Evolution of the structure of a gas–liquid two-phase flow in a large vertical pipe

The evolution of the structure of a gas–liquid flow in a large vertical pipe of 195 mm inner diameter was investigated at the TOPFLOW test facility in Rossendorf. Wire-mesh sensors were used to measure sequences of two-dimensional distributions of local instantaneous gas fraction within the complete...

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Published inNuclear engineering and design Vol. 237; no. 15; pp. 1848 - 1861
Main Authors Prasser, Horst-Michael, Beyer, Matthias, Carl, Helmar, Gregor, Sabine, Lucas, Dirk, Pietruske, Heiko, Schütz, Peter, Weiss, Frank-Peter
Format Journal Article Conference Proceeding
LanguageEnglish
Published Amsterdam Elsevier B.V 01.09.2007
Elsevier
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Abstract The evolution of the structure of a gas–liquid flow in a large vertical pipe of 195 mm inner diameter was investigated at the TOPFLOW test facility in Rossendorf. Wire-mesh sensors were used to measure sequences of two-dimensional distributions of local instantaneous gas fraction within the complete pipe cross-section. The sensors own a resolution of 3 mm at a frequency of 2500 Hz. Superficial velocities were varied in a range covering flow regimes from bubbly to churn-turbulent flow. The distance between the gas injection and the sensor position was changed using a so-called variable gas injection system. It consists of six gas injection units, each equipped with three rings of injection orifices in the pipe wall (orifice diameter: 1 and 4 mm), which are fed from ring chambers. The gas flow towards these distributor chambers is individually controlled by valves. Measured bubble-size resolved radial gas fraction profiles reveal differences in the lateral migration of bubbles of different size starting from the injection at the wall. The evolution of bubble-size distributions allows to study bubble coalescence and break-up. The influence of the physical properties of the fluid was studied by comparing cold air–water experiments with steam–water tests at 65 bar.
AbstractList The evolution of the structure of a gas–liquid flow in a large vertical pipe of 195 mm inner diameter was investigated at the TOPFLOW test facility in Rossendorf. Wire-mesh sensors were used to measure sequences of two-dimensional distributions of local instantaneous gas fraction within the complete pipe cross-section. The sensors own a resolution of 3 mm at a frequency of 2500 Hz. Superficial velocities were varied in a range covering flow regimes from bubbly to churn-turbulent flow. The distance between the gas injection and the sensor position was changed using a so-called variable gas injection system. It consists of six gas injection units, each equipped with three rings of injection orifices in the pipe wall (orifice diameter: 1 and 4 mm), which are fed from ring chambers. The gas flow towards these distributor chambers is individually controlled by valves. Measured bubble-size resolved radial gas fraction profiles reveal differences in the lateral migration of bubbles of different size starting from the injection at the wall. The evolution of bubble-size distributions allows to study bubble coalescence and break-up. The influence of the physical properties of the fluid was studied by comparing cold air–water experiments with steam–water tests at 65 bar.
The evolution of the structure of a gas-liquid flow in a large vertical pipe of 195mm inner diameter was investigated at the TOPFLOW test facility in Rossendorf. Wire-mesh sensors were used to measure sequences of two-dimensional distributions of local instantaneous gas fraction within the complete pipe cross-section. The sensors own a resolution of 3mm at a frequency of 2500Hz. Superficial velocities were varied in a range covering flow regimes from bubbly to churn-turbulent flow. The distance between the gas injection and the sensor position was changed using a so-called variable gas injection system. It consists of six gas injection units, each equipped with three rings of injection orifices in the pipe wall (orifice diameter: 1 and 4mm), which are fed from ring chambers. The gas flow towards these distributor chambers is individually controlled by valves. Measured bubble-size resolved radial gas fraction profiles reveal differences in the lateral migration of bubbles of different size starting from the injection at the wall. The evolution of bubble-size distributions allows to study bubble coalescence and break-up. The influence of the physical properties of the fluid was studied by comparing cold air-water experiments with steam-water tests at 65bar. D diameter (m) Dbub equivalent bubble diameter (mm) Dbub,xy bubble diameter in the horizontal (xy) plane (mm) i, j, k numeric indexes J superficial velocity (m/s) L length (m) p pressure (MPa) T temperature ( deg C) v velocity (m/s) V volume (m3) x, y, z co-ordinates , eps volumetric gas fraction (%) air index for air cr criterion, critical DN abbreviation for nominal diameter G gas inj injection L liquid PDF probability density function S saturation steam index for steam water index for water.
Author Weiss, Frank-Peter
Prasser, Horst-Michael
Carl, Helmar
Beyer, Matthias
Gregor, Sabine
Schütz, Peter
Lucas, Dirk
Pietruske, Heiko
Author_xml – sequence: 1
  givenname: Horst-Michael
  surname: Prasser
  fullname: Prasser, Horst-Michael
  email: hprasser@ethz.ch
  organization: Forschungszentrum Rossendorf e.V., Institute of Safety Research, P.O. Box 510119 Dresden, Germany
– sequence: 2
  givenname: Matthias
  surname: Beyer
  fullname: Beyer, Matthias
  organization: Forschungszentrum Rossendorf e.V., Institute of Safety Research, P.O. Box 510119 Dresden, Germany
– sequence: 3
  givenname: Helmar
  surname: Carl
  fullname: Carl, Helmar
  organization: Forschungszentrum Rossendorf e.V., Institute of Safety Research, P.O. Box 510119 Dresden, Germany
– sequence: 4
  givenname: Sabine
  surname: Gregor
  fullname: Gregor, Sabine
  organization: Forschungszentrum Rossendorf e.V., Institute of Safety Research, P.O. Box 510119 Dresden, Germany
– sequence: 5
  givenname: Dirk
  surname: Lucas
  fullname: Lucas, Dirk
  organization: Forschungszentrum Rossendorf e.V., Institute of Safety Research, P.O. Box 510119 Dresden, Germany
– sequence: 6
  givenname: Heiko
  surname: Pietruske
  fullname: Pietruske, Heiko
  organization: Forschungszentrum Rossendorf e.V., Institute of Safety Research, P.O. Box 510119 Dresden, Germany
– sequence: 7
  givenname: Peter
  surname: Schütz
  fullname: Schütz, Peter
  organization: Forschungszentrum Rossendorf e.V., Institute of Safety Research, P.O. Box 510119 Dresden, Germany
– sequence: 8
  givenname: Frank-Peter
  surname: Weiss
  fullname: Weiss, Frank-Peter
  organization: Forschungszentrum Rossendorf e.V., Institute of Safety Research, P.O. Box 510119 Dresden, Germany
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Issue 15
Keywords Two phase flow
Turbulent flow
Vertical pipe
Gas injection
Cross section (collision)
Water vapor
Physical properties
Nuclear reactor
Flow regime
Test facility
Starting
Gas liquid flow
Valve
Coalescence
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Snippet The evolution of the structure of a gas–liquid flow in a large vertical pipe of 195 mm inner diameter was investigated at the TOPFLOW test facility in...
The evolution of the structure of a gas-liquid flow in a large vertical pipe of 195mm inner diameter was investigated at the TOPFLOW test facility in...
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SubjectTerms Applied sciences
Controled nuclear fusion plants
Energy
Energy. Thermal use of fuels
Exact sciences and technology
Fission nuclear power plants
Fuels
Installations for energy generation and conversion: thermal and electrical energy
Nuclear fuels
Title Evolution of the structure of a gas–liquid two-phase flow in a large vertical pipe
URI https://dx.doi.org/10.1016/j.nucengdes.2007.02.018
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Volume 237
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