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                <rdf:li rdf:resource="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case081-plots&amp;rev=1690371289&amp;do=diff"/>
                <rdf:li rdf:resource="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case081&amp;rev=1690371289&amp;do=diff"/>
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    </channel>
    <image rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/lib/exe/fetch.php?media=logo.png">
        <title>ERCOFTAC Classic Collection</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/</link>
        <url>http://cfd.mace.manchester.ac.uk/ercoftac/lib/exe/fetch.php?media=logo.png</url>
    </image>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case001-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case001-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case001-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Isothermal Dump Combustor With Swirl

Sample Data Plots

The plots below show profiles of mean swirl and streamwise velocity components, turbulent kinetic energy and shear stress \(\overline{uv}\) at a selection of streamwise locations.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case001&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case001</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case001&amp;rev=1690371289&amp;do=diff</link>
        <description>Isothermal Dump Combustor With Swirl

Experiments by Ahmed, Boray and Nejad

----------

Description

Isothermal confined swirling and non-swirling flows in a dump combustor. 
The case is a 2D axisymmetric flow with constant temperature.

Geometry of the Computational Domain
\(D_i=2R_i =101.6\)\(D=2R=152.4\)\(H\)\(8H\)\(4.3H\)\(S=0.3\)\(3.2H\)\(S=0.5\)\(S=0.5\)\(4.4H\)\(x/H=15\)\(x/H=24\)\(\nu = 1.56 \times 10^{-5}\)\(U_{ref} = 19.2 \pm 0.4\)\(Re = 1.25 \times 10^5\)\(S=0.3\)\(0.4\)\(0.5\)\[ S =…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case002-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case002-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case002-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>3D Flow in Wedge-Plate Junction

Sample Data Plots

The plots below show velocity vectors on 4 planes parallel to the wall, but at
varying distances, \(y\), from it.



The plots below show mean \(U\) velocity and temperature profiles at 4 locations
following a streamline along the duct.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case002&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case002</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case002&amp;rev=1690371289&amp;do=diff</link>
        <description>3D Flow in Wedge-Plate Junction

Experiments by Anderson and Eaton

----------

Description

Three dimensional thermal boundary layer ahead and on the side of 
an upstream-facing wedge. The flow is a 3D flow with temperature variation.

Geometry

The wind-tunnel consists of two parallel planes separated by 11.9 cm with a
development section for the preliminary two-dimensional boundary layer and a 
test-section including the wedge and a heating surface. The geometry is shown in
\(x = 7.6\)\(x = 1…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case003-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case003-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case003-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Plane Wake after a Circular Cylinder

Sample Data Plots

The plots below show profiles of the dynamic and thermal fields downstream of the cylinder at
\(x/d=420\).</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case003&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case003</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case003&amp;rev=1690371289&amp;do=diff</link>
        <description>Plane Wake after a Circular Cylinder

Experiments by Antonia and Browne

----------

Description

Plane turbulent wake downstream of a heated circular cylinder.
A 2D flow with temperature as passive scalar.

Geometry and Flow Characteristics

The wake-generating body is a stainless steel tube
of \(d = 2.67\)\(x = 0\)\(y = 0\)\(x/d=-10\)\(x/d = 420\)\(\nu =1.53 \times 10^{-5}\)\(U_e = 6.70\)\(d\)\(Re_d = 1170\)\(x/d = 420\)\(L = 12.3\)\(U_o = 0.36\)\(T_o = 0.82\)\(x/d\)\(U_e\)\(\delta(\overline{v…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case004-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case004-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case004-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Swirling and Non-Swirling Flow in Curved Pipe

Sample Data Plots

The plots below show profiles along the horizontal and vertical axes of the pipe of axial and 
cross-stream velocity components, axial rms velocity and turbulent shear stress at selected 
locations upstream of the bend, through the bend, and downstream.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case004&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case004</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case004&amp;rev=1690371289&amp;do=diff</link>
        <description>Swirling and Non-Swirling Flows in Curved Pipe

Experiments by Anwer and So

----------

Description

Swirling and non-swirling flows in a circular cross
section pipe made of a 180o bend and two long 
straight inlet and outlet parts.
3D flow with constant temperature.\(D = 2a = 76.2\)\(R = 495.3\)\(96D\)\(1D\)\(s\)\(s&lt;0\)\(s&gt;0\)\(\theta\)\(s/D=-12\)\(-6\)\(\theta = 112.5^o\)\(s/D = 18\)\(\nu = 1.58 \times 10^{-5}\)\(W_o = 10.4\)\(W_oD/\nu = 5 \times 10^5\)\(s/D = -18\)\(w_{\tau s} = 0.323\)\(\Om…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case005-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case005-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case005-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Unsteady Boundary Layer

Sample Data Plots

The plots below show profiles across the boundary layer of mean velocity and Reynolds
stress components at three \(x\) locations along the test section.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case005&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case005</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case005&amp;rev=1690371289&amp;do=diff</link>
        <description>Unsteady Boundary Layer

Experiments by Brereton, Reynolds, Jayaraman

----------

Description

Developing turbulent boundary layer responding to a forced sinusoidal
free stream unsteadiness. 2D flow with constant temperature.

Geometry of the Computational Domain
\( \langle U_{\infty} \rangle = U_o(1-A) + U_oA cos(\omega t)\)\(U_{\infty}\)\(U_o\)\(A\)\(\partial (\langle U_{\infty} \rangle/U_o)/\partial x\)\(A\)\(\nu = 1.1 \times 10^{-6}\)\(U_o = 0.74\)\(x_o\)\(x=0\)\(\delta^* = 6.8\)\(\theta = …</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case006-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case006-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case006-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Square-Section Duct 180 Degree Bend

Sample Data Plots

The plots below show profiles at different heights across the duct, for a range
of angular positions around the bend.











The contours below show data provided for use as inlet conditions at \(z/D=-1\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case006&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case006</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case006&amp;rev=1690371289&amp;do=diff</link>
        <description>Square-Section Duct 180 Degree Bend

Experiments by Choi, Moon, Yang

----------

Description

Turbulent flow in a square cross-section duct made of a 180o bend and two
long straight inlet and outlet parts. 3D flow with constant temperature.

Geometry of the Computational Domain
\(D \times D = 88.9 \times 88.9\)\(R_c = 3.357D\)\(30D\)\(W_B = 11\)\(W_B\)\(Re = W_B D/\nu = 56,690\)\(U\)\(V\)\(W\)\(k\)\(\varepsilon\)\(1D\)\(\Psi = 0^o\)\(45^o\)\(90^o\)\(135^o\)\(180^o\)\(U/W_B\)\(V/W_B\)\(W/W_B\)\(…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case007-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case007-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case007-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Circular to Rectangular Transition Duct

Sample Data Plots

The plots below show radial profiles at the inlet section, \(x/D=-0.5\)
of angular positions around the bend.



The plots below show profiles along the semi-major and semi-minor axes
at the measurement locations \(x/D=1.1\)\(1.4\)\(2.0\)\(3.0\)\(C_P\)\(C_f\)\(x/D=2.0\)\(4.0\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case007&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case007</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case007&amp;rev=1690371289&amp;do=diff</link>
        <description>Circular to Rectangular Transition Duct

Experiments by Davis and Gessner

----------

Description

Turbulent flow in a circular to rectangular transition duct. The flow remains
wholly attached along the transition.  A 3D flow with constant temperature.\(0.5D\)\(D = 2R = 204.3\)\(2D\)\[ \left(y/a \right)^{\eta} + \left( z/b\right)^{\eta} = 1  \]\(a\)\(b\)\(\eta\)\(x\)\(a\)\(b\)\(\eta\)\(T = 298.3\)\(U_b=29.95\)\(\nu =1.57 \times 10^{-5}\)\(Re=U_b D/\nu =3.9 \times 10^5\)\(x/D=-0.5\)\(\delta/R=0.…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case008-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case008-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case008-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Wing/Body Junction with Separation

Sample Data Plots

The plots below show profiles on the symmetry plane, \(z=0\), upstream of the wing.



The plots below show streamwise velocity profiles and cross-stream velocity vectors at \(x/C=0.18\).



The plots below show streamwise velocity profiles and cross-stream velocity vectors at \(x/C=0.75\)\(x/C=1.05\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case008&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case008</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case008&amp;rev=1690371289&amp;do=diff</link>
        <description>Wing/Body Junction with Separation

Experiments by Devenport, Simpson and Fleming

----------

Description

Turbulent flow at the junction of a flat surface and a normally-mounted cylindrical wing dominated by 
the presence of a horseshoe vortex. 3D flow with constant temperature.\(T = 71.7\)\(18.24T\)\(x\)\(U_{ref} = 26.75\)\(x/T = -18.24\)\(z = 0\)\(y/T\)\(U/U_{ref}\)\(\overline{u^2}/U_{ref}^2\)\(\overline{w^2}/U_{ref}^2\)\(\overline{uw}/U_{ref}^2\)\(x/T=-2.146\)\(T\)\(U_{ref}\)\(\delta/T\)\(\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case009-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case009-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case009-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Natural Convective Vertical Boundary Layer

Sample Data Plots

The plot below shows the Nusselt number distribution along the wall for two wall temperature cases.



The plots below show mean velocity and temperature profiles across the boundary layer at four 
locations along the plate.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case009&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case009</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case009&amp;rev=1690371289&amp;do=diff</link>
        <description>Natural Convective Vertical Boundary Layer

Experiments by Tsuji and Nagano

----------

Description

Turbulent natural convective boundary layer along a vertical heated copper
plate. 2D incompressible air flow with temperature and density variation.\(x = 0.8\)\(T_a = 16\)\(\nu = 1.67 \times 10^{-5}\)\(p_a = 1017\)\(T_w = 60\)\(T_w = 100\)\(Pr = 0.71\)\(Gr_x = g(T_w - T_a)x^3/((273. + T_a)\nu^2) = 5.50 \times 10^9 x^3\)\(Nu_x = q_wx/((T_w - T_a)\lambda_w)\)\(q_w\)\(\lambda_w\)\(U_b = (g(T_w - T_…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case010-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case010-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case010-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Couette Flow with Fixed Wavy Wall

Sample Data Plots

The plots below show the mean and rms streamwise velocity at eight sections along the 
channel. In each profile \(y\) represents distance from the wavy wall.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case010&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case010</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case010&amp;rev=1690371289&amp;do=diff</link>
        <description>Couette Flow with Fixed Wavy Wall

Experiments by Nakabayashi, Kitoh and Iwata

----------

Description

Experimental work has been performed to investigate turbulent Couette-type flow with
repeated longditudinal pressure gradients that are realized in a channel consisting of a
wavy fixed wall on one side and a moving wall on the other.\(L = 1.4\)\(2h = 15\)\(y = 2h - e\,cos(2\pi x/L)\)\(e = 4.5\)\(x/l\)\(Re=2hU_b/\nu=8000\)\(u^{-1} = (\nu dp/dx)/(\rho (U^*)^3)\)\(x/l\)\(u^{-1}\)\(x=0\)\(U\)\(V\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case011-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case011-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case011-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Airfoil Boundary Layer and Wake

Sample Data Plots

The plot below shows the surface pressure coefficient distribution around the two airfoil models.



