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Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology Gliwice, Poland Identification of Boundary Velocity Basing on Internal Temperature Measurements – sensitivity analysis IPES 2003

Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

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Identification of Boundary Velocity Basing on Internal Temperature Measurements – sensitivity analysis. Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology Gliwice, Poland. IPES 2003. Outline. Introduction Direct problem formulation - PowerPoint PPT Presentation

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Page 1: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Ireneusz SzczygiełInstitute of Thermal Technology

Silesian University of TechnologyGliwice, Poland

Identification of Boundary Velocity Basing on Internal Temperature

Measurements – sensitivity analysis

IPES 2003

Page 2: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Outline

Introduction Direct problem formulation Inverse problem formulation Discussion on sensitivity coefficient field Results of numerical tests Final remarks

IPES 2003

Page 3: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Basic assumptions

•2D, Cartesian geometry 2D, Cartesian geometry •Steady stateSteady state•Potential or laminar flowPotential or laminar flow•Isoparametric fluidIsoparametric fluid

IPES 2003

Page 4: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

IPES 2003

Direct problem formulation

temperature field descriptiontemperature field description

Page 5: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Direct problem formulation

xux

y

u y

velocity field description – potential flowvelocity field description – potential flow

IPES 2003

Page 6: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Direct problem formulation

velocity field description – incompressible flowvelocity field description – incompressible flow

IPES 2003

Page 7: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Boundary conditions inflow profileinflow profile

0

n

ui

iTT

symmetry wallssymmetry walls 0nT

0n

heating pipes surfaceheating pipes surface pTT

0n

outlet profileoutlet profile 0nT

const

flow direction symmetry walls

heating pipes

inflow surface outflow surface

0; yix uuu

0;0 yxx unuuu

0;0 yx uu

0;0 yx uu

IPES 2003

Page 8: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Inverse problem formulation

definition of sensitivity coefficients:definition of sensitivity coefficients:

iT u

TZ

Estimate inflow velocity knowing the value of internal temperature

IPES 2003

Page 9: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Evaluation of sensitivity coefficients

Tuy

cTux

cqyTk

yxTk

x yxv

iu

TyTxATT Zu

ycZu

xcS

yZ

kyx

Zk

x

IPES 2003

Page 10: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Evaluation of sensitivity coefficient

boundary conditionsboundary conditions

iu

iTT

0nT

pTT

inflow profileinflow profile

symmetry wallssymmetry walls

heating pipes surfaceheating pipes surface

0TZ

0nZT

0TZ

IPES 2003

Page 11: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Evaluation of sensitivity coefficient

source term Ssource term SAA

yT

uu

xT

uu

kcS

i

y

i

xA

soso

yTZ

xTZ

kcS uyuxA

IPES 2003

Page 12: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Evaluation of sensitivity coefficients – potential flow

02 iu

02 Z

boundary conditionsboundary conditions

0

n

ui

0n iu

01

nZ

0

nZ

xZ

Zux

iuZ

yZ

Zuy

IPES 2003

Page 13: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Evaluation of sensitivity coefficients – NS flow

IPES 2003

Page 14: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

source term Ssource term Suxux

yuZ

xuZS x

uyx

uxux

Evaluation of sensitivity coefficients – NS flow

yu

Zxu

ZS yuy

yuxuy

source term Ssource term Suyuy

IPES 2003

Page 15: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Evaluation of sensitivity coefficients – NS flowboundary conditionsboundary conditions

inflow profileinflow profile

symmetry wallssymmetry walls

heating pipes surfaceheating pipes surface

outlet profileoutlet profile

0; yix uuu

0;0 yxx unuuu

0;0 yx uu

0;0 yx uu

0;1 uyux ZZ

0;0 uyuxux ZnZZu

0;0 uyux ZZ

0;0 uyux ZZ

IPES 2003

Page 16: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Examplary iterative inverse procedure –potential flow

• calculations of the Zcalculations of the Z fieldfield•assumption of the inflow velocity valueassumption of the inflow velocity value•evaluation of the potential and the velocity fieldevaluation of the potential and the velocity field•evaluation of the temperature sensitivity coefficient evaluation of the temperature sensitivity coefficient distributiondistribution•calculation of the new boundary velocitycalculation of the new boundary velocity

•convergence test for the inflow velocityconvergence test for the inflow velocity

Tii ZTYuu /** where Y stands for the measurementswhere Y stands for the measurements resultsresults

IPES 2003

Page 17: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Examplary iterative inverse procedure –NS flow

•assumption of the inflow velocity valueassumption of the inflow velocity value•evaluation of the velocity fieldevaluation of the velocity field•evaluation of the evaluation of the velocityvelocity sensitivity coefficient sensitivity coefficient distributiondistribution Z Zuxux

•evaluation of the evaluation of the velocityvelocity sensitivity coefficient sensitivity coefficient distributiondistribution Z Zuyuy

•evaluation of the temperature sensitivity coefficient evaluation of the temperature sensitivity coefficient distributiondistribution•calculation of the new boundary velocitycalculation of the new boundary velocity•convergence test for the inflow velocityconvergence test for the inflow velocity

