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 in | Nuclear engineering and design Vol. 237; no. 15; pp. 1848 - 1861 |
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Main Authors | , , , , , , , |
Format | Journal Article Conference Proceeding |
Language | English |
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Elsevier B.V
01.09.2007
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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. |
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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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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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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 |
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