The plots below show mean velocity and Reynolds stress profiles at five locations (two before the trailing edge, three in the wake) for Model A.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case011&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case011</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case011&amp;rev=1690371289&amp;do=diff</link>
        <description>Airfoil Boundary Layer and Wake

Experiments by Nakayama

----------

Description

Flows around two different airfoil models: a conventional one at zero
incidence and a supercritical one at an angle of attack of 4o, in the same
flow conditions. 2D flows at low Mach number.\(C = 24\)\(\approx 610\)\(x/C=0.16\)\(x/C=0.05\)\(U_{ref} = 30.5\)\(Re_C = 1.2\times 10^6\)\(U_{ref} = 30.5\)\(C_p = (p - p_{ref})/(0.5\rho U_{ref}^2)\)\(p_{ref}\)\(\delta(C_p)\)\(\pm 0.03\)\(\delta(\text{second order moments}…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case012-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case012-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case012-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Vortices in Boundary Layer

Sample Data Plots

The plots below show contours of streamwise velocity and Reynolds stress, together with cross-stream
vectors, at \(x=97\) cm.



The plots below show contours of streamwise velocity and Reynolds stress, together with cross-stream
vectors, at \(x=188\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case012&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case012</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case012&amp;rev=1690371289&amp;do=diff</link>
        <description>Vortices in Boundary Layer

Experiments by Pauley and Eaton

----------

Description

Flow over an initially two-dimensional turbulent boundary layer with longitudinal
embedded vortices. 3D flow with constant temperature.

Geometry of the Computational Domain
\(x = 0\)\(x=200cm\)\(x = 188\)\(0.16 &lt; y &lt; 6.75\)\(0 \le z \le 15\)\(U_e = 16\)\(x=0\)\(x = -53\)\(Re = 1700\)\(\delta(\text{flow angles})\)\(\pm 0.5^o\)\(\delta(\text{velocity vector magnitudes})\)\(\pm 5\%\)\(x\)\(x=97\)\(188\)\(U/U_e\)\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case013-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case013-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case013-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Sudden Pipe Expansion

Sample Data Plots

The graphs below show mean velocity and turbulent kinetic energy profiles upstream of the expansion, at \(x/D=-0.25\).



The graphs below show mean velocity and Reynolds stress profiles just downstream of the expansion, at \(x/D=0.05\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case013&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case013</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case013&amp;rev=1690371289&amp;do=diff</link>
        <description>Sudden Pipe Expansion

Experiments by Szczepura

----------

Description

Flow of water in a sudden pipe expansion.  One of the aims of the experiment was to 
provide results which shed light upon the limitations of the standard 
\(k\)-\(\varepsilon\) model for turbulent flows.\(d = 78.3\)\(47d\)\(D = 152.4\)\(4.2D\)\(8.0D\)\(x/D = 1.5\)\(x/D = 2.3\)\(x/D = 1.4\)\(2.2\)\(4 \times 10^5\)\(\overline{u_1u_2}\)\(x/D = 0.35\)\(Re = 2\times 10^5\)\(x/D = -0.25\)\(r/D\)\(U\)\(V\)\(k\)\(\nu_t\)\(\vareps…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case014-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case014-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case014-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Homogeneous Curved Flow

Sample Data Plots

The graphs below show the development along the tunnel centreline of the turbulent kinetic energy and
the ratios \(\overline{uv}/k\), \(\overline{u^2}/k\) and \(\overline{v^2}/k\) for the six cases.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case014&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case014</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case014&amp;rev=1690371289&amp;do=diff</link>
        <description>Homogeneous Curved Flow

Experiments by Holloway and Tavoularis

----------

Description

These experiments were carried out in order to study the effects of curvature on sheared turbulence 
in relative isolation from wall and entrainment effects. Uniformly sheared turbulence was allowed to reach 
a state of transverse statistical homogeneity in a rectangular straight duct and then passed into a curved 
duct, also of rectangular cross section.\(S\)\[ S = \frac{(U_c/R_c)}{dU/dn} \]\(U_c\)\(dU/dn\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case015-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case015-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case015-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Transitional Cascade Blade

Sample Data Plots

The graph below shows the \(C_p\) distribution along the blade for the three incidence angles.



The graphs below show velocity profiles at selected locations over the suction and pressure surfaces and in the wake for the \(5^o\)\(-8.5^o\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case015&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case015</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case015&amp;rev=1690371289&amp;do=diff</link>
        <description>Transitional Cascade Blade

Experiments by Zierke and Deutsch

----------

Description

Flow around a highly loaded compressor blade in cascade at three different
incidence angles.

2D flow with constant temperature.

Geometry

Domain around a double-circular-arc blade.\[ x_p^2 + (y_p + 219.7)^2 = 246.8^2 \]\[ x_s^2 + (y_s + 149.5)^2 = 189.1^2 \]\[ x_c^2 + (y_c + 179.4)^2 = 212.8^2 \]\(0.9144\)\(c=228.6\)\(s=106.8\)\(212.8\)\(\phi=65\)\(\gamma=20.5\)\(c = 228.6\)\(c/s=2.14\)\(0.9144\)\(\nu = 1.5…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case016-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case016-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case016-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Horizontal Convective Boundary Layer

Sample Data Plots

The graphs below show non-dimensionalized mean temperature, temperature variance, Reynolds stresses and
turbulent heat flux profiles at the three times of \(t^*=6\), \(6.5\) and \(7\).</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case016&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case016</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case016&amp;rev=1690371289&amp;do=diff</link>
        <description>Horizontal Convective Boundary Layer

LES by Schmidt and Schumann

----------

Description

Convective boundary layer in the atmosphere, uniformly heated from below and
topped by a layer of uniformly stratified fluid, for zero mean horizontal
flow. Results from Large Eddy Simulations.\(X = 8000\)\(= 5z_{io}\)\(x\)\(y\)\(z = 0\)\(z = 2400\)\(= 1.5z_{io}\)\(z_{io}\)\(\nu = 1.5\times 10^5\)\(\rho = 1.43\)\(Q_s = 0.06\)\(T_o = 26.6\)\(z_i\)\(z_{io} = 1600\)\(\beta = 1/300\)\(w^*_o = (\beta gQ_sz_{io…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case017-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case017-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case017-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Laterally Strained Boundary Layers

Sample Data Plots

The graphs below show the profiles of the side and top wall along the duct for the laterally
converging wall case. The diverging case is the same duct, but reversed.



The graphs below show the development of the wall friction coefficient, and boundary layer
thickness parameters along the duct centreline for the three cases (2D = flat plate boundary layer,
3C = converging case, 3D = diverging case).</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case017&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case017</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case017&amp;rev=1690371289&amp;do=diff</link>
        <description>Laterally Strained Boundary Layers

Experiments by Pompeo, Bettelini, Thomann

----------

Description

Turbulent boundary layers on a flat surface laterally strained by converging or
diverging walls. 3D flow with constant temperature.

Geometry of the Computational Domain
\(x\)\(\partial W/\partial z(x,0,0)\)\(y=0\)\(z=0\)\(y=0\)\(y\)\(T = 28\)\(U_o = 42\)\(p = 967\)\(\nu = 1.7 \times 10^5\)\(\rho = 1.11\)\(x = 0\)\(\delta = 16\)\(\delta_1 = 2.3\)\(\delta_2 = 1.7\)\(y\)\(z = 0\)\(y\)\(C_p = (p …</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case018-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case018-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case018-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>2D Model Hill Flows

Sample Data Plots

The graphs below show profiles of mean velocity and Reynolds stresses at a selection
of streamwise locations in the isolated single hill case.



The graphs below show profiles of mean velocity and Reynolds stresses at a selection
of streamwise locations in the periodic hill case.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case018&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case018</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case018&amp;rev=1690371289&amp;do=diff</link>
        <description>2D Model Hill Flows

Experiments by Almeida, Durao, Heitor

----------

Description

Flows over 2D polynomial-shaped obstacle(s) mounted on a flat plate with
recirculation region in their wake.

Two configurations are available, as shown in .
In the first configuration, case \(A\)\(B\)\(H = 170\)\(h_{max} = 28\)\(2R = 108\)\(4.5h_{max}\)\(h(x)\)\(\nu = 1\times 10^{-6}\)\(U_o = 2.147\)\(U_oh/\nu = 60,000\)\(U\)\(\overline{u^2}\)\(\overline{v^2}\)\(\overline{w^2}\)\(\overline{uv}\)\(C_f = 0.0027\)…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case019-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case019-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case019-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Boundary Layer with Adverse Pressure Gradient

Sample Data Plots

The graphs below show profiles of wall pressure coefficient, and free-stream
velocity (derived from the pressure measurements) along the pipe for the three
cases reported, over the range of \(x_A\)\(x_E\)\(q_D\)\(x_M\)\(x_A\)\(x_M\)\(x_A\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case019&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case019</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case019&amp;rev=1690371289&amp;do=diff</link>
        <description>Boundary Layer with Adverse Pressure Gradient

Experiments by Gasser and Thomann

----------

Description

Two-dimensional incompressible turbulent boundary layers with strong adverse pressure gradients.

