Multivariable Control --g| 12.18.t| On-stream Analysers --g| 12.19.t| Towers with Sidestreams --g| 12.20.t| Column Optimisation --g| 12.21.t| Optimisation of Column Pressure --g| 12.22.t| Energy/Yield Optimisation --t| References --g| 13.t| APC Project Execution --g| 13.1.t| Benefits Study --g| 13.2.t| Benefit Estimation for Improved Regulatory Control --g| 13.3.t| Benefits of Closed-Loop Real-Time Optimisation --g| 13.4.t| Basic Controls --g| 13.5.t| Inferentials --g| 13.6.t| Organisation --g| 13.7.t| Vendor Selection --g| 13.8.t| Safety in APC Design --g| 13.9.t| Alarms --t| References.;

506 a| Available only to authorized users.;

538 a| Mode of access: World Wide Web;

650 0 a| Chemical process control.=| ^A216044;

655 0 a| Electronic books.=| ^A491897;

856 40 z| Full text available from Ebook Central - Academic Completeu| https://ebookcentral.proquest.com/lib/eastcarolina/detail.action?docID=624654;

947 a| (OCoLC)ocn662152657;

949 a| CLICK ON WEB ADDRESSw| ASISh| JOYNER188;

949 a| CLICK ON WEB ADDRESSw| ASISh| HSL77;

949 a| CLICK ON WEB ADDRESSw| ASISh| JMUSIC60;

596 a| 1 3 4;

998 a| 5577118;

999 a| CLICK ON WEB ADDRESSw| ASISc| 1i| 5577118-1001l| JNETm| JOYNERr| Ys| Yt| JNESSBKu| 3/17/2021x| EBOOKz| JERESOURCE;

999 a| CLICK ON WEB ADDRESSw| ASISc| 1i| 5577118-2001l| HSLELECm| HSLr| Ys| Yt| HEBKu| 3/17/2021x| EBOOKz| HERESOURCE;

999 a| CLICK ON WEB ADDRESSw| ASISc| 1i| 5577118-3001l| MNETm| JMUSICr| Ys| Yt| MNESSBKu| 3/17/2021x| EBOOKz| JERESOURCE;

Process control a practical approach / Myke King.

Author/creator	King, Myke, 1951-
Format	Electronic
Publication Info	Chicester, West Sussex : Wiley,
Description	xv, 400 p. : ill. (some col.) ; 25 cm.
Supplemental Content	Full text available from Ebook Central - Academic Complete
Subjects	Chemical process control.

