Handling Uncertainty in the Development and Design of Chemical Processes PowerPoint PPT Presentation

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Title: Handling Uncertainty in the Development and Design of Chemical Processes


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Handling Uncertainty in the Development and
Design of Chemical Processes
  • David Bogle,
  • David Johnson and
  • Sujan Balendra
  • Centre for Process Systems Engineering
  • Dept of Chemical Engineering
  • University College London
  • Collaborating Company Pharmacia

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Summary
  • Objectives
  • Process Development
  • Methodology
  • A Multiphase reactor
  • Complete Manufacturing Processes
  • Conclusions

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Dealing with Uncertainty in Process Development
  • Utilise the available information
  • What can be done?
  • manipulate available decisions
  • improve the model - reduce uncertainty
  • alternative process/route

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Methodology
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Methodology
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Uncertainty Analysis
  • Estimate characteristics based on local
    linearisation and approx. confidence region
  • Hammersley sampling procedure
  • Solve stochastic model to give expected values
    of statistics for output variables
  • Continue sampling until mean and variance are
    unchanging (lt1)

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Validation and Sensitivity Analysis
  • Estimate ranking priority of inputs contributing
    to uncertainty
  • Use
  • Correlation coefficients linear measures of
    input contribution
  • Standardised regression coefficient fraction
    of output variability explained by input
    variability not due to any of the other inputs

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Optimal reduction in uncertainty
d decision variables fractions of original
values of parameters which characterise spread of
uncertainties Max S dst S ddt Subject
to deterministic model uncertainty space
characterisation stochastic inequality
constraint FW(F) lt a FW (F) (width between 5
and 95 fractiles)
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Optimal isothermal conditions
Criteria Nominal optimal operation Uncertain optimal operation
Scenarios 456 418
Mean-variance YC 0 0.234
EYC (), VarYC 94.35, 50.4 94.30, 26.9
EYD () 2.75 2.77
Etf (hr) 9.34 2.35
FWYC () 18.73 15.92
FWYD () 8.83 7.55
FWtf (hr) 24.97 5.17
PrpassYD ? 2.0, Prpasstf ? 8.0 0.59, 0.59 0.53, 0.98
EviolYD ? 2.0, Evioltf ? 8.0 1.39, 4.49 1.25, 0.05
Decisions
tadd (hr) 1.79 1.12
Tiso (K) 296.8 312.4
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Process development methodology
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Typical Pharmaceutical Plant
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Process design systems are typically modular and
data comes as error bounds around a data point
use interval methods
But how conservative?
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Conclusions
  • Process development
  • Methodology for quantifying and minimising
    uncertainty
  • Uncertainty analysis and identification of
    potential uncertainty reduction
  • Case study of semi batch reactor
  • Contrast of stochastic and interval approaches

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Acknowledgements
EPSRC, Pharmacia, Aspentech
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