&lt;[Flow geometry]Flow geometry and test section&gt;

The boundary layer develops over the inner wall of an annular pipe of diameter 200 mm. As shown in
\(x_M\)\(x_A\)\(x_A\)\(x_M\)\(x_M\)\(x_E\)\(x_M\)\(q_D=P_o - P_D\)\(x_A\)\(q_D\)\(x_A\)\(q_D=600\)\(1000\)\(x_A=-100\)\(0\)\(50\)\(100\)\(200\)\(30…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case020-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case020-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case020-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flat Plate Transitional Boundary Layers

Sample Data Plots

The graphs below show the skin friction coefficient development along the
plate (left hand graph for aero-pressure-gradient cases, right hand graph for
the variable pressure gradient cases).\(C_p\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case020&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case020</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case020&amp;rev=1690371289&amp;do=diff</link>
        <description>Flat Plate Transitional Boundary Layers

Experiments by Coupland

----------

Description

Flat-plate transitional 2D boundary layers flows with or without pressure gradient. No
temperature variations.

Free-stream velocity and turbulence intensity  vary between \(U_o = 1.2\)\(19.8\)\(Tu_o = 0.9\)\(6.6\)\(C_p\)\(y^+ &lt; 3\)\(U\)\(V\)\(U\)\(W\)\(\overline{uv}\)\(\overline{uw}\)\(u'\)\(x\)\(x\)\(x\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case021-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case021-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case021-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Sink-Flow Boundary Layer

Sample Data Plots

The graph below shows the mean velocity log-plot for the three acceleration cases.



The graphs below show the Reynolds stress profiles for the three acceleration cases.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case021&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case021</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case021&amp;rev=1690371289&amp;do=diff</link>
        <description>Sink-Flow Boundary Layer

DNS by Spalart

----------

Description

The data are from direct numerical simulations of sink-flow boundary layers, with acceleration parameters 
\(K=(\nu/U_{\infty}^2)(dU_{\infty}/dx)\) between \(1.5\times 10^{-6}\) and \(2.75\times 10^{-6}\). The three-dimensional, 
time-dependent Navier-Stokes equations are solved numerically using a spectral method.\(170 \times 30 \times 85\)\(x\)\(y\)\(z\)\(8.7\times 10^5\)\(\Lambda_x\)\(\Lambda_z\)\(125\delta^*\)\(25\delta^*\)\(…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case022-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case022-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case022-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Boundary Layer in and Downstream from Convex Curvature

Sample Data Plots

The graph below shows the skin friction coefficient development along the wall.



The graph below show mean velocity profiles upstream and downstream of the curved section,
compared to the standard log-law.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case022&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case022</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case022&amp;rev=1690371289&amp;do=diff</link>
        <description>Boundary Layer In and Downstream from Convex Curvature

Experiment by Alving, Smits, Watmuff

----------

Description

Developing boundary layer submitted to stabilizing convex curvature at \(Re_{\theta} = 6000\) without 
longitudinal pressure gradient (\(S = \partial p/\partial x \approx 0\)).

A study to examine the flat plate relaxation behaviour of a turbulent boundary layer recovering 
from 90\(\delta_o/R = 0.08\)\(90\delta_o\)\(\delta_o\)\(\times\)\(R = 300\)\(s\)\(Re_{\theta}\)\(\delta_o\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case023-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case023-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case023-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Boundary Layer in a Concave Bend

Sample Data Plots

For the case with no turbulence-generating grid the graphs below show profiles of mean 
velocity and Reynolds stresses upstream of the bend (\(x=-56\)cm) and at four stations 
through the bend.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case023&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case023</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case023&amp;rev=1690371289&amp;do=diff</link>
        <description>Boundary Layer in a Concave Bend

Experiments by Johnson

----------

Description

Developing boundary layer submitted to destabilizing concave curvature at 
\(Re_{\theta} = 1450\) without longitudinal pressure 
gradient (\(S = \partial p/\partial x \approx 0\)).

The test facility is a free surface water channel, shown schematically in \(R = -136\)\(y^+ \approx 5\)\(u'\)\(w'\)\(y^+\)\(M = 6.35\)\(M/w = 4\)\(u'/U_{pw} = 0.05\)\(x=-56\)\(x=35.5\)\(15^o\)\(x=71\)\(30^o\)\(x=106.5\)\(45^o\)\(x=142\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case024-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case024-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case024-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Stably Curved Mixing Layer

Sample Data Plots

The plots below show profiles of the total mean velocity, and the Reynolds stress components 
(using the polar coordinate system) at a selection of angular locations in the curved part of the layer.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case024&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case024</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case024&amp;rev=1690371289&amp;do=diff</link>
        <description>Stably-Curved Mixing Layer

Experiments by Castro and Bradshaw

----------

Description

As part of a general investigation of complex turbulent flows, extensive one-point measurements 
have been made of the turbulence structure of the mixing layer bounding a normally impinging 
plane jet with an irrotational core. The ratio of shear-layer thickness to streamline radius of 
curvature reaches a maximum of about 0.2, the sense of the curvature being stabilizing. 
Downstream of the impingement regi…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case025-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case025-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case025-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Normally Impinging Jet from a Circular Nozzle

Sample Data Plots

The plots below show profiles of the mean velocity and second moments (plotted against distance from the impingement wall) at a selection of radial locations for the \(H/D=2\), \(Re=23000\) case.



The plots below show profiles of the mean velocity and second moments (plotted against distance from the impingement wall) at a selection of radial locations for the \(H/D=2\)\(Re=70000\)\(H/D=6\)\(Re=70000\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case025&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case025</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case025&amp;rev=1690371289&amp;do=diff</link>
        <description>Normally-Impinging Jet from a Circular Nozzle

Experiments by Cooper, Jackson, Launder, Liao, and Baughn and Shimizu

----------

Description

The experiments provide an extensive set of measurements of a circular turbulent 
jet impinging orthogonally onto a large plane surface, as shown in \(2.3\times 10^4\)\(7\times 10^4\)\(x-r\)\(r/D=6\)\(r/D=8\)\(1275\times 975\)\(H/D\)\(r/D\)\(H/D = 2\)\(r/D = 9\)\(r/D = 3\)\(2.3\times 10^4\)\(2.3\times 10^4\)\(7.1\times 10^4\)\(H/D\)\(u'\)\(v'\)\(y\)\(y_{1…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case026-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case026-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case026-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Single-Stream Swirling Jet in Still Air

Sample Data Plots

The plots below show development along the jet of the centreline velocity, maximum swirl
velocity and jet halfwidth.



The plots below show profiles of the mean streamwise and swirl velocity components, and the
Reynolds stresses, plotted against normalised distance across the jet, at the six streamwise 
measurement locations.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case026&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case026</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case026&amp;rev=1690371289&amp;do=diff</link>
        <description>Single-Stream Swirling Jet in Still Air

Experiments by Morse

----------

Description

Single-stream swirling jet in still air.

Swirl number: \(S = G_{\theta}/(RG_{x}) = 0.36\) where \(G_x\) and \(G_{\theta}\) are
the axial and angular momentum fluxes, and \(R\) the incoming pipe radius.

Exit Reynolds number: \(Re = 56,000\)\(U\)\(V\)\(W\)\(\overline{u_iu_j}\)\(S = 0\)\(S = 0.36\)\(x/D = 6\)\(U\)\(\overline{u^2}\)\(\overline{v^2}\)\(x/D\)\(U\)\(V\)\(W\)\(U\)\(W\)\(U\)\(V\)\(W\)\(U\)\(W\)\(P\)…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case027-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case027-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case027-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Infinite 35 Degree Swept Wing

Sample Data Plots

The plot below shows the distribution of wall pressure coefficient along the plate.



The plots below show profiles of the mean velocity and Reynolds stress components at a
selection of streamwise locations along the plate.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case027&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case027</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case027&amp;rev=1690371289&amp;do=diff</link>
        <description>Infinite 35 Degree Swept Wing

Experiments by Van den Berg, Elsenaar, Lindhout, Wesseling

----------

Description

This study was undertaken by the authors in order to investigate three-dimensional turbulent boundary layers.
A two dimensional boundary layer initially developed on a test plate is subjected to adverse pressure gradient leading to three
dimensional separation near the trailing edge of the plate.\(Re_{\theta} = 3290\)\(\times\)\(y=75\)\(x= 0.52\)\(0.62\)\(0.72\)\(0.82\)\(0.92\)\(1.…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case028-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case028-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case028-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Pseudo-Ekman Boundary Layer

Sample Data Plots

The plots below show profiles of the mean \(U\) and \(W\) velocities, and the
Reynolds stress components, across the boundary layer.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case028&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case028</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case028&amp;rev=1690371289&amp;do=diff</link>
        <description>Pseudo-Ekman Boundary Layer

DNS by Spalart

----------

Description

In this study, a three dimensional boundary layer is simulated on an infinite flat plate by a time
dependent free-stream velocity vector, whose magnitude is independent of time but whose
direction, as seen in plan view, changes at a constant angular velocity (see \(Re_1 = U_o(2/(f\nu))^{1/2} = 500\)\(620\)\(767\)\(U_o\)\(f\)\([-\infty,\infty]\times [0,\infty]\times [-\infty, \infty]\)\(x\)\(y\)\(z\)\(y = 0\)\((u, v, w) = 0\)\(…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case029-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case029-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case029-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Time-Periodic Boundary Layer

Sample Data Plots

The plot below shows the variation of mean wall shear stress through the periodic cycle.



The plots below show profiles of the mean \(U\) velocity, rms \(u'\) and \(v'\), and
\(\overline{uv}\) across the boundary layer at a selection of phase times through the cycle.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case029&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case029</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case029&amp;rev=1690371289&amp;do=diff</link>
        <description>Time-Periodic Boundary Layer

Experiments by Jensen, Sumer, Fredsoe

----------

Description

The data is for turbulent oscillatory boundary-layer flow over a smooth wall. The free-stream
flow is a purely oscillating flow with sinusoidal velocity variation. Mean and turbulence properties were 
measured mainly in two directions, namely in the streamwise direction and in the direction perpendicular to 
the wall. Some measurements were made also in the transverse direction. The measurements were ca…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case030-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case030-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case030-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Backward-Facing Step with Inclined Opposite Wall

Sample Data Plots

The plot below shows the variation of wall friction coefficient along the step wall for
the \(\alpha=0^o\) and \(6^o\) cases.



