The flow unsteadiness generated in a swirl apparatus is investigated experimentally and numerically. The swirl apparatus has two parts: a swirl generator and a test section. The swirl generator which includes two blade rows, one stationary and one rotating, is designed such that the emanating flow at free runner rotational speed resembles that of a Francis hydroturbine operated at partial discharge. The test section consists of a conical diffuser similar to the draft tube cone of a Francis turbine. Several swirling flow regimes are produced, and the laser Doppler anemometry (LDA) measurements are performed along three survey axes in the test section for different runner rotational speeds (400–920 rpm), with a constant flow rate, 30 l/s. The measured mean velocity components and its fluctuating parts are used to validate the results of unsteady numerical simulations, conducted using the foam-extend-3.0 CFD code. Furthermore, phase-averaged pressure measured at two positions in the draft tube is compared with those of numerical simulations. A dynamic mesh is used together with the sliding general grid interfaces (GGIs) to mimic the effect of the rotating runner. The delayed detached-eddy simulation method, conjugated with the Spalart–Allmaras turbulence model (DDES–SA), is applied to achieve a deep insight about the ability of this advanced modeling technique and the physics of the flow. The RNG model is also used to represent state-of-the-art of industrial turbulence modeling. Both models predict the mean velocity reasonably well while DDES–SA presents more realistic flow features at the highest and lowest rotational speeds. The highest level of turbulence occurs at the highest and lowest rotational speeds which DDES–SA is able to predict well in the conical diffuser. The special shape of the blade plays more prominent role at lower rotational speeds and creates coherent structures with opposite sign of vorticity. The vortex rope is captured by both turbulence models while DDES–SA presents more realistic one at higher rotational speeds.
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August 2016
Research-Article
Experimental and Numerical Investigation of the Precessing Helical Vortex in a Conical Diffuser, With Rotor–Stator Interaction
A. Javadi,
A. Javadi
Division of Fluid Dynamics,
Department of Applied Mechanics,
Chalmers University of Technology,
Göteborg SE-412 96, Sweden
e-mail: ardalan.javadi@chalmers.se
Department of Applied Mechanics,
Chalmers University of Technology,
Göteborg SE-412 96, Sweden
e-mail: ardalan.javadi@chalmers.se
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A. Bosioc,
A. Bosioc
Assistant Professor
Department of Hydraulic Machinery,
University Politehnica Timişoara,
Bv. Mihai Viteazu, No. 1,
Timişoara Ro-300222, Romania
e-mail: alin.bosioc@upt.ro
Department of Hydraulic Machinery,
University Politehnica Timişoara,
Bv. Mihai Viteazu, No. 1,
Timişoara Ro-300222, Romania
e-mail: alin.bosioc@upt.ro
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H. Nilsson,
H. Nilsson
Professor
Division of Fluid Dynamics,
Department of Applied Mechanics,
Chalmers University of Technology,
Göteborg SE-412 96, Sweden
e-mail: hani@chalmers.se
Division of Fluid Dynamics,
Department of Applied Mechanics,
Chalmers University of Technology,
Göteborg SE-412 96, Sweden
e-mail: hani@chalmers.se
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S. Muntean,
S. Muntean
Center for Advanced Research in
Engineering Sciences,
Romanian Academy—Timişoara Branch,
Bv. Mihai Viteazu, No. 24,
Timişoara Ro-300223, Romania
e-mail: seby@acad-tim.tm.edu.ro
Engineering Sciences,
Romanian Academy—Timişoara Branch,
Bv. Mihai Viteazu, No. 24,
Timişoara Ro-300223, Romania
e-mail: seby@acad-tim.tm.edu.ro
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R. Susan-Resiga
R. Susan-Resiga
Professor
Department of Hydraulic Machinery,
University Politehnica Timişoara,
Bv. Mihai Viteazu, No. 1,
Timişoara Ro-300222, Romania
e-mail: romeo.resiga@upt.ro
Department of Hydraulic Machinery,
University Politehnica Timişoara,
Bv. Mihai Viteazu, No. 1,
Timişoara Ro-300222, Romania
e-mail: romeo.resiga@upt.ro
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A. Javadi
Division of Fluid Dynamics,
Department of Applied Mechanics,
Chalmers University of Technology,
Göteborg SE-412 96, Sweden
e-mail: ardalan.javadi@chalmers.se
Department of Applied Mechanics,
Chalmers University of Technology,
Göteborg SE-412 96, Sweden
e-mail: ardalan.javadi@chalmers.se
A. Bosioc
Assistant Professor
Department of Hydraulic Machinery,
University Politehnica Timişoara,
Bv. Mihai Viteazu, No. 1,
Timişoara Ro-300222, Romania
e-mail: alin.bosioc@upt.ro
Department of Hydraulic Machinery,
University Politehnica Timişoara,
Bv. Mihai Viteazu, No. 1,
Timişoara Ro-300222, Romania
e-mail: alin.bosioc@upt.ro
H. Nilsson
Professor
Division of Fluid Dynamics,
Department of Applied Mechanics,
Chalmers University of Technology,
Göteborg SE-412 96, Sweden
e-mail: hani@chalmers.se
Division of Fluid Dynamics,
Department of Applied Mechanics,
Chalmers University of Technology,
Göteborg SE-412 96, Sweden
e-mail: hani@chalmers.se
S. Muntean
Center for Advanced Research in
Engineering Sciences,
Romanian Academy—Timişoara Branch,
Bv. Mihai Viteazu, No. 24,
Timişoara Ro-300223, Romania
e-mail: seby@acad-tim.tm.edu.ro
Engineering Sciences,
Romanian Academy—Timişoara Branch,
Bv. Mihai Viteazu, No. 24,
Timişoara Ro-300223, Romania
e-mail: seby@acad-tim.tm.edu.ro
R. Susan-Resiga
Professor
Department of Hydraulic Machinery,
University Politehnica Timişoara,
Bv. Mihai Viteazu, No. 1,
Timişoara Ro-300222, Romania
e-mail: romeo.resiga@upt.ro
Department of Hydraulic Machinery,
University Politehnica Timişoara,
Bv. Mihai Viteazu, No. 1,
Timişoara Ro-300222, Romania
e-mail: romeo.resiga@upt.ro
1Corresponding author.
Contributed by the Fluids Engineering Division of ASME for publication in the JOURNAL OF FLUIDS ENGINEERING. Manuscript received May 12, 2015; final manuscript received April 5, 2016; published online June 8, 2016. Assoc. Editor: Bart van Esch.
J. Fluids Eng. Aug 2016, 138(8): 081106 (13 pages)
Published Online: June 8, 2016
Article history
Received:
May 12, 2015
Revised:
April 5, 2016
Citation
Javadi, A., Bosioc, A., Nilsson, H., Muntean, S., and Susan-Resiga, R. (June 8, 2016). "Experimental and Numerical Investigation of the Precessing Helical Vortex in a Conical Diffuser, With Rotor–Stator Interaction." ASME. J. Fluids Eng. August 2016; 138(8): 081106. https://doi.org/10.1115/1.4033416
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