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        <description>Pipe Constriction

Experiments by Durst and Wang

----------

Description

The flow through a wall-mounted constriction in a pipe was studied, with geometry shown
schematically in .  Refractive index matching was employed to ensure 
that velocity measurements could be obtained in all regions inside of measured positions. 
Laser-Doppler-anemometry was used to obtain quantitative velocity information.\(d\)\(U_{\max}\)\(2.2\times 10^4\)\(D\)\(d\)\(L=1\)\(25\)\(L/d=0.04\)\(1\)\(60 D\)\(36 D\)\(L/d=0…</description>
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        <title>case083</title>
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        <description>Wall-Mounted 2-D Hump with Oscillatory Zero-Mass-Flux Jet or Suction through a Slot

Experiments by Greenblatt, Paschal, Yao, Harris, Schaeffler and Washburn

----------

Description

The case is a wall-mounted Glauert-Goldschmidt type body, geometrically 
similar to that employed by Seifert and Pack (2002). Full details of the 
current case are given in Greenblatt et al (2004, 2005) and 
Naughton et al (2004). The model is mounted between two glass endplate frames,
as shown in \(x = 0.0\)\(x = …</description>
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        <title>case095</title>
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        <description>Thermal Boundary Layers in Turbulent Rayleigh-Bénard Convection with Rough and Smooth Surfaces

Experiments by du Puits

----------

Description

In this data set, we provide wall-normal profiles of the mean temperature
\(\overline{T}(z)\) (\(z\) is the coordinate perpendicular to the wall) and its fluctuations
\(T'(z)\)\(\mu\)\(\mu\)\(Ra=5.4\times 10^9\)\(Ra&lt;9.6\times 10^{11}\)\(\Gamma=1.1\)\(\Gamma=2.9\)\(Pr=0.7\)\[ Ra = \frac{\beta g \Delta T H^3}{\nu \kappa} \qquad\qquad Pr = \frac{\nu}{\kap…</description>
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        <description>Local and Time-Resolved Wall Heat Flux in Turbulent Rayleigh-Bénard Convection

Experiments by du Puits and Hertlein

----------

Description

In this data set, we provide direct and time-resolved measurements of the local wall heat 
flux in turbulent Rayleigh-Bénard convection in air. The measurements have been performed 
at the heated bottom and the cooled top plate of a large-scale Rayleigh-Bénard experiment 
which is called \(R=0.45\)\(Ra=8.5\times 10^5\)\(Ra \approx 2.6\times 10^9\)\(Pr=0.7…</description>
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        <description>Viscous Boundary Layers in Turbulent Rayleigh-Bénard Convection

Experiments and DNS by Li, Resagk, du Puits, Shi, Emran, Schumacher and Thess

----------

Description

The velocity field has been studied in a large-scale Rayleigh-Bénard (RB) experiment 
(called \(Ra_{max} = 10^{12}\)\(Ra = (\gamma g \Delta \theta H^3)/(\nu k)\)\(Pr = \nu/k\)\(\Gamma = D/H\)\(Re = (v_m H)/\nu\)\(Nu = (4Hq)/(\lambda \pi D^2\Delta \theta)\)\(\gamma\)\(g\)\(\Delta \theta\)\(\nu\)\(k\)\(D\)\(H\)\(v\)\(q\)\(\lambda\)…</description>
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        <title>case095-plots</title>
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        <description>Thermal Boundary Layers in Turbulent Rayleigh-Bénard Convection with Rough and Smooth Surfaces

Sample Data Plots

The plots below show profiles of mean and rms non-dimensional temperature in the aspect ratio 1.1 case.



The plots below show profiles of mean and rms non-dimensional temperature in the aspect ratio 2.9 case.</description>
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