The plot below shows the variation of pressure coefficient along the step and top walls for
the \(\alpha=0^o\)\(6^o\)\(U\)\(\overline{u^2}\)\(\overline{v^2}\)\(\overline{uv}\)\(\alpha=0^o\)\(U\)\(\overline{u^2}\)\(\overline{v^2}\)\(\overline{uv}\)\(\alpha=6^o\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case030&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case030</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case030&amp;rev=1690371289&amp;do=diff</link>
        <description>Backward-Facing Step with Inclined Opposite Wall

Experiments by Driver and Seegmiller

----------

Description

Experimental data have been obtained in an incompressible turbulent flow over a rearward-facing step in a 
diverging channel flow.

Mean velocities, Reynolds stresses, and triple products that were measured by a laser Doppler velocimeter 
are presented for two cases of tunnel wall divergence. Eddy viscosities, production, convection, turbulent 
diffusion, and dissipation (from a balan…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case031-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case031-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case031-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Backward-Facing Step

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity, rms velocities
\(u'\), \(v'\), \(w'\), and shear stress \(\overline{uv}\) at selected streamwise locations.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case031&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case031</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case031&amp;rev=1690371289&amp;do=diff</link>
        <description>Backward-Facing Step

DNS by Le and Moin

----------

Description

Simulation of flow over a backward-facing step.

The mean velocity profile obtained from a boundary layer simulation by Spalart (1988) is
imposed at the inlet at  \(Re_{\theta}= 667\).
Random velocity fluctuations \(u'\)\(v'\)\(w'\)\(10h\)\(20h\)\(h\)\(H_1 = 5h\)\(H_2 = 6h\)\(ER\)\(h\)\(U_0\)\(Re_h = 5100\)\(\omega_z\)\(U_0/h\)\(x_R = 6h\)\(x\)\(z\)\(y\)\(W\)\(4h\)\(770 \times 194 \times 66\)\(x/h=-3\)\(4\)\(6\)\(10\)\(15\)\(19\)…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case032-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case032-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case032-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Channel Flow

Sample Data Plots

The plots below show profiles of the mean velocity and Reynolds stresses for the two
cases available.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case032&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case032</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case032&amp;rev=1690371289&amp;do=diff</link>
        <description>Channel Flow

DNS by Kim, Moin, Moser

----------

Description

Direct numerical simulation of a turbulent channel flow where all essential scales of motion are
resolved.

Two cases are reported, one with \(Re \approx 3300\) based on channel half height and centreline 
velocity, and the other with \(Re \approx 7890\)\(Re_{\tau} = 180\)\(395\)\(\delta\)\(192\times 129\times 160\)\(x\)\(y\)\(z\)\(Re_{\tau}=180\)\(4\pi \delta\)\(2\pi \delta\)\(\Delta x^+ \approx 12\)\(\Delta z^+ \approx 7\)\(y_j = …</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case033-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case033-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case033-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Constant-Pressure Boundary Layer

Sample Data Plots

The plots below show profiles of the mean velocity and Reynolds stresses for the three
values of \(Re_{\theta}\) available.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case033&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case033</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case033&amp;rev=1690371289&amp;do=diff</link>
        <description>Constant-Pressure Boundary Layer

DNS by Spalart

----------

Description

The turbulent boundary layer on a flat plate, with zero pressure gradient, was simulated 
numerically at four stations between \(Re_{\theta} = 225\) to \(Re_{\theta} = 1410\). The 
three-dimensional time-dependent Navier-Stokes equations are solved using a spectral method 
with up to about 10\(\delta^*\)\(\delta\)\(\theta\)\(y_o\)\(\delta^*\)\(x\)\(x\)\(Re_{\theta}=300\)\(670\)\(1410\)\(Re_{\theta}\)\(Re_{\theta}=300\)\(R…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case034-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case034-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case034-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Plane Mixing Layer

Sample Data Plots

The plots below show the profiles of mean and rms streamwise velocity just downstream of the
splitter plate.



The plots below show the development of the vorticity thickness and momentum thickness of
the mixing layer along the channel.\(X=150\)\(200\)\(250\)\(650\)\(800\)\(950\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case034&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case034</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case034&amp;rev=1690371289&amp;do=diff</link>
        <description>Plane Mixing Layer

Experiments by Delville, Bellin, Garem, Bonnet

----------

Description

The subsonic turbulent plane mixing layer under investigation has the following
characteristics: external velocities of \(U_a = 42.8\) and 
\(U_b = 25.2\) m/s, fully turbulent co-flowing boundary 
layers; the test section is \(30\times 30\)\(U_a = 42.8\)\(U_b = 25.2\)\(r = U_b/U_a = 0.6\)\(X\)\(Z\)\(Y\)\(XZ\)\(Y = 0\)\(X=-10\)\(U_{\infty}\)\(\delta\)\(\delta_1\)\(\theta\)\(H\)\(Re_{\theta}\)\(u'/U_{\inft…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case035-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case035-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case035-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Low Reynolds Number Turbulent Flow Near Wakes

Sample Data Plots

The plots below show the profiles of mean streamwise velocity, and the \(\overline{u^2}\)
and \(\overline{uv}\) Reynolds stress components, at a selection of downstream locations for 
both the symmetric and asymmetric wake cases.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case035&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case035</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case035&amp;rev=1690371289&amp;do=diff</link>
        <description>Low Reynolds Number Turbulent Flow Near Wakes

Experiment by Gough and Hancock

----------

Description

Measurements have been made in two low-Reynolds number wakes, one symmetrical and one
asymmetrical with a boundary layer thickness ratio of 1.9. \(U_e\theta/\nu)^3\)\(\theta\)\(U_e\)\((U_e\theta/\nu)\)\(t\)\(\delta\)\(U_e\theta/\nu = 600\)\(u_{\tau}\)\(k\)\(\overline{uv}\)\(u'\)\(x=301\)\(x=302\)\(x=303\)\(x=304\)\(x=305\)\(x=306\)\(x=308\)\(x=310\)\(x=315\)\(x=320\)\(x=340\)\(x=380\)\(x=400\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case036-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case036-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case036-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Couette Flow with Plane Fixed Wall

Sample Data Plots

The plots below show the developed mean velocity and Reynolds stress profiles of the fully Poiseuille 
flow case (no moving wall), and the three cases with a moving wall. The moving wall cases are data
from Station 5.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case036&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case036</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case036&amp;rev=1690371289&amp;do=diff</link>
        <description>Couette Flow with Plane Fixed Wall

Experiments by Corenflos,  Rida, Monnier, Dupont, Dang Tran, Stanislas

----------

Description

Flow in a channel, between a plane fixed wall and a plane moving wall as shown in . 
The distance between the two walls is \(h = 2\delta = 29.7\)\(L = 1.38\)\(\partial U/\partial y\)\(\nu = 1.5 \times 10^5\)\(U_w\)\(U_q\)\(u_{\tau f}\)\(u_{\tau m}\)\(Re_q = U_qh/\nu\)\(Re_w = U_wh/\nu\)\(U_w\)\(u_{\tau m}\)\(u_{\tau f}\)\(x=0\)\(x = -0.235\)\(U/U_q\)\(V/U_q\)\(W/U_…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case037&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case037</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case037&amp;rev=1690371289&amp;do=diff</link>
        <description>Pulsed Channel Flow

Experiments by Tardu, Binder, Feng, Vezin, Blackwelder

----------

Description

Tardu et al (1994) report measurements in turbulent channel flow with forced oscillations 
covering a range of frequencies (\(\omega^+ = 0.03-0.0005\)) and amplitudes (10-70 % of 
centreline velocity). Phase averages of the velocity (\(&lt;u&gt;\)\(&lt;\tau&gt;\)\(&lt;u'u'&gt;\)\(&lt;\tau'\tau'&gt;\)\(2.5l_v\)\(\overline{U}_c = 17.5\)\(\tau\)\(l_s=\sqrt(2\nu/\omega)\)\(\omega=2\pi f\)\(l_s^+=l_s \overline{u}_{\tau}/\nu…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case038-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case038-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case038-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Circular Air Jet

Sample Data Plots

The plots below show profiles of mean and rms velocity, and Reynolds shear stress, across the jet
at a selection of streamwise locations. Quantities are normalized with the local jet centreline velocity
and halfwidth.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case038&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case038</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case038&amp;rev=1690371289&amp;do=diff</link>
        <description>Circular Air Jet

Experiments by Anselmet and Fulachier

----------

Description

The aim of these experiments is to investigate the development of 
turbulent axisymmetric jets in the near field region, close to the nozzle exit. A vertical
axisymmetric turbulent jet emitted from a fully developed pipe flow, weakly confined in
coflowing air, is investigated. Special attention is paid to the near-field region,
\(x/D_j \le 20\)\(Mj\)\(D_j= 26\)\(D_e\)\(U_e \approx 1\)\(285 \times 285\)\(110 D_j\)\(…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case039-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case039-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case039-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Rotating Homogeneous Turbulence in Axisymmetric Contraction

Sample Data Plots

The plots below show the mean velocity, strain rate and rotation along the duct, together with the 
development of the Reynolds stress anisotropies (\(a_{ij}=\overline{u_iu_j}/k - 2/3\delta_{ij}\))
and turbulent kinetic energy.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case039&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case039</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case039&amp;rev=1690371289&amp;do=diff</link>
        <description>Rotating Homogeneous Turbulence in Axisymmetric Contraction

Experiment by Leuchter and Dupeuble

----------

Description

This investigation was carried out by the authors to investigate the effects of rotation on
homogeneous anisotropic turbulence by superimposing solid-body rotation on axisymmetric 
contraction.\(\Omega_o\)\(D\)\(U_o\)\(U_1 = CU_o\)\(C\)\[ R(\xi) = R_o/(1+\beta\xi)^{1/2} \]\(R(\xi)\)\(\xi = x/L\)\(R_o = R(0)\)\(L\)\(\beta = DL/U_o\)\(\beta = C - 1\)\(C\)\(D=24\)\(D=48\)\(\Ome…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case040-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case040-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case040-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Plane Wake Near a Swept Wing

Sample Data Plots

The plots below show mean velocity vectors in the \(x\)-\(z\) plane, contours of the mean \(V\)
velocity and contours of the turbulent kinetic energy at a selection of \(y\) locations.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case040&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case040</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case040&amp;rev=1690371289&amp;do=diff</link>
        <description>Plane Wake Near a Swept Wing

Experiments by Pailhas and Jayaraman

----------

Description

Measurements were taken in the wake in the vicinity of a wing-body junction, with a
symmetric airfoil at an angle of incidence of 15o, and sweep angle of 22o\(Re_{chord} = 500,000\)\(x\)\(z\)\(y\)\(y\)\(y=10\)\(y=20\)\(y=30\)\(y=40\)\(y=50\)\(y=60\)\(y=70\)\(y=80\)\(y=90\)\(y=100\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case041-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case041-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case041-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow around Surface-Mounted Cubical Obstacle

Sample Data Plots

The plot below shows mean velocity vectors on the geometry centreline.



