59 Skogestad PPTs View free & download

PID Tuning and Controllability Sigurd Skogestad NTNU, Trondheim, Norway PowerPoint PPT Presentation

PID Tuning and Controllability Sigurd Skogestad NTNU, Trondheim, Norway - PID Tuning and Controllability Sigurd Skogestad NTNU, Trondheim, Norway Tuning of PID controllers SIMC tuning rules ( Skogestad IMC )(*) Main message: Can usually ...

PID Tuning and Controllability Sigurd Skogestad NTNU, Trondheim, Norway Tuning of PID controllers SIMC tuning rules ( Skogestad IMC )(*) Main message: Can usually ...

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PID Tuning Sigurd Skogestad NTNU, Trondheim, Norway PowerPoint PPT Presentation

PID Tuning Sigurd Skogestad NTNU, Trondheim, Norway - Algebra: IMC Tuning = Direct Synthesis ... Delay-free process ( =0) ... If the plant is not controllable then improved tuning will not help. Alternatives ...

Algebra: IMC Tuning = Direct Synthesis ... Delay-free process ( =0) ... If the plant is not controllable then improved tuning will not help. Alternatives ...

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Fremtidige trender innen prosessoptimalisering PowerPoint PPT Presentation

Fremtidige trender innen prosessoptimalisering - Fremtidige trender innen prosessoptimalisering Sigurd Skogestad Institutt for kjemisk prosessteknologi NTNU, Trondheim Effective Implementation of optimal operation ...

Fremtidige trender innen prosessoptimalisering Sigurd Skogestad Institutt for kjemisk prosessteknologi NTNU, Trondheim Effective Implementation of optimal operation ...

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Modelling solid heat exchanger NPK 4 PowerPoint PPT Presentation

Modelling solid heat exchanger NPK 4 - Modelling solid heat exchanger NPK 4 Bj rn Tore Mathisen Supervisor: Sigurd Skogestad Yara Supervisor: Jakub Bujalski Start up Project restructuring

Modelling solid heat exchanger NPK 4 Bj rn Tore Mathisen Supervisor: Sigurd Skogestad Yara Supervisor: Jakub Bujalski Start up Project restructuring

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Feedback: The simple and best solution. Applications to self-optimizing control and stabilization of new operating regimes PowerPoint PPT Presentation

Feedback: The simple and best solution. Applications to self-optimizing control and stabilization of new operating regimes - Title: Engelske lysark 2001 Author: Infoavdelingen Last modified by: Sigurd Skogestad Created Date: 10/19/1998 12:17:04 PM Document presentation format

Title: Engelske lysark 2001 Author: Infoavdelingen Last modified by: Sigurd Skogestad Created Date: 10/19/1998 12:17:04 PM Document presentation format

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Ingen lysbildetittel PowerPoint PPT Presentation

Ingen lysbildetittel - Optimal operation of energy storage in buildings: The use of hot water system Emma Johansson Supervisors: Sigurd Skogestad and Vinicius de Oliveira

Optimal operation of energy storage in buildings: The use of hot water system Emma Johansson Supervisors: Sigurd Skogestad and Vinicius de Oliveira

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PLANTWIDE CONTROL PowerPoint PPT Presentation

PLANTWIDE CONTROL - Title: Plantwide control: Towards a systematic procedure Author: norevik Last modified by: Sigurd Skogestad Created Date: 1/3/2002 2:27:29 PM Document presentation format

Title: Plantwide control: Towards a systematic procedure Author: norevik Last modified by: Sigurd Skogestad Created Date: 1/3/2002 2:27:29 PM Document presentation format

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Ingen lysbildetittel - The dos and don ts of distillation column control Sigurd Skogestad Norwegian University of Science and Technology NTNU N-7491 Trondheim, Norway

The dos and don ts of distillation column control Sigurd Skogestad Norwegian University of Science and Technology NTNU N-7491 Trondheim, Norway

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Practical Implementation of Optimal Operation using Off-Line Computations PowerPoint PPT Presentation

Practical Implementation of Optimal Operation using Off-Line Computations - Title: Plantwide control: Towards a systematic procedure Author: norevik Last modified by: Sigurd Skogestad Created Date: 1/3/2002 2:27:29 PM Document presentation format

Title: Plantwide control: Towards a systematic procedure Author: norevik Last modified by: Sigurd Skogestad Created Date: 1/3/2002 2:27:29 PM Document presentation format

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Plantwide%20control:%20Towards%20a%20systematic%20procedure PowerPoint PPT Presentation

Plantwide%20control:%20Towards%20a%20systematic%20procedure - Production rate set inside process. March 2002. S. Skogestad. 36 ... A review and a new design procedure', Modeling, Identification and Control, 21, 209-240. ...

Production rate set inside process. March 2002. S. Skogestad. 36 ... A review and a new design procedure', Modeling, Identification and Control, 21, 209-240. ...

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Lynkurs Prosessregulering (Crash course process control) PowerPoint PPT Presentation

Lynkurs Prosessregulering (Crash course process control) - Lynkurs Prosessregulering (Crash course process control) Sigurd Skogestad Institutt for kjemisk prosessteknologi Rom K4-232 skoge@ntnu.no Pensum (syllabus): Lectures ...

Lynkurs Prosessregulering (Crash course process control) Sigurd Skogestad Institutt for kjemisk prosessteknologi Rom K4-232 skoge@ntnu.no Pensum (syllabus): Lectures ...

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ECONOMIC PLANTWIDE CONTROL: Control structure design for complete processing plants PowerPoint PPT Presentation

ECONOMIC PLANTWIDE CONTROL: Control structure design for complete processing plants - Title: Plantwide control: Towards a systematic procedure Author: norevik Last modified by: Sigurd Skogestad Created Date: 1/3/2002 2:27:29 PM Document presentation format

Title: Plantwide control: Towards a systematic procedure Author: norevik Last modified by: Sigurd Skogestad Created Date: 1/3/2002 2:27:29 PM Document presentation format

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Optimal output selection for batch processes PowerPoint PPT Presentation

Optimal output selection for batch processes - H kon Dahl-Olsen, Sridharakumar Narasimhan. and Sigurd Skogestad ... Look for variables which give small deviation from optimality when controlled at ...

H kon Dahl-Olsen, Sridharakumar Narasimhan. and Sigurd Skogestad ... Look for variables which give small deviation from optimality when controlled at ...

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Internal Model Control IMC PowerPoint PPT Presentation

Internal Model Control IMC - (Chien and Fruehauf, 1990) (Skogestad, 2003) Controller Tuning Relations ... Table 12.1 IMC-Based PID Controller Settings for Gc(s) (Chien and Fruehauf, 1990) ...

(Chien and Fruehauf, 1990) (Skogestad, 2003) Controller Tuning Relations ... Table 12.1 IMC-Based PID Controller Settings for Gc(s) (Chien and Fruehauf, 1990) ...

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ECONOMIC PLANTWIDE CONTROL: Control structure design for complete processing plants - ECONOMIC PLANTWIDE CONTROL: Control structure design for complete processing plants Sigurd Skogestad Department of Chemical Engineering Norwegian University of ...

ECONOMIC PLANTWIDE CONTROL: Control structure design for complete processing plants Sigurd Skogestad Department of Chemical Engineering Norwegian University of ...

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Outline - Title: Plantwide control: Towards a systematic procedure Author: norevik Last modified by: Sigurd Skogestad Created Date: 1/3/2002 2:27:29 PM Document presentation format

Title: Plantwide control: Towards a systematic procedure Author: norevik Last modified by: Sigurd Skogestad Created Date: 1/3/2002 2:27:29 PM Document presentation format

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USE OF PERFECT INDIRECT CONTROL TO MINIMIZE STATE DEVIATIONS Eduardo Shigueo Hori, Wu Hong Kwong Federal University of S PowerPoint PPT Presentation

USE OF PERFECT INDIRECT CONTROL TO MINIMIZE STATE DEVIATIONS Eduardo Shigueo Hori, Wu Hong Kwong Federal University of S - Federal University of S o Carlos. S o Carlos/SP Brazil. Sigurd Skogestad ... Although the choice of top and bottom compositions as primary variables ...

Federal University of S o Carlos. S o Carlos/SP Brazil. Sigurd Skogestad ... Although the choice of top and bottom compositions as primary variables ...

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Control limitations for unstable plants PowerPoint PPT Presentation

Control limitations for unstable plants - Performance limitation for unstable plant when combined with unstable (RHP) zero ' ... Seron, Braslavsky and Goodwin (1997) str m (1997) ...

Performance limitation for unstable plant when combined with unstable (RHP) zero ' ... Seron, Braslavsky and Goodwin (1997) str m (1997) ...

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Modelling of Biodiesel Production Marianne PowerPoint PPT Presentation

Modelling of Biodiesel Production Marianne - Title: Ingen lysbildetittel Author: Marianne Last modified by: Marianne Created Date: 8/16/2002 11:58:11 AM Document presentation format: Skjermfremvisning (4:3)

Title: Ingen lysbildetittel Author: Marianne Last modified by: Marianne Created Date: 8/16/2002 11:58:11 AM Document presentation format: Skjermfremvisning (4:3)

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Integrated%20Process%20Networks:%20Nonlinear%20Control%20System%20Design%20for%20Optimality%20and%20Dynamic%20Performance PowerPoint PPT Presentation

Integrated%20Process%20Networks:%20Nonlinear%20Control%20System%20Design%20for%20Optimality%20and%20Dynamic%20Performance - Michael Baldeaa,b and Prodromos Daoutidisa. aUniversity of Minnesota, ... Moves across product slate due to frequent. changes in market conditions and economics ...

Michael Baldeaa,b and Prodromos Daoutidisa. aUniversity of Minnesota, ... Moves across product slate due to frequent. changes in market conditions and economics ...

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Operation of Divided Wall (Petlyuk) Column at energy lower than minimum energy PowerPoint PPT Presentation

Operation of Divided Wall (Petlyuk) Column at energy lower than minimum energy - Title: Ingen lysbildetittel Author: Ambari Last modified by: Ambari Created Date: 8/16/2002 11:58:11 AM Document presentation format: On-screen Show (4:3)

Title: Ingen lysbildetittel Author: Ambari Last modified by: Ambari Created Date: 8/16/2002 11:58:11 AM Document presentation format: On-screen Show (4:3)

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Control Structure Design: New Developments and Future Directions PowerPoint PPT Presentation

Control Structure Design: New Developments and Future Directions - 2. Control Structure Design. Challenges. Tools (partial ... Kandepu et al., Proceedings of SIMS, Trondheim, Norway, 2005. 24. Extra Manipulated Variables ...

2. Control Structure Design. Challenges. Tools (partial ... Kandepu et al., Proceedings of SIMS, Trondheim, Norway, 2005. 24. Extra Manipulated Variables ...

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Controller Design (to determine controller settings for P, PI or PID controllers) Based on Transient Response Criteria PowerPoint PPT Presentation

Controller Design (to determine controller settings for P, PI or PID controllers) Based on Transient Response Criteria - Title: No Slide Title Author: Preferred Customer Last modified by: ncku Created Date: 12/14/1998 6:48:55 PM Document presentation format:

Title: No Slide Title Author: Preferred Customer Last modified by: ncku Created Date: 12/14/1998 6:48:55 PM Document presentation format:

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PLANTWIDE CONTROL - Title: Plantwide control: Towards a systematic procedure Author: norevik Last modified by: Administrator Created Date: 1/3/2002 2:27:29 PM Document presentation format

Title: Plantwide control: Towards a systematic procedure Author: norevik Last modified by: Administrator Created Date: 1/3/2002 2:27:29 PM Document presentation format

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Modeling of a CO2-stripper PowerPoint PPT Presentation

Modeling of a CO2-stripper - ... hf B, xB LT, XLT QR 75 stages including reboiler and reflux tank Bottom product ... PowerPoint Presentation Author: Sajy Bhaskaran Last modified by:

... hf B, xB LT, XLT QR 75 stages including reboiler and reflux tank Bottom product ... PowerPoint Presentation Author: Sajy Bhaskaran Last modified by:

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Implementation of Coordinator MPC on a Large-Scale Gas Plant PowerPoint PPT Presentation

Implementation of Coordinator MPC on a Large-Scale Gas Plant - 1. Implementation of Coordinator MPC on a Large-Scale Gas Plant ... Naphtha. Ethane. Condensate. Sleipner. condensate. Tampen rich gas. Halten/ Nordland rich gas ...

1. Implementation of Coordinator MPC on a Large-Scale Gas Plant ... Naphtha. Ethane. Condensate. Sleipner. condensate. Tampen rich gas. Halten/ Nordland rich gas ...

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Introduction to Distillation: Steady State Design and Operation PowerPoint PPT Presentation

Introduction to Distillation: Steady State Design and Operation - Title: PowerPoint Presentation Author: Ahmed Esmat Last modified by: Administrator Created Date: 2/3/2003 7:47:59 AM Document presentation format

Title: PowerPoint Presentation Author: Ahmed Esmat Last modified by: Administrator Created Date: 2/3/2003 7:47:59 AM Document presentation format

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More General Transfer Function Models PowerPoint PPT Presentation

More General Transfer Function Models - Pole at the origin (1/s term in TF model): results in an 'integrating process' ... One half of its value is added to the existing time delay (if any) and the other ...

Pole at the origin (1/s term in TF model): results in an 'integrating process' ... One half of its value is added to the existing time delay (if any) and the other ...

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Rigorous Simulation of Divided-wall Columns PowerPoint PPT Presentation

Rigorous Simulation of Divided-wall Columns - The 15th NPCW'09, Telemark University College, Porsgrunn, ... Monz main vendor for BASF. Krupp-Uhde. Sulzer. Rashig. Linde. Others. MW Kellogg (UK) UOP (USA) ...

The 15th NPCW'09, Telemark University College, Porsgrunn, ... Monz main vendor for BASF. Krupp-Uhde. Sulzer. Rashig. Linde. Others. MW Kellogg (UK) UOP (USA) ...

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Plantwide control: Towards a systematic procedure PowerPoint PPT Presentation

Plantwide control: Towards a systematic procedure - Based on: Plenary Presentation at ESCAPE'12, den Haag, May 2002. 2 ... ESCAPE'12 Symposium, Haag, Netherlands, May 2002. Larsson, T., 2000. ...

Based on: Plenary Presentation at ESCAPE'12, den Haag, May 2002. 2 ... ESCAPE'12 Symposium, Haag, Netherlands, May 2002. Larsson, T., 2000. ...

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PROCESS SYSTEMS ENGINEERING GROUP PowerPoint PPT Presentation

PROCESS SYSTEMS ENGINEERING GROUP - PROCESS SYSTEMS ENGINEERING GROUP Process modelling Including thermodynamic modelling Process optimization and control Process simulation and design

PROCESS SYSTEMS ENGINEERING GROUP Process modelling Including thermodynamic modelling Process optimization and control Process simulation and design

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Throughput maximization by improved bottleneck control PowerPoint PPT Presentation

Throughput maximization by improved bottleneck control - Department of Chemical Engineering, Norwegian University of ... Price, Lyman and Georgakis (1994). Throughput manipulation. in plantwide control structures. ...

Department of Chemical Engineering, Norwegian University of ... Price, Lyman and Georgakis (1994). Throughput manipulation. in plantwide control structures. ...

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Analysis of techniques for automatic detection and quantification of stiction in control loops PowerPoint PPT Presentation

Analysis of techniques for automatic detection and quantification of stiction in control loops - Title: Analysis of techniques for automatic detection and quantification of stiction in control loops Author: Student Last modified by: Student Created Date

Title: Analysis of techniques for automatic detection and quantification of stiction in control loops Author: Student Last modified by: Student Created Date

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Feedback Applications to self-optimizing control and stabilization of new operating regimes PowerPoint PPT Presentation

Feedback Applications to self-optimizing control and stabilization of new operating regimes - Mr = Mrmax. Active constraint. xB = xBmin. One unconstrained DOF left for ... Looking for 'magic' variables to keep at constant setpoints. How can we find them? ...

Mr = Mrmax. Active constraint. xB = xBmin. One unconstrained DOF left for ... Looking for 'magic' variables to keep at constant setpoints. How can we find them? ...

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Outline - Outline About Trondheim and myself Control structure design (plantwide control) A procedure for control structure design I Top Down Step 1: Degrees of freedom

Outline About Trondheim and myself Control structure design (plantwide control) A procedure for control structure design I Top Down Step 1: Degrees of freedom

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Controlled Variables Selection for a Biological Wastewater Treatment Process PowerPoint PPT Presentation

Controlled Variables Selection for a Biological Wastewater Treatment Process - Anoxic zone (Denitrification) followed by an aerobic zone (Nitrification) ... Step 1. Define Operational objectives (cost J) and constraints ...

Anoxic zone (Denitrification) followed by an aerobic zone (Nitrification) ... Step 1. Define Operational objectives (cost J) and constraints ...

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Controller Design Based on Transient Response Criteria PowerPoint PPT Presentation

Controller Design Based on Transient Response Criteria - ... on 1/4 decay ratio have been proposed: Cohen-Coon, Ziegler-Nichols ... Ziegler-Nichols Rules: These well-known tuning rules were published by Z-N in 1942: ...

... on 1/4 decay ratio have been proposed: Cohen-Coon, Ziegler-Nichols ... Ziegler-Nichols Rules: These well-known tuning rules were published by Z-N in 1942: ...

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Dividingwall column review and Design comparisons PowerPoint PPT Presentation

Dividingwall column review and Design comparisons - Chemical Engineering & Technology 30(9): 1284-1291. Agrawal, R. and Z. T. Fidkowski (1998) ... Industrial & Engineering Chemistry Research 37(8): 3444-3454. ...

Chemical Engineering & Technology 30(9): 1284-1291. Agrawal, R. and Z. T. Fidkowski (1998) ... Industrial & Engineering Chemistry Research 37(8): 3444-3454. ...

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Outline - Step 2: Operational objectives (optimal operation) Step 3: What ... Determine secondary controlled variables and structure ... Statics: Want large gain ...

Step 2: Operational objectives (optimal operation) Step 3: What ... Determine secondary controlled variables and structure ... Statics: Want large gain ...

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Feedback: The simple and best solution. Applications to self-optimizing control and stabilization of new operating regimes - No slug. Slugging. 66. Avoid slugging? Design changes ... Minimize effect of slugging: 3. Build large slug-catcher. Most common strategy in practice ...

No slug. Slugging. 66. Avoid slugging? Design changes ... Minimize effect of slugging: 3. Build large slug-catcher. Most common strategy in practice ...

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PSE and PROCESS CONTROL PowerPoint PPT Presentation

PSE and PROCESS CONTROL - ... PRACTISE Laboratory Simulation (Aspen, Hysys/Unisim..) SYSTEMS Modelling principles, Solution. State space models, linearization (ABCD), ...

... PRACTISE Laboratory Simulation (Aspen, Hysys/Unisim..) SYSTEMS Modelling principles, Solution. State space models, linearization (ABCD), ...

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Plantwide Control for Economically Optimal Operation of Chemical Plants - Applications to GTL plants and CO2 capturing processes PowerPoint PPT Presentation

Plantwide Control for Economically Optimal Operation of Chemical Plants - Applications to GTL plants and CO2 capturing processes - Plantwide Control for Economically Optimal Operation of Chemical Plants - Applications to GTL plants and CO2 capturing processes Mehdi Panahi PhD defense presentation

Plantwide Control for Economically Optimal Operation of Chemical Plants - Applications to GTL plants and CO2 capturing processes Mehdi Panahi PhD defense presentation

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ClosedLoop Frequency Response and Sensitivity Functions PowerPoint PPT Presentation

ClosedLoop Frequency Response and Sensitivity Functions - Ziegler-Nichols tuning (Table 12.6) Tyreus-Luyben tuning (Table 12.6) ... Ziegler-Nichols. MT. Kc. Controller. Controller Settings for Example 14.8. 13. Chapter 14 ...

Ziegler-Nichols tuning (Table 12.6) Tyreus-Luyben tuning (Table 12.6) ... Ziegler-Nichols. MT. Kc. Controller. Controller Settings for Example 14.8. 13. Chapter 14 ...

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PROCESS CONTROL GROUP PowerPoint PPT Presentation

PROCESS CONTROL GROUP - Plantwide control and optimization (including self-optimizing control) ... 7. H. Petter Lundstr m, Studies on robust multivariable control of distillation ...

Plantwide control and optimization (including self-optimizing control) ... 7. H. Petter Lundstr m, Studies on robust multivariable control of distillation ...

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HDA case study PowerPoint PPT Presentation

HDA case study - Benzene production from thermal-dealkalination of toluene ... Quench. Separator. Compressor. Cooler. Stabilizer. Benzene. Column. Toluene. Column. H2 CH4 ...

Benzene production from thermal-dealkalination of toluene ... Quench. Separator. Compressor. Cooler. Stabilizer. Benzene. Column. Toluene. Column. H2 CH4 ...

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Separation%20of%20Ternary%20Heteroazeotropic%20Mixtures%20in%20a%20Closed%20Multivessel%20Batch%20Distillation%20Column PowerPoint PPT Presentation

Separation%20of%20Ternary%20Heteroazeotropic%20Mixtures%20in%20a%20Closed%20Multivessel%20Batch%20Distillation%20Column - Separation of Ternary Heteroazeotropic Mixtures in a Closed Multivessel Batch ... One distillation boundary (unstable separatrix) Two distillation regions ...

Separation of Ternary Heteroazeotropic Mixtures in a Closed Multivessel Batch ... One distillation boundary (unstable separatrix) Two distillation regions ...

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Cr - ... Simulated Annealing) Algorithmes g n tiques (GAs: ... unit s et de r tro-installations Turbine gaz bas e sur les usines CHP dans des ...

... Simulated Annealing) Algorithmes g n tiques (GAs: ... unit s et de r tro-installations Turbine gaz bas e sur les usines CHP dans des ...

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Ph.D. Summer school Process and Tools Integration Operability and Control for Process Integration 17. August 2005 Sten Bay J PowerPoint PPT Presentation

Ph.D. Summer school Process and Tools Integration Operability and Control for Process Integration 17. August 2005 Sten Bay J - C A P E C Ph.D. Summer school Process and Tools Integration Operability and Control for Process Integration 17. August 2005 Sten Bay J rgensen CAPEC - Department of ...

C A P E C Ph.D. Summer school Process and Tools Integration Operability and Control for Process Integration 17. August 2005 Sten Bay J rgensen CAPEC - Department of ...

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Fig. 12.1. Unit-step disturbance responses for the candidate controllers (FOPTD Model: K = 1, PowerPoint PPT Presentation

Fig. 12.1. Unit-step disturbance responses for the candidate controllers (FOPTD Model: K = 1, - ... Simulation results for Example 12.1 (b): incorrect model gain. 16. Chapter ... For lag-dominant models, the standard IMC controllers for first-order and second ...

... Simulation results for Example 12.1 (b): incorrect model gain. 16. Chapter ... For lag-dominant models, the standard IMC controllers for first-order and second ...

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Program for North American Mobility in Higher Education PowerPoint PPT Presentation

Program for North American Mobility in Higher Education - Title: Slide 1 Last modified by: Agnes Devarieux Created Date: 1/17/2006 2:56:32 PM Document presentation format: On-screen Show Company: cole Polytechnique de Montreal

Title: Slide 1 Last modified by: Agnes Devarieux Created Date: 1/17/2006 2:56:32 PM Document presentation format: On-screen Show Company: cole Polytechnique de Montreal

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Control System Design Based on Frequency Response Analysis PowerPoint PPT Presentation

Control System Design Based on Frequency Response Analysis - Frequency response concepts and techniques play an important role in control ... A similar requirement occurs when a person bounces a ball. ...

Frequency response concepts and techniques play an important role in control ... A similar requirement occurs when a person bounces a ball. ...

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Control System Design Based on Frequency Response Analysis - Suppose that controller Gc is designed to cancel the unstable pole in Gp: ... function GOL(s) that is proper and has no unstable pole-zero cancellations. ...

Suppose that controller Gc is designed to cancel the unstable pole in Gp: ... function GOL(s) that is proper and has no unstable pole-zero cancellations. ...

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Fig' 12'1' Unitstep disturbance responses for the candidate controllers FOPTD Model: K 1, - ... design because the closed-loop transfer function Y/Ysp is not known a priori. ... A practical design equation can be derived by replacing the unknown G by , and Y ...

... design because the closed-loop transfer function Y/Ysp is not known a priori. ... A practical design equation can be derived by replacing the unknown G by , and Y ...

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ESCAPE 18 - New configuration for heteroazeotropic batch distillation: I. Feasibility studies Peter Lang1, Ferenc Denes1, Xavier Joulia2 1BUTE Dept. of Building Services ...

New configuration for heteroazeotropic batch distillation: I. Feasibility studies Peter Lang1, Ferenc Denes1, Xavier Joulia2 1BUTE Dept. of Building Services ...

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Cr - Program for North American Mobility in Higher Education (NAMP) Introducing Process Integration for Environmental Control in Engineering Curricula (PIECE)

Program for North American Mobility in Higher Education (NAMP) Introducing Process Integration for Environmental Control in Engineering Curricula (PIECE)

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Program for North American Mobility in Higher Education - Program for North American Mobility in Higher Education Module 8 Introduction to Process Integration Tier I PIECE Introducing Process integration for Environmental ...

Program for North American Mobility in Higher Education Module 8 Introduction to Process Integration Tier I PIECE Introducing Process integration for Environmental ...

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Skogestad PowerPoint PPT Presentations