Effect of cross-section geometry on the thermohydraulic - - PowerPoint PPT Presentation

effect of cross section geometry on the thermohydraulic
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Effect of cross-section geometry on the thermohydraulic - - PowerPoint PPT Presentation

2 nd International Conference on Sustainable Energy and Resource Use in Food Chains Effect of cross-section geometry on the thermohydraulic characteristics of supercritical CO 2 in minichannels Lei Chai*, Savvas A Tassou Institute of Energy


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2nd International Conference on Sustainable Energy and Resource Use in Food Chains

RCUK Centre for Sustainable Energy Use in Food Chains

Effect of cross-section geometry on the thermohydraulic characteristics of supercritical CO2 in minichannels

Lei Chai*, Savvas A Tassou

Institute of Energy Futures, Brunel University London

Paphos, Cyprus 17-19 October 2018

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Lei Chai

Outline

  • Introduction

– Why sCO2? Why minichannels?

  • Computational method

– Element, model, boundary condition.

  • Data acquisition

– Local and average parameters.

  • Results and discussion

– Thermohydraulic performance, comparison with correlations.

  • Future work
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Why sCO2?

  • Environment-friendly, nontoxic, non-

flammable

  • a zero net impact on climate change
  • reduced emission of greenhouse gas
  • high power density for power

generation

  • transcritical refrigeration cycle
  • supercritical Brayton cycle
  • natural circulation loops
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Why minichannels?

  • highly compact construction
  • high heat transfer coefficient
  • high pressure capability
  • lower fluid inventory

Cross-section geometry exerts an influence on fluid flow and heat transfer

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Computational element and model

  • standard k-ε model
  • NIST real gas

thermophysical properties

  • buoyant effect
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Lei Chai Why NIST real gas model?

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Boundary and operating conditions

  • Constant heat flux for channel wall, velocity-inlet for channel

inlet, pressure-outlet for channel outlet

  • Corresponding mass flux for the four cases are 545.6, 1629.5, 473.9 and 561.3 kg/(m2·s)
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Data acquisition

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Local fluid temperature

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Local heat transfer coefficient

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Local Nusselt number

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Local pressure drop

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Local friction factor

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Average thermohydraulic performance

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Lei Chai Comparison with heat transfer correlations

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Comparison with heat transfer correlations

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Comparison with fluid friction correlations

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Lei Chai Future work – modeling for heater, recuperator, cooler

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Lei Chai Future work - numerical study for different flow passages

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Lei Chai Future work – sCO2 heat exchanger test facility

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Acknowledgements

  • Engineering and Physical Sciences Research Council (EPSRC) of the UK

under research grants EP/P004636/1 and EP/K011820/1

  • European Union’s Horizon 2020 research and innovation programme

under grant agreement No. 680599.

  • The authors would like to acknowledge the financial support received by

the project funders and the industry partners.

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Thank you !

Lei Chai Savvas A Tassou lei.chai@brunel.ac.uk savvas.tassou@brunel.ac.uk