The plots below show profiles of the mean \(U\) velocity, and Reynolds stress components
at selected locations along the geometry centreline.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case041&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case041</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case041&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow around Surface-Mounted Cubical Obstacle

Experiments by Martinuzzi and Tropea

----------

Description

The flow field around a surface-mounted cube has been investigated, using LDA
measurement techniques.
The experiments were performed in a fully developed channel flow, so that the
incoming flow conditions are well-defined. The Reynolds number, based on the height of the 
channel, is around \(8\times 10^4\)\(l \times w \times h\)\(H=h/2\)\(U\)\(V\)\(W\)\(\overline{u^2}\)\(\overline{v^2}\)\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case042-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case042-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case042-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flows over 3D and 2D Hills

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity, rms velocities and Reynolds shear stress
at three locations along the flat plate.



The plots below show profiles of the mean \(U\) velocity, rms \(u'\) velocity and Reynolds shear stress
at selected streamwise locations in the axisymmetric hill and 2D ridge cases.\(\chi=CU_{\infty}h^2/Q\)\(Q\)\(\chi=CU_{\infty}h^2/Q\)\(Q\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case042&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case042</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case042&amp;rev=1690371289&amp;do=diff</link>
        <description>Flows over 3D and 2D Hills

Experiments by Thompson and Lawson

----------

Description

A wind tunnel study was conducted to examine the flowfield and the ground-level 
scalar concentrations from a variety of scalar source positions (locations and heights) both 
upstream and downstream of two model hills, an axisymmetric hill (maximum slope 24\[ f(r) = \frac{h+c}{1+(r/L)^4} - c  \]\(r\)\(h = 155\)\(L = 388\)\(c = 10\)\(r \le 775\)\(r &gt; 775\)\(f(r)=0\)\(- a &lt; \xi &lt; a\)\[ x = (1/2) \xi \left( 1 +…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case043-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case043-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case043-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Vortex Shedding Past Square Cylinder

Sample Data Plots

The plot below shows mean velocity vectors of the flow around the cylinder.



The plots below show profiles of the time-averaged mean \(U\) velocity and Reynolds stress components
at selected streamwise locations.\(U\)\(V\)\(y\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case043&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case043</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case043&amp;rev=1690371289&amp;do=diff</link>
        <description>Vortex Shedding Past Square Cylinder

Experiment by Lyn and Rodi

----------

Description

Ensemble-averaged statistics at constant phase of the turbulent near-wake flow 
(Reynolds number = 21400) around a square cylinder have been obtained from two-component
laser-Doppler measurements.\(Re\)\(-0.5 \leq x/H \le 8\)\(0 \leq y/H \leq 2.5\)\(H = 4\)\(H\)\(U\)\(U = 0.535\)\(U\)\(U\)\(H\)\(Re = 21400\)\(f\)\(St = f H/U = 0.132 \pm 0.004\)\(O(10^4)\)\(x/H = 8\)\(x/H = -3\)\(y/H = 2\)\(y/H = 2.5\)\(y/H…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case044-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case044-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case044-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>2D Channel Flow with/without Scalar Transport

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity and Reynolds stress components
across the channel.



The plots below show profiles of the mean scalar, turbulent scalar fluxes, and rms
scalar fluctuations across the channel.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case044&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case044</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case044&amp;rev=1690371289&amp;do=diff</link>
        <description>2D Channel Flow with/without Scalar Transport

DNS by Horiuti

----------

Description

The flow field is a fully developed two-dimensional turbulent flow between two parallel flat 
plates as shown in .  
Passive scalar transport is calculated, with the scalar being uniformly input
within the fluid and then removed at both walls.  Wall temperatures (the scalar) at the two 
plates are set equal.\(Re_{\delta} = 3245\)\(Re_{\tau} = 180\)\(Pr = 0.7\)\(x\)\(z\)\(y\)\(12.8\delta\)\(x\)\(6.4\delta\)\(z…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case045-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case045-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case045-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>2D Channel Flow with/without Thermal Field

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity and Reynolds stress components
for the \(Re_{\tau}=100\) case.



The plots below show profiles of the mean \(U\) velocity and Reynolds stress components
for the \(Re_{\tau}=150\)\(Re_{\tau}=150\)\(Pr=0.71\)\(Re_{\tau}=150\)\(Pr=0.0.25\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case045&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case045</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case045&amp;rev=1690371289&amp;do=diff</link>
        <description>2D Channel Flow with/without Thermal Field

DNS by Kasagi, Tomita, Kuroda, Ohtsubo

----------

Description

The cases here consist of DNS studies of fully developed plane channel flow, as shown in
. The dynamic field is reported at two Reynolds numbers (\(Re_{\tau}=100\)\(150\)\(Re_{\tau}\)\(Re_{bulk}\)\(Pr\)\(y\)\(\delta\)\(y = 0\)\(2\)\(Re\)\(u_{\tau}\)\(\delta\)\(Re_{bulk}\)\(v\)\(\omega_y\)\(x\)\(z\)\(Re_{\tau}=150\)\(5\pi\delta\)\(2\pi\delta\)\(x\)\(z\)\(128 \times 128\)\(\Delta x^+ \appro…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case046-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case046-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case046-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Couette Flow with Plane Fixed Wall

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity and Reynolds stress components
for case CP1.



The plots below show profiles of the mean \(U\) velocity and Reynolds stress components
for case CP2.\(U\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case046&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case046</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case046&amp;rev=1690371289&amp;do=diff</link>
        <description>Couette Flow with Plane Fixed Wall

Direct Numerical Simulations by Kuroda, Kasagi, Hirata

----------

Flow Description

Couette-Poiseuille flow in a channel, between a plane fixed wall and a plane moving wall. 
The mean shear rate on one wall is varied by changing the relative wall velocities and the
streamwise pressure gradient, allowing the turbulence statistics and structures under different
wall shear rates to be investigated.\(U_w\)\(\nu = 1.5 \times 10^{-5}\)\(U_w\)\(U_q\)\(U_{\tau f}\)\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case047-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case047-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case047-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Homogeneous Isotropic Flow with/without Mean Temperature Gradient

Sample Data Plots

The plots below show the development in time of the Reynolds stresses, turbulent heat flux
and temperature variance.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case047&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case047</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case047&amp;rev=1690371289&amp;do=diff</link>
        <description>Homogeneous Isotropic Flow with/without Mean Temperature Gradient

Simulation by Iida and Kasagi

----------

Description

Direct numerical simulation (DNS) of homogeneous decaying, almost isotropic, turbulence with a 
mean temperature gradient imposed in one direction was carried out by using a spectral method. 
Each term in the budget equations of the Reynolds stresses and turbulent heat flux were 
calculated, together with turbulence spectra and lengthscales.\(L = 2\pi\)\(\nu=1/300\)\(Pr = 0.…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case048-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case048-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case048-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Homogeneous Isotropic Turbulence Decay of Passive Scalar Fluctuations

Sample Data Plots

The plots below show the decay in time of the turbulent kinetic energy and temperature variance.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case048&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case048</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case048&amp;rev=1690371289&amp;do=diff</link>
        <description>Homogeneous Isotropic Turbulence Decay of Passive Scalar Fluctuations

DNS by Miyauchi and Ishizu

----------

Description

Decay of temperature fluctuations in isotropic decaying turbulence was investigated by
performing direct numerical simulations using a spectral method. Temperature was treated
as a passive scalar, thus, it has no effect on the velocity field. Two cases are reported;
for Prandtl numbers \(Pr=0.2\)\(0.71\)\[ \nabla \cdot u = 0 \]\[ \frac{\partial u}{\partial t} = u\times \ome…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case049-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case049-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case049-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Homogeneous Turbulent Shear Flow

Sample Data Plots

The plots below show the development in non-dimensional time of the Reynolds stress 
ratios \(\overline{u_iu_j}/k\), the turbulent kinetic energy and the production
to dissipation ratio \(P_k/\varepsilon\).</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case049&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case049</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case049&amp;rev=1690371289&amp;do=diff</link>
        <description>Homogeneous Turbulent Shear Flows

Direct Numerical Simulation by Matsumoto, Nagano and Tsuji

----------

Description

A sheared homogeneous turbulent field  is simulated, as shown schematically in
.  The mean flow  is imposed in  
the \(x\)-direction  and is sheared in the \(y\)\(S\)\(Sk_o/\varepsilon_o\)\(St=14\)\(2\pi \times 2\pi \times 2\pi\)\(64\times 64\times 64\)\(x\)\(y\)\(z\)\(E(k)= 8.417\times 10^{-3}k^2\)\(k \le 11\)\(E(k)= 8.417\times 10^{-3}\times (11^{11/3})k^{-5/3}\)\(11 \le k \l…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case050-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case050-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case050-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Boundary Layer on the Verge of Separation

Sample Data Plots

The plots below show the development in the streamwise direction of the skin friction,
\(C_f\), pressure coefficient, \(C_p\), and boundary layer shape factor, \(H_{12}\).



The plots below show profiles of the mean streamwise velocity \(U\)\(\overline{u^2}\)\(\overline{uv}\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case050&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case050</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case050&amp;rev=1690371289&amp;do=diff</link>
        <description>Boundary Layer on the Verge of Separation

Experiments by Dengel and Fernholz

----------

Description

The data characterises the behaviour of boundary layers in the vicinity of separation. 
Three similar flows are studied, each with slightly different pressure distributions resulting 
in finite regions of small, constant, but different skin frictions: case 1, approximately zero; 
case 2, slightly positive (\(C_f \approx 0.0001\)\(C_f \approx -0.0001\)\(Re = 10^6\)\(u_d\)\(x\)\(C_p\)\(C_f\)\(U\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case051-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case051-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case051-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Boundary Layer in a S-Shaped Channel

Sample Data Plots

The plot below shows contours of the wall surface pressure coefficient
upstream and around the bend section.