Contents	Machine generated contents note: 1. Introduction -- 2. Process Dynamics -- 2.1. Definition -- 2.2. Cascade Control -- 2.3. Model Identification -- 2.4. Integrating Processes -- 2.5. Other Types of Process -- 2.6. Robustness -- 2.7. Laplace Transforms for Processes -- References -- 3. PID Algorithm -- 3.1. Definitions -- 3.2. Proportional Action -- 3.3. Integral Action -- 3.4. Derivative Action -- 3.5. Versions of Control Algorithm -- 3.6. Interactive PID Controller -- 3.7. Proportional-on-PV Controller -- 3.8. Nonstandard Algorithms -- 3.9. Tuning -- 3.10. Ziegler-Nichols Tuning Method -- 3.11. Cohen-Coon Tuning Method -- 3.12. Tuning Based on Penalty Functions -- 3.13. Manipulated Variable Overshoot -- 3.14. Lambda Tuning Method -- 3.15. IMC Tuning Method -- 3.16. Choice of Tuning Method -- 3.17. Suggested Tuning Method for Self-Regulating Processes
Contents	3.18. Tuning for Load Changes -- 3.19. Tuning for Unconstrained MV Overshoot -- 3.20. PI Tuning Compared to PID Tuning -- 3.21. Tuning for Large Scan Interval -- 3.22. Suggested Tuning Method for Integrating Processes -- 3.23. Implementation of Tuning -- 3.24. Loop Gain -- 3.25. Adaptive Tuning -- 3.26. Initialisation -- 3.27. Anti-Reset Windup -- 3.28. On-Off Control -- 3.29. Laplace Transforms for Controllers -- 3.30. Direct Synthesis -- References -- 4. Level Control -- 4.1. Use of Cascade Control -- 4.2. Parameters Required for Tuning Calculations -- 4.3. Tight Level Control -- 4.4. Averaging Level Control -- 4.5. Error-Squared Controller -- 4.6. Gap Controller -- 4.7. Impact of Noise on Averaging Control -- 4.8. General Approach to Tuning -- 4.9. Three-Element Level Control -- 5. Signal Conditioning -- 5.1. Instrument Linearisation -- 5.2. Process Linearisation -- 5.3. Constraint Conditioning -- 5.4. Pressure Compensation of Distillation Tray Temperature
Contents	5.5. Pressure Compensation of Gas Flow Measurement -- 5.6. Filtering -- 5.7. Exponential Filter -- 5.8. Higher Order Filters -- 5.9. Nonlinear Exponential Filter -- 5.10. Averaging Filter -- 5.11. Least Squares Filter -- 5.12. Control Valve Characterisation -- 5.13. Equal Percentage Valve -- 5.14. Split-Range Valves -- 6. Feedforward Control -- 6.1. Ratio Algorithm -- 6.2. Bias Algorithm -- 6.3. Deadtime and Lead-Lag Algorithms -- 6.4. Tuning -- 6.5. Laplace Derivation of Dynamic Compensation -- 7. Deadtime Compensation -- 7.1. Smith Predictor -- 7.2. Internal Model Control -- 7.3. Dahlin Algorithm -- References -- 8. Multivariate Control -- 8.1. Constraint Control -- 8.2. SISO Constraint Control -- 8.3. Signal Selectors -- 8.4. Relative Gain Analysis -- 8.5. Steady State Decoupling -- 8.6. Dynamic Decoupling -- 8.7. MVC Principles -- 8.8. Parallel Coordinates -- 8.9. Enhanced Operator Displays -- 8.10. MVC Performance Monitoring -- References
Contents	9. Inferential and Analysers -- 9.1. Inferential Properties -- 9.2. Assessing Accuracy -- 9.3. Laboratory Update of Inferential -- 9.4. Analyser Update of Inferential -- 9.5. Monitoring On-stream Analysers -- Reference -- 10. Combustion Control -- 10.1. Fuel Gas Flow Correction -- 10.2. Measuring NHV -- 10.3. Dual Firing -- 10.4. Inlet Temperature Feedforward -- 10.5. Fuel Pressure Control -- 10.6. Combustion Air Control -- 10.7. Boiler Control -- 10.8. Fired Heater Pass Balancing -- 11. Compressor Control -- 11.1. Polytropic Head -- 11.2. Flow Control (Turbo-Machines) -- 11.3. Flow Control (Reciprocating Machines) -- 11.4. Anti-Surge Control -- 12. Distillation Control -- 12.1. Key Components -- 12.2. Relative Volatility -- 12.3. McCabe-Thiele Diagram -- 12.4. Cut and Separation -- 12.5. Effect of Process Design -- 12.6. Basic Controls -- 12.7. Pressure Control -- 12.8. Level Control -- 12.9. Tray Temperature Control
Contents	12.10. Pressure Compensated Temperature -- 12.11. Inferentials -- 12.12. First-Principle Inferentials -- 12.13. Feedforward on Feed Rate -- 12.14. Feed Composition Feedforward -- 12.15. Feed Enthalpy Feedforward -- 12.16. Decoupling -- 12.17. Multivariable Control -- 12.18. On-stream Analysers -- 12.19. Towers with Sidestreams -- 12.20. Column Optimisation -- 12.21. Optimisation of Column Pressure -- 12.22. Energy/Yield Optimisation -- References -- 13. APC Project Execution -- 13.1. Benefits Study -- 13.2. Benefit Estimation for Improved Regulatory Control -- 13.3. Benefits of Closed-Loop Real-Time Optimisation -- 13.4. Basic Controls -- 13.5. Inferentials -- 13.6. Organisation -- 13.7. Vendor Selection -- 13.8. Safety in APC Design -- 13.9. Alarms -- References.
Bibliography note	Includes bibliographical references and index.
Access restriction	Available only to authorized users.
Technical details	Mode of access: World Wide Web
Genre/form	Electronic books.
LCCN	2010034824
ISBN	9780470975879 (cloth)
ISBN	0470975873 (cloth)

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