Tii ZTYuu /** where Y stands for the measurementswhere Y stands for the measurements resultsresults

IPES 2003

Page 18: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Examplary iterative inverse procedure –NS flow

•assumption of the inflow velocity valueassumption of the inflow velocity value•evaluation of the velocity fieldevaluation of the velocity field•evaluation of the evaluation of the velocityvelocity sensitivity coefficient sensitivity coefficient distributiondistribution Z Zuxux

•evaluation of the evaluation of the velocityvelocity sensitivity coefficient sensitivity coefficient distributiondistribution Z Zuyuy

•evaluation of the temperature sensitivity coefficient evaluation of the temperature sensitivity coefficient distributiondistribution•calculation of the new boundary velocitycalculation of the new boundary velocity•convergence test for the inflow velocityconvergence test for the inflow velocity

Tii ZTYuu /** where Y stands for the measurementswhere Y stands for the measurements resultsresults

IPES 2003

Page 19: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Simple channel, Re=500Simple channel, Re=500

ZZux ux distribution distribution

ZZuuyy distribution distribution

Velocity distribution Velocity distribution

IPES 2003

Page 20: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Potential flowPotential flow, Re=20, Re=20

Temperature

IPES 2003

Page 21: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Potential flowPotential flow, Re=20, Re=20

Temperature sensitivity coefficients

IPES 2003

Page 22: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests NSNS flow flow, Re=200, Re=200

Temperature

IPES 2003

Page 23: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests NSNS flow flow, Re=200, Re=200

Velocity magnitude

IPES 2003

Page 24: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests NSNS flow flow, Re=200, Re=200

Sensitivity coefficients Zux

IPES 2003

Page 25: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests NSNS flow flow, Re=200, Re=200

Sensitivity coefficients Zuy

IPES 2003

Page 26: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests NSNS flow flow, Re=200, Re=200

Sensitivity coefficients ZT

IPES 2003

Page 27: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of nodal quantity, NS flow, Re=200Estimation of nodal quantity, NS flow, Re=200

Temperature

IPES 2003

Page 28: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of nodal quantity, NS flow, Re=200Estimation of nodal quantity, NS flow, Re=200

Velocity

IPES 2003

Page 29: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of nodal quantity, NS flow, Re=200Estimation of nodal quantity, NS flow, Re=200

Sensitivity coefficient Zux

IPES 2003

Page 30: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of nodal quantity, NS flow, Re=200Estimation of nodal quantity, NS flow, Re=200

Sensitivity coefficient Zux

IPES 2003

Page 31: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of nodal quantity, NS flow, Re=200Estimation of nodal quantity, NS flow, Re=200

Sensitivity coefficient Zux

IPES 2003

Page 32: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of nodal quantity, NS flow, Re=200Estimation of nodal quantity, NS flow, Re=200

Sensitivity coefficient Zux

IPES 2003

Page 33: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of nodal quantity, NS flow, Re=200Estimation of nodal quantity, NS flow, Re=200

Sensitivity coefficient ZT

IPES 2003

Page 34: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of nodal quantity, NS flow, Re=200Estimation of nodal quantity, NS flow, Re=200

Sensitivity coefficient ZT

IPES 2003

Page 35: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of nodal quantity, NS flow, Re=200Estimation of nodal quantity, NS flow, Re=200

Sensitivity coefficient ZT

IPES 2003

Page 36: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of nodal quantity, NS flow, Re=200Estimation of nodal quantity, NS flow, Re=200

Sensitivity coefficient ZT

IPES 2003

Page 37: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of mass velocity, NS flow, Re=50Estimation of mass velocity, NS flow, Re=50

Velocity

IPES 2003

Page 38: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of mass velocity, NS flow, Re=50Estimation of mass velocity, NS flow, Re=50

Sensitivity coefficient Zux

IPES 2003

Page 39: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

Results of numerical tests Estimation of mass velocity, NS flow, Re=50Estimation of mass velocity, NS flow, Re=50

Sensitivity coefficient ZT

IPES 2003

Page 40: Ireneusz Szczygieł Institute of Thermal Technology Silesian University of Technology

• the shape of the sensitivity coefficient distribution is a the shape of the sensitivity coefficient distribution is a function of inlet velocity value. It means, the that the function of inlet velocity value. It means, the that the optimal location for the measurement sensors varies with optimal location for the measurement sensors varies with the inlet velocity value;the inlet velocity value;•the region of maximum values of the sensitivity coefficient the region of maximum values of the sensitivity coefficient is shifted from the inlet surface toward the flow direction: is shifted from the inlet surface toward the flow direction: bringing the measurement sensors close to the inflow bringing the measurement sensors close to the inflow boundary can result in worse estimation of the inflow boundary can result in worse estimation of the inflow velocity;velocity;• the application of the inverse algorithm is possible on in the application of the inverse algorithm is possible on in the regions with nonuniform temperature distribution;the regions with nonuniform temperature distribution;•inverse procedure for the NS flow is much more time inverse procedure for the NS flow is much more time consuming than the procedure for the potential flowconsuming than the procedure for the potential flow;;

Final remarks