The plots below show profiles of the mean velocities and Reynolds stresses
at selected cross-stream locations (\(Z\)\(X\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case051&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case051</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case051&amp;rev=1690371289&amp;do=diff</link>
        <description>Boundary Layer in a S-Shaped Channel

Experiments by Truong and Brunet

----------

Description

The experiment was conducted with the purpose of studying a pressure gradient driven three-dimensional 
boundary layer, to provide a comprehensive data base to examine critically different 
turbulence models. 
There are a number of ways to produce a three-dimensional boundary layer: e.g. by using appropriate 
curved walls to generate a transverse pressure gradient, by arranging for a local transverse…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case052-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case052-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case052-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Duct Flows with Smooth and Rough Walls

Sample Data Plots

The plots below show secondary flow vectors across the two ducts. (Making use of symmetries, a 
quarter of the square duct is shown, and half of the rectangular one).



The plots below show contours of mean streamwise velocity and rms streamwise velocity
fluctuations in the two ducts.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case052&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case052</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case052&amp;rev=1690371289&amp;do=diff</link>
        <description>Duct Flows with Smooth and Rough Walls

Experiments by Fujita, Hirota, Yokosawa, Hasegawa, Gotoh and Nagata

----------

Description

Experimental data is presented for fully developed turbulent flow in square and rectangular ducts
with combinations of smooth and roughened walls. Two configurations are included here, as shown in
\(6.5\times 10^4\)\(U_1\)\(U_2\)\(U_3\)\(\overline{u_2u_2}\)\(\overline{u_3u_3}\)\(\overline{u_1u_2}\)\(\overline{u_1u_3}\)\(U\)\(V\)\(W\)\(u'\)\(v'\)\(w'\)\(overline{u_…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case053-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case053-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case053-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Backward-Facing Inclined Step

Sample Data Plots

The plots below show streamlines for a selection of step angles and channel expansion ratios,
at Reynolds number of \(Re_H=15000\).



The plots below show profiles of the mean and rms streamwise velocity at
selected streamwise locations for the channel expansion ratio of \(1.48\)\(Re_H=47000\)\(90^o\)\(1.48\)\(Re_H=47000\)\(25^o\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case053&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case053</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case053&amp;rev=1690371289&amp;do=diff</link>
        <description>Backward-Facing Inclined Step

Experiments by Ruck and Makiola

----------

Description

The case considered is of flow over an inclined backward-facing step, as shown in
. 

&lt;[Flow configuration]Flow configuration&gt;

A number of cases have been considered, with step expansion angles of \(\alpha=10^o\),
\(15^o\), \(20^o\)\(25^o\)\(30^o\)\(45^o\)\(90^o\)\(h_2/h_1=1.48\)\(2\)\(3.27\)\(Re_H\)\(ER=2\)\(40H\)\(ER\)\(\alpha\)\(x\)\(x\)\(ER\)\(\alpha\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case054-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case054-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case054-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Upslope and Vertical Convective Boundary Layer

Sample Data Plots

The plots below show profiles of the mean velocity and temperature for both slope angles
at selected times during the simulation, demonstrating that an essentially steady state 
situation is arrived at.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case054&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case054</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case054&amp;rev=1690371289&amp;do=diff</link>
        <description>Upslope and Vertical Convective Boundary Layer

Large Eddy Simulation by Schumann

----------

Description

Large-eddy simulation has been used to determine the turbulent structure of the steady-state up-slope
boundary layer (UBL) which forms at a uniformly heated inclined or vertical plane surface below a 
stratified atmosphere at rest. The configuration is shown in \(\alpha\)\(\rho\)\(d\theta/dz'\)\(\beta\)\(z_o\)\(Q_s\)\(N=(g \beta\, d\theta/dz')^{1/2}\)\(v^*\)\(H\)\(\theta^*\)\[ v^*= (\beta …</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case055-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case055-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case055-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>2D Plane Turbulent Wall Jet

Sample Data Plots

The plots below show the streamwise development of the jet maximum velocity, the
wall skin friction coefficient, and the jet halfwidth.



The plots below show profiles of the normalized mean velocity, rms velocities and Reynolds
shear stress at a selection of streamwise locations. Quantities are normalized with
the local jet halfwidth and maximum velocity.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case055&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case055</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case055&amp;rev=1690371289&amp;do=diff</link>
        <description>2D Plane Turbulent Wall Jet

Experiments by Karlsson, Eriksson, Persson

----------

Description

Laser-Doppler measurements were conducted in a plane turbulent wall jet at a Reynolds
number based on inlet velocity, \(Re_o\), of 9600. The initial development, as well
as the fully developed flow, was studied. Special attention was given to the near-wall
region, including the use of small measuring volumes and the application of specific
near-wall data corrections, so that wall shear stresses were…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case056-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case056-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case056-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Backward-Facing Step with Uniform Normal Bleed

Sample Data Plots

The plots below show the wall static pressure coefficient distribution for
the \(U_o=20\) and \(60\) m/s cases.



The plot below shows the normalized reattachment length for all cases.



The plots below show profiles of the normalized mean velocity, turbulence intensity and Reynolds
shear stress at a selection of streamwise locations for the \(U_o=20\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case056&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case056</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case056&amp;rev=1690371289&amp;do=diff</link>
        <description>Backward-Facing Step with Uniform Normal Bleed

Experiments by Yang, Tsai, Tsai

----------

Description

The case examines the effect of normal mass bleed into the separated-reattaching flow behind a 
back-ward-facing step, for a geometry shown in .\(Re = U_oH/\nu = 1.91 \times 10^4\)\(3.82\times 10^4\)\(5.74 \times 10^4\)\(U_o = 20\)\(40\)\(60\)\(Q = 0\)\(180\)\(360\)\(540\)\(U_oH/\nu\)\(1.91\times 10^4\)\(3.82\times 10^4\)\(5.74 \times 10^4\)\(V_s\)\(Q\)\(0.6 H\)\(U_o = 20\)\(X_r\)\(0.05 H\)\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case057-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case057-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case057-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>3-Dimensional Boundary Layer Generated by a Spinning Body

Sample Data Plots

The plots below show the wall skin friction coefficients \(C_{fx}\) and
\(C_{fz}\) for three spin ratios in the C cases.



The plot below shows the pressure coefficient distribution for various adverse
pressure gradient cases.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case057&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case057</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case057&amp;rev=1690371289&amp;do=diff</link>
        <description>3-Dimensional Boundary Layer Generated by a Spinning Body

Experiments by Driver and Johnston

----------

Description

Experimental data are given for a three-dimensional, shear-driven, turbulent boundary
layer subjected to sudden transverse strain. Measurements made with a three-component laser Doppler 
velocimeter include all components of mean flow, turbulent Reynolds stresses, and triple-product correlations.\(0.31 \times 0.31\)\(U_e\)\(W_s\)\(U_e = 30\)\(W_s= 0\)\(30\)\(W_s=U_e = 30\)\(U_e…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case058-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case058-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case058-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Pipe Constriction

Sample Data Plots

The plots below show profiles of streamwise velocity, rms velocity fluctuations, and
Reynolds shear stress at selected streamwise locations for the \(L/d=1\) case.



The plots below show profiles of streamwise velocity, rms velocity fluctuations, and
Reynolds shear stress at selected streamwise locations for the \(L/d=0.04\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case058&amp;rev=1758027587&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2025-09-16T12:59:47+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case058</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case058&amp;rev=1758027587&amp;do=diff</link>
        <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>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case059-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case059-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case059-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Swirling Mixing Layer

Sample Data Plots

The plots below show profiles of streamwise velocity, Reynolds stress components
\(\overline{u^2}\) and \(\overline{uv}\), and swirl velocity at selected streamwise
locations for the three cases.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case059&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case059</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case059&amp;rev=1690371289&amp;do=diff</link>
        <description>Swirling Mixing Layer

Experiments by Mehta, Wood and Clausen

----------

Description

An experimental study has been conducted to investigate the effects of swirl on the streamwise development 
of an axisymmetric turbulent mixing layer. The flow geometry is shown in \(S=0\)\(0.2\)\(0.4\)\(S = W_{max}/U_o = 0\)\(0.2\)\(0.4\)\(Re_{exit} =U_oR/\nu = 130,000\)\(R = 130\)\(X/R = 0.19\)\(4.62\)\(X = 25\)\(600\)\(\Omega = 0\)\(28.8\)\(57.6\)\(S = 0\)\(0.2\)\(0.4\)\(S = W_{max}/U_o\)\(W\)\(U_o\)\(G_{\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case060-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case060-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case060-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Swirling Boundary Layer in a Conical Diffuser

Sample Data Plots

The plots below show profiles of streamwise and swirl velocity components, and
some of the Reynolds stress components, at selected \(x\) locations along the diffuser.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case060&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case060</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case060&amp;rev=1690371289&amp;do=diff</link>
        <description>Swirling Boundary Layer in a Conical Diffuser

Experiments by Clausen, Koh and Wood

----------

Description

The flow examined is a swirling boundary layer developing in a conical diffuser. The geometry is shown
in . The conical diffuser is placed 100 mm downstream of a rotating swirl generator of 
diameter \(D=260\)\(X=510\)\(\nu = 1.5 \times 10^{-5}\)\(x = -25\)\(U_o = 11.6\)\(U_oD/\nu = 202,000\)\(x = -25\)\(75\)\(25\)\(W_{max}/U_o = 0.59\)\(W_{max}\)\(\tau_{wx}/U_o^2 = 0.00282\)\(x\)\(\tau_…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case061-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case061-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case061-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Wake of a Streamwise Axially Rotating Cylinder

Sample Data Plots

The plots below show circumferential profiles of the mean velocities and Reynolds stresses
at four radial locations (\(r=0.1\), \(0.08\), \0.06\) and \(0.04\) m) in the \(S^*=0.57\)
case at \(x=0.394\) m downstream of the cylinder.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case061&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case061</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case061&amp;rev=1690371289&amp;do=diff</link>
        <description>Wake of a Streamwise Axially Rotating Cylinder

Experiments by Wood, Peterson and Clausen

----------

Description

Measurements are given in the turbulent wake of a circular cylinder mounted with its
axis normal to the free-stream velocity, and rotating about an axis parallel
to the streamwise direction, as shown in \(d\)\(39 &lt; x/d &lt; 79\)\(S = \Omega r/U_o\)\(U_o\)\(S\)\(U_o\)\(U\)\(u'\)\(U\)\(U_o\)\(r\)\(x\)\(S^*\)\(S\)\(r=0.1\)\(S^*\)\(U_o\)\(\Omega\)\(r = 0.1\)\(r = 0.08\)\(0.06\)\(0.04\)\(r…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case062-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case062-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case062-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Developing Flow in a Curved Rectangular Duct

Sample Data Plots

The plot below shows the wall pressure coefficient on the symmetry plane along the
inner and outer walls of the duct.



The plots below show the skin friction coefficient around the duct walls at the
five measurement locations (U1, U2, 15, 45, 75, D1 and D2).\(U\)\(z\)\(U\)\(W\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case062&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case062</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case062&amp;rev=1690371289&amp;do=diff</link>
        <description>Developing Flow in a Curved Rectangular Duct

Experiments by Kim and Patel

----------

Description

The flow considered is a developing turbulent flow in a 90 deg. curved duct of rectangular 
cross-section. As shown in  there is an initial 2D wind tunnel
constriction, resulting in a rectangular duct cross-section of width \(H=20.3\)\(6H\)\(7.5H\)\(25.5H\)\(R_i=3H\)\(R_o=4H\)\(4.5H\)\(0.5H\)\(15^o\)\(45^o\)\(75^o\)\(0.5H\)\(4.5H\)\(\nu = 1.45 \times 10^{-5}\)\(U1\)\(x = -4.5H\)\(U_o = 16\)\(U_oH…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case063-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case063-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case063-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Wing-Body Junction Flow

Sample Data Plots

The plots below show profiles of the mean \(U\), \(W\) and \(V\) velocities at a
selection of the LDV measurement locations.



The plots below show profiles of the Reynolds stresses at the same LDV measurement locations.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case063&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case063</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case063&amp;rev=1690371289&amp;do=diff</link>
        <description>Wing-Body Junction Flow

Experiments by Ölçmen and Simpson

----------

Description

A three dimensional, pressure driven turbulent boundary layer created by a wing-body 
junction flow was experimentally studied. The geometry is shown in .

&lt;[ Flow geometry]Flow geometry&gt;

The wing used was a 3:2, semi-elliptical nosed NACA 0020 tailed symmetric profile which has
a chord length of 30.5 cm (12 in.), maximum thickness of 7.17 cm (2.824 in.), and height of
22.9 cm (9.016 in.). The wing was mounted …</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case064-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case064-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case064-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow Approaching a Wall-Mounted Cylinder

Sample Data Plots

The plots below show profiles of the mean velocities at a selection of the measurement locations.



The plots below show profiles of the Reynolds stresses at the same measurement locations.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case064&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case064</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case064&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow Approaching a Wall-Mounted Cylinder

Experiments by Dechow and Felsch

----------

Description

The data is from experiments that were carried out in a three-dimensional incompressible 
turbulent boundary layer growing in front of a cylinder standing on a flat wall in a wind 
tunnel (see \(x\)\(U\)\(U_s\)\(\gamma\)\(\sqrt{\overline{u_s^2}}\)\(\beta\)\(y\)\(U_s\)\(y = 0.2\)\(x\)\(z\)\(x\)\(z\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case065-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case065-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case065-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Turning Flow Over a Flat Plate

Sample Data Plots

The plots below show profiles of the mean velocities at a selection of the measurement stations.



The plots below show profiles of the Reynolds stresses at the same measurement locations.



The plot below shows measured \(C_p\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case065&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case065</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case065&amp;rev=1690371289&amp;do=diff</link>
        <description>Turning Flow Over A Flat Plate

Experiment by Müller

----------

Description

This test case was performed in order to study the steady incompressible,
three-dimensional turbulent boundary layer approaching separation. Turning vanes were used
to deflect the flow field external to the boundary layer laterally so that streamwise flow
deceleration occurred simultaneously with cross-flow acceleration (see \(Re=1.95 \times 10^6\)\(y\)\(\pm \Delta \beta = 45^o\)\(X_m\)\(Y_m\)\(Z_m\)\(y = 0.1\)\(U_m\)…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case066-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case066-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case066-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Strained Flow over a Streamwise Axially Rotating Cylinder

Sample Data Plots

The plots below show profiles of the mean velocities at a selection of the measurement stations
for the low Reynolds number cases.



The plots below show profiles of the Reynolds stresses at a selection of measurement locations
for the high Reynolds number case with cylinder rotation.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case066&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case066</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case066&amp;rev=1690371289&amp;do=diff</link>
        <description>Strained Flow over a Streamwise Axially Rotating Cylinder

Experiments by Bissonnette and Mellor

----------

Description

Mean velocity and mean turbulent field measurements are performed for the case of a
three-dimensional turbulent boundary layer on an axially rotated cylinder, as shown in
\(U_e\)\(W_o\)\(U_e\)\(Re\)\(W_o\)\(\Omega\)\(=W_o/U_e\)\(U\)\(W\)\(\Omega = 0\)\(\Omega=1.8\)\(\Omega=0\)\(\Omega=0.936\)\(\overline{u^2}\)\(\overline{w^2}\)\(\overline{uw}\)\(\overline{v^2}\)\(\overline{u…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case067-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case067-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case067-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow along a Streamwise Axially Rotating Cylinder

Sample Data Plots

The plots below show profiles of the mean \(U\) and \(W\) velocities, and Reynolds normal
stresses, at the six measurement stations.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case067&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case067</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case067&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow along a Streamwise Axially Rotating Cylinder

Experiments by Lohmann

----------

Description

The data represent the results of an experimental investigation of the
three-dimensional turbulent boundary layer formed when an initially collateral boundary
layer encounters local transverse motion of the bounding surface The flow field was
generated by permitting the collateral boundary layer to develop on the surface of a
cylindrical body with an external flow parallel to its axis and with a r…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case068-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case068-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case068-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Near-Wake Flow of a V-gutter with Slit Bleed

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity and Reynolds shear stress
at selected streamwise locations for the 2 mm and 4 mm gutter slit cases.



The plots below show profiles of the rms fluctuating velocities \(u'\)\(v'\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case068&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case068</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case068&amp;rev=1690371289&amp;do=diff</link>
        <description>Near-Wake Flow of a V-gutter with Slit Bleed

Experiments by Yang and Tsai

----------

Description

The cold-flow characteristics of a v-shape flame holder with flow bleed from a slit
located at the leading edge (as shown in ) have been investigated. 
A nonsymmetric wake structure is
developed behind the symmetric slit v-gutter. The flow through the slit induces greater
reverse flow and greater back pressure in the near wake. It also provokes more extensive
transport across the shear layers and…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case069-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case069-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case069-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow over Isolated 2D Hill

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity and Reynolds shear stress
at selected streamwise locations for the three hill geometries.



The plots below show profiles of the rms fluctuating velocities \(u'\)\(w'\)\(a/H=3\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case069&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case069</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case069&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow over Isolated 2D Hill

Experiments by Snyder, Khurshudyan and Nekrasov

----------

Description

The case is flow over an isolated 2D hill in a neutral boundary layer, as shown schematically 
in . The free-stream velocity \(U_{\infty} = 4\) m/s. Three hill geometries
are considered, each with hill height \(H = 0.117\)\(a/H\)\(|\xi| \le a\)\[ x(\xi) = 0.5\xi \left[ 1 + \frac{a^2}{\xi^2 + m^2 (a^2 - \xi^2)} \right]  \]\[ z(\xi) = 0.5m (a^2 - \xi^2)^{1/2} \left[ 1 - \frac{a^2}{\xi^2 + m^2(a^2 …</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case070-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case070-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case070-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow over Isolated 2D Valley

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity and Reynolds shear stress
at selected streamwise locations for the three valley geometries.



The plots below show profiles of the rms fluctuating velocities \(u'\)\(w'\)\(a/H=3\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case070&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case070</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case070&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow over Isolated 2D Valley

Experiments by Khurshudyan, Snyder, Nekrasov, Lawson, Thompson and Schiermeier

----------

Description

The case consists of flow over an isolated 2D valley in a neutral boundary layer, as shown
schematically in . The free-stream velocity \(U_{\infty} = 4\)\(H = 0.117\)\(a/H\)\(|\xi| \le a\)\[ x(\xi) = 0.5\xi \left[ 1 + \frac{a^2}{\xi^2 + m^2 (a^2 - \xi^2)} \right]  \]\[ z(\xi) = -0.5m (a^2 - \xi^2)^{1/2} \left[ 1 - \frac{a^2}{\xi^2 + m^2(a^2 - \xi^2)} \right] \]\(…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case071-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case071-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case071-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Turbulent Plane Couette Flow

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity and Reynolds stress components
across half the channel.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case071&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case071</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case071&amp;rev=1690371289&amp;do=diff</link>
        <description>Turbulent Plane Couette Flow

DNS by Bech, Tillmark, Alfredsson and Andersson

----------

Description

The turbulent structure in plane Couette flow at low Reynolds number is studied using
data obtained from Direct Numerical Simulation. The geometry is shown in \(Re=U_wh/\nu\)\(L_x\)\(L_z\)\(L_z/h = 4\pi\)\(Re_{\tau}\)\(N_1\times N_2 \times N_3\)\(L_x/h\)\(L_z/h\)\(\Delta x\)\(\Delta z\)\(\Delta y\)\( 256 \times 70 \times 256\)\( 10\pi\)\(4\pi\)\(64 \times 32 \times 64\)\(256 \times 70 \times 2…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case072-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case072-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case072-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Turbulent Pipe Flow with Swirl

Sample Data Plots

The plots below show profiles of the mean \(U\) and \(W\) velocities across the pipe
at selected streamwise locations for the two Concentrated Vortex cases.



The plots below show profiles of the Reynolds stresses across the pipe at 
selected streamwise locations for the Concentrated Vortex case at \(Re=500,000\)\(U\)\(W\)\(Re=500,000\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case072&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case072</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case072&amp;rev=1690371289&amp;do=diff</link>
        <description>Turbulent Pipe Flow with Swirl

Experiments by Steenbergen

----------

Description

Water flows along a straight pipe are considered with two types of swirl: “wall jet” (WJ hereafter) 
and “concentrated vortex” (CV hereafter), as shown in . 
These names are based on the initial conditions of the measurement series.\(D=70\)\(Re_D=50,000\)\(300,000\)\(D=70\)\(x/D\)\(R\)\(D\)\(U\)\(W\)\(V\)\(Re_D\)\(x/D\)\(x/D=4.3\)\(Re_D=50,000\)\(x/D=55.2\)\(Re=50,000\)\(Re=300,000\)\(x/D=4.3\)\(x/D=7.7\)\(x/D=1…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case073-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case073-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case073-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flat Plate Transitional Boundary Layer

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity, rms velocities
\(u'\),\(v'\), \(w'\) and Reynolds shear stress \(\overline{uv}\) at
four \(x\) locations along the plate.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case073&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case073</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case073&amp;rev=1690371289&amp;do=diff</link>
        <description>Flat Plate Transitional Boundary Layer

LES by Yang and Voke

----------

Description

The case consists of a flat-plate transitional 2D boundary layer flow without pressure gradient, and
with no temperature variations.

Free-stream velocity: \(U_o=9.6\) m/s.

\(Tu_o=5.0\)\[ \nu_s = (\Delta c_s)^2 \sqrt{2s_{ij}s_{ij}}    \qquad \nu_e = \nu_s - (2\nu/n)[ 1 - \exp(-n\nu_s/(2\nu)]  \]\(c_s=0.1\)\(n=9\)\(Re_x = 6620\)\(200000\)\(L_x^+ = 10138\)\(L_z = 20\)\(L_z^+ = 676\)\(L_y = 30\)\(L_y^+ = 1014\)\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case074-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case074-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case074-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Three-Dimensional Boundary Layer and Flow Field Data on an Inclined Prolate Spheroid

Sample Data Plots

The plots below show the variation of surface pressure coefficient along the spheroid
at selected angles around the body for the three cases (\(\phi=0^o\) corresponds to vertically downwards).\(U\)\(U\)\(U\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case074&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case074</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case074&amp;rev=1690371289&amp;do=diff</link>
        <description>Three-Dimensional Boundary Layer and Flow Field Data of an Inclined Prolate Spheroid

H.-P. Kreplin

----------

Description

The wind tunnel model consists of a 6:1 prolate spheroid, as shown in 
and .

Several incidence/Reynolds number combinations have been investigated, and data about
transition in the 3d boundary layer, development of the boundary layers, 3d boundary layer
separation and the separated flow field have been obtained. Measured data are surface
pressures, skin friction, and mea…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case075-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case075-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case075-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow through Axisymmetric Expansions

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity and Reynolds stresses at a selection
of streamwise locations for the 14 degree expansion case.



The plots below show profiles of the mean \(U\) velocity and Reynolds stresses at a selection
of streamwise locations for the 18 degree expansion case.\(U\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case075&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case075</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case075&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow through Axisymmetric Expansions

Experiments by Stieglmeier, Tropea, Weiser, Nitsche

----------

Description

This study examines the flow field in three axisymmetric expansions having diffuser 
half-angles, \(\alpha\), of 14, 18, and 90 degrees, respectively, as shown in \(Re = 1.56 \times 10^4\)\(U\)\(V\)\(W\)\(\overline{u^2}\)\(\overline{v^2}\)\(\overline{w^2}\)\(\overline{uv}\)\(\overline{uw}\)\(D_1= 2 R_1\)\(D_2=2R_2\)\(D_2/D_1\)\(Re = 1.56 \times 10^4\)\(U_o\)\(z\)\(\pm  100\mu\)\(r\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case076-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case076-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case076-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow Over a Wavy Wall

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity, rms velocities, and
Reynolds shear stress, all normalized using the wall friction velocity, at
selected streamwise locations.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case076&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case076</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case076&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow Over a Wavy Wall

Experiment by Hudson, Dykhno and Hanratty

----------

Description

Measurements of the spatial and time variation of two components of the velocity have
been made over a sinusoidal solid wavy boundary (see ) with a height 
to length ratio of \(2\delta/\lambda =0.10\)\(\alpha^+ = (2\pi/\lambda)(\nu/u^*)=0.02\)\(Re_H=U_bH/\nu = 6760\)\(H\)\(U_b\)\(H = 50.8\)\(L_z = 610\)\(\delta = 2.54\)\(\lambda = 50.8\)\(U =120\)\(Re = U_bH/\nu = 6760\)\(0.05\lambda\)\(2\delta/\lambda = 0…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case077-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case077-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case077-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Separated Turbulent Flow Over a Wavy Wall

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity and Reynolds stresses
all normalized using the bulk velocity, at selected streamwise locations.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case077&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case077</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case077&amp;rev=1690371289&amp;do=diff</link>
        <description>Separated Turbulent Flow Over a Wavy Wall

DNS by Maaß and Schumann

----------

Description

The impact of a wavy surface on turbulent flow is investigated by direct numerical simulations. By means of 
finite differences in terrain following coordinates, the method treats the flow in a plane channel with wavy 
lower and flat top surface. Both surfaces are smooth. The lower surface wave amplitude is 0.05 and the 
wavelength is 1 in units of the mean channel height. The Reynolds number in terms o…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case078-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case078-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case078-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow through Staggered Tube Bundle

Sample Data Plots

The plots below show profiles of the mean velocities and Reynolds stresses
across the gaps between tubes at the three \(x\) locations, \(x=0\), \(11\)
and \(16.5\) mm.



The plots below show profiles of the mean velocities and Reynolds normal
stresses across the gaps between tubes at the two \(y\)\(y=0\)\(22.5\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case078&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case078</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case078&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow through Staggered Tube Bundle

Experiments by Simonin and Barcouda

----------

Flow Description

The case is a nominally two-dimensional isothermal flow
through a staggered tube bundle array.

The experimental test section consists of 7 horizontal, staggered rows of rods, as 
shown in \(U\)\(V\)\(\overline{u^2}\)\(\overline{v^2}\)\(\overline{uv}\)\(x=0\)\(11\)\(16.5\)\(y=0\)\(22.5\)\(V_o = 1.06\)\(V_o\)\(U\)\(V\)\(\overline{u^2}\)\(\overline{v^2}\)\(\overline{uv}\)\(x=0\)\(11\)\(16.5\)\(y=…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case079-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case079-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case079-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Turbulent Natural Convection in an Enclosed Tall Cavity

Sample Data Plots

The plots below show profiles of the mean and rms vertical velocity and temperature
across the cavity on the mid-span plane at a selection of heights for the lower
Raleigh number case, \(Ra=0.86\times 10^6\)\(Ra=1.43\times 10^6\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case079&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case079</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case079&amp;rev=1690371289&amp;do=diff</link>
        <description>Turbulent Natural Convection in an Enclosed Tall Cavity

Experiments by Betts and Bokhari

----------

Description

Experiments have been undertaken to investigate the natural convection of air in 
a tall differentially heated rectangular cavity (2.18 m high by 0.076 m wide by 0.52 m 
in depth, shown diagrammatically in the \(0.86\times 10^6\)\(1.43\times 10^6\)\(z=0\)\(y/H\)\(V\)\(v'\)\(U\)\(u'\)\(T\)\(t'\)\(y/H=0.05\)\(y/H=0.10\)\(y/H=0.30\)\(y/H=0.40\)\(y/H=0.50\)\(y/H=0.60\)\(y/H=0.70\)\(y/H…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case080-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case080-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case080-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Steady Flow Past Tube Bundles

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity, and rms \(u'\) and \(v'\)
velocities at a selection of streamwise locations through the tube bundle for the
staggered \(3.6\times 1.6\) case.



The plots below show profiles of the mean \(U\)\(u'\)\(v'\)\(3.6\times 2.1\)\(U\)\(u'\)\(v'\)\(3.6\times 2.1\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case080&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case080</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case080&amp;rev=1690371289&amp;do=diff</link>
        <description>Steady Flow Past Tube Bundles

Experiments by S. Balabani

----------

Flow Configuration

The experiments were carried out in a purpose-designed tunnel with water at 
20oC used as the working fluid. The maximum flowrate was 290 lt/min, 
corresponding to an upstream bulk velocity, \(U_{bulk}\)\(72 \times 72\)\(\mu\)\(\mu\)\(Re_{g,d}\)\(z/d = 0\)\(0.0 \le y/d \le 1.8\)\(x\)\(Re_{g,d}\)\(U\)\(V\)\(u'\)\(v'\)\(x/d\)\(x/d\)\(U\)\(V\)\(u'\)\(v'\)\(x/d\)\(U\)\(V\)\(u'\)\(v'\)\(U\)\(U\)\(V\)\(V\)\(x/d\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case081-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case081-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case081-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow over Periodic Hills

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity, and Reynolds stresses
\(\overline{u^2}\), \(\overline{v^2}\) and \(\overline{uv}\) at selected locations
along the geometry.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case081&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case081</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case081&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow over Periodic Hills

LES by Temmerman and Leschziner

----------

Flow Configuration

Flow over 2D periodic hills, consisting of polynomial-shaped obstacles mounted on a flat plate with a recirculation region in their wake, as shown in .

&lt;[Flow geometry]Periodic hills geometry&gt;

The test case is relevant for studying near-wall or/and subgrid-scale modelling in \(h = 28\)\(L_x = 9h\)\(L_y = 3.035h\)\(U_bh/\nu = 10 595\)\(U_b\)\(h\)\(4.5h\)\(y^+\)\(x=0.22h\)\(x=4.72h\)\(U\)\(V\)\(\overline{u…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case082-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case082-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case082-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow Around a Simplified Car Body (Ahmed Body)

Sample Data Plots

The plots below show profiles of the mean \(U\) velocity at a selection of 
streamwise locations on the symmetry plane \(y=0\).



The plots below show profiles of the mean \(U\) and rms \(u'\) velocities 
over the rear sloping end of the body at a selection of streamwise locations on 
the symmetry plane \(y=0\)\(U\)\(x=0\)\(x=200\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case082&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case082</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case082&amp;rev=1690371289&amp;do=diff</link>
        <description>Flow Around a Simplified Car Body (Ahