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On-line Performance Monitoring of a Chemical Process

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Title: On-line Performance Monitoring of a Chemical Process


1
On-line Performance Monitoring of a Chemical
Process
BP Chemicals/CPACT/MDC
2
Summary
  • Will talk about application of multivariate SPC.
  • A data visualisation system for overview of plant
    operation.
  • Tried on Hull site plant.
  • Will aid operators control of plant.

3
Introduction
  • Plants have data overload.
  • MSPC gives overview of plant operation on just a
    few graphs.
  • PCA is used to compress correlated plant
    variables to just a few PCs.
  • Technique was applied to the BP Hull A4 CO plant.
  • Plant manufactures CO by steam reforming of nat.
    gas. CO is feedstock for acetic acid production.

4
Plant Schematic
MEA
Steam
Reformer Heat
CO2 Removal
Natural Gas (desulphurised)
H2 (NH3 plant)
Water Removal
Cold Box Separation
CO (acetic acid plant)
5
MSPC
  • Data point on PC scores plots represent plant
    status at that time.
  • Data points due to plant problem appear outside a
    confidence ellipse.
  • Problem points also show up using statistical
    measures (e.g. SPE and T2 statistic) - distances
    from model.
  • Problem points interrogated using contribution
    plots for causal variables.

6
First Model
  • An MSPC model was built of normal operation for
    the A4 CO plant.
  • The model used 27 main plant variables, including
    temperatures, pressures, flows and analyser
    results.
  • Model training data was collected at 4 minute
    snapshots over a 1 week period of stable
    operation.
  • 6 PCs explains 70 of variance.
  • This is effectively then used as a basis to
    compare future operation.

7
Off-line Analysis
  • Using CPACT MultiDAT and PreScreen2 Software

Off-line Analysis of Operator Error
8
On-line with MDC
  • PC scores plots, statistics vs time, etc
  • Zoom in
  • Click on point to select contribution plot
  • Plus off-line tools for model building
  • Plus PLS and adaptive models

On-line Model, Feedstock Upset (N2)
9
On-line with MDC
  • Normalised
  • Greatest first
  • Scrollable
  • Click for time trend

Process Variable Contribution Plots
Time Trend of a Process Variable
10
Problems
  • But plant operates at different rates.
  • What data to use for model?
  • What variables to use?
  • Dynamic data influenced by the past.
  • Serially correlated (invalid control limits).
  • Result hard to find balance between alerts and
    false alarms.
  • So concentrated on smaller section of plant
    tried new techniques.

11
Plant Section - MEA
  • Model for MEA (10 tags)
  • Has oscillation upset at high rates

The Oscillation
Upset in Column Level
  • Clusters 1, 2 and 3 represent different modes
    of operation

3
2
1
Score Statistics Plots
12
Live Demo
  • Live demo of MDC MSPC with the previous data for
    MEA.

13
Multi Rate Model
  • Work by Ewan Mercer et al (CPACT Newcastle
    University).
  • Model for MEA.
  • Need models for different plant rates.
  • Modes of operation seen as clusters.
  • But better to collapse clusters together

PC1 vs PC2 Scores Plot
14
New Technique
  • Also by Ewan Mercer et al.
  • Based on plant model mismatch (PMM).
  • Build state space model for MEA (1m data, I/Ps
    and O/Ps).
  • Build PCA model on differences between predicted
    and actual plant data (residuals).
  • Will effectively collapse clusters.
  • Use standard MSPC graphs to monitor plant.

15
Plant/Model Mismatch
Schematic of Technique
16
PCA on Residuals
  • Model for multiple plant rates.
  • Near normal distribution with low serial
    correlation.
  • Picks up upset with fewer false alarms.

17
Parallel Coords
  • Another potential technique
  • Light cluster is normal MEA operation
  • Other darker data is upset
  • Can also use to visualise many PCs
  • Each y-axis is a plant variable
  • Each path is state of plant at one point in time

18
Conclusion/Next Steps
  • Model built for overview of the A4 CO plant.
  • Tested on-line using MDCs MSPC software.
  • Overview of plant operation with drill down.
  • Picks up process problems and helps diagnose
    cause.
  • Will improve running of plants.
  • Gain site acceptance for deployment.
  • Initially to see plant changes.
  • Use alerting later with the new techniques (i.e.
    PMM).

19
Acknowledgements
  • BP Hull Site
  • Steve Batty, Zaid Rawi et al.
  • CPACT/Newcastle University
  • Ewan Mercer, Julian Morris, Elaine Martin et al.
  • MDC
  • Chris Hawkins, Paul Booth et al.
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