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Using traditional techniques to develop a
complex and maintainable PAT system.
 Paul Brodbeck – Process Control Engineer
 30 Years experience.
 BS in Chemical Engineering from Case Western Reserve University
 Process Modeling/Optimization
 APL Matrix Language - MATLAB.
 Statistical based analysis at Chemical Plant: FOCUS, SAS and SPC.
 Statistical Process Control
 Machine Learning Course with Stephen Ng from Stanford
 Eigenvector Software
 Recent PAT Application with Chromatography Endpoint Detection
 Similarities
 Basic Process Control applied to PAT
 Case studies
 Enterprise PAT Architecture
 Manageable and maintainable system.
 Top Down Approach
 System Complex
 Black Box
 Build from Ground Up
 Simple Blocks to Start
 Build complexity
 Learn
1. Data Management
 Collection
 Storage
 Analytical Tools/Visualization
2. Process Model Building
 MATLAB, PCA, PLS, MPC, NN, Optimization
3. Process Control
 Implementation of Real-Time Prediction Models
 Closed-Loop Control of CPPs, CQAs
Basic PID Block Temperature Controller
 Basic Single Loop – PID Block
 Reactor Temperature Ctrl
 Closed-Loop Feedback
 Uni-Variate Process Inputs
 Temperature, Pressure,
Flow, pH, Level, …
LOOP TUNING CONSTANTS
 Work Against the Error
◦ Error = Setpoint - Value
 Proportional
◦ Linear Error
 Integral
◦ Time
 Derivative
◦ Rate of Change
 Cruise Control in Car
Building Blocks Approach Refinery Controls
 Analyzers
 Bruker, Thermo, RAMAN
 MVA Packages
 CAMO, Umetrics, Eigenvector, Infometrix
 MATLAB, Mathemtica
 Process Control Systems
 PC Based – Sartorius, ABEC, GE
 PLC – ABB, Rockwell
 DCS – Siemens, Emerson, Honeywell
 Analysis of Critical Quality Attributes (CQA)
◦ Mass Spectrometry, Infrared Spectroscopy,
◦ Raman, FBRM, NMR, UV Spectroscopy.
 Spectral Analysis MVA
◦ Chemometrics – Principal Component Analysis (PCA) &
Partial Least Squares (PLS)
◦ CAMO, UMetrics, EigenVector
 Modeling/Optimization MVA
◦ Linear Regression, Logistic Regression, Support Vector
Machines, Neural Networks, Clustering, Linear
Programming, PCA, PLS. MATLAB, Mathematica.
 Control of Critical Process Parameters (CPP)
◦ PC Based, PLC, DCS
 Analyzer Interfaces
 Spectral Analysis
 Modeling Capability
 Optimization
 Process Control System Interface
 Methods
 CFR Part 11 Compliant
 Siemens SIMATIC
 Optimal SynTQ
 ABB XPAT
 GE Fanuc Proficy RX
 Basic Process Control Loops
 Complex Control Strategies
 PAT Online Analyzers CQAs
 Closed Loop Control CPPs
 Enterprise PAT
 Collect Data
◦ Data Analytics
◦ Batch Analytics
◦ Multi Variable SPC
 Modeling/Optimization

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PAT Process Control IFPAC 2013

  • 1. Using traditional techniques to develop a complex and maintainable PAT system.
  • 2.  Paul Brodbeck – Process Control Engineer  30 Years experience.  BS in Chemical Engineering from Case Western Reserve University  Process Modeling/Optimization  APL Matrix Language - MATLAB.  Statistical based analysis at Chemical Plant: FOCUS, SAS and SPC.  Statistical Process Control  Machine Learning Course with Stephen Ng from Stanford  Eigenvector Software  Recent PAT Application with Chromatography Endpoint Detection
  • 3.  Similarities  Basic Process Control applied to PAT  Case studies  Enterprise PAT Architecture  Manageable and maintainable system.
  • 4.
  • 5.  Top Down Approach  System Complex  Black Box  Build from Ground Up  Simple Blocks to Start  Build complexity  Learn
  • 6. 1. Data Management  Collection  Storage  Analytical Tools/Visualization 2. Process Model Building  MATLAB, PCA, PLS, MPC, NN, Optimization 3. Process Control  Implementation of Real-Time Prediction Models  Closed-Loop Control of CPPs, CQAs
  • 7. Basic PID Block Temperature Controller  Basic Single Loop – PID Block  Reactor Temperature Ctrl  Closed-Loop Feedback  Uni-Variate Process Inputs  Temperature, Pressure, Flow, pH, Level, …
  • 8. LOOP TUNING CONSTANTS  Work Against the Error ◦ Error = Setpoint - Value  Proportional ◦ Linear Error  Integral ◦ Time  Derivative ◦ Rate of Change  Cruise Control in Car
  • 9.
  • 10. Building Blocks Approach Refinery Controls
  • 11.
  • 12.  Analyzers  Bruker, Thermo, RAMAN  MVA Packages  CAMO, Umetrics, Eigenvector, Infometrix  MATLAB, Mathemtica  Process Control Systems  PC Based – Sartorius, ABEC, GE  PLC – ABB, Rockwell  DCS – Siemens, Emerson, Honeywell
  • 13.  Analysis of Critical Quality Attributes (CQA) ◦ Mass Spectrometry, Infrared Spectroscopy, ◦ Raman, FBRM, NMR, UV Spectroscopy.  Spectral Analysis MVA ◦ Chemometrics – Principal Component Analysis (PCA) & Partial Least Squares (PLS) ◦ CAMO, UMetrics, EigenVector  Modeling/Optimization MVA ◦ Linear Regression, Logistic Regression, Support Vector Machines, Neural Networks, Clustering, Linear Programming, PCA, PLS. MATLAB, Mathematica.  Control of Critical Process Parameters (CPP) ◦ PC Based, PLC, DCS
  • 14.
  • 15.
  • 16.
  • 17.  Analyzer Interfaces  Spectral Analysis  Modeling Capability  Optimization  Process Control System Interface  Methods  CFR Part 11 Compliant
  • 18.  Siemens SIMATIC  Optimal SynTQ  ABB XPAT  GE Fanuc Proficy RX
  • 19.  Basic Process Control Loops  Complex Control Strategies  PAT Online Analyzers CQAs  Closed Loop Control CPPs  Enterprise PAT  Collect Data ◦ Data Analytics ◦ Batch Analytics ◦ Multi Variable SPC  Modeling/Optimization

Editor's Notes

  1. Why is this complicated?
  2. Function Block Slide, Thermometer, Temperature temp up steam down
  3. Goes away
  4. Actual Vendors, segue without blip
  5. synTQ, SIPAT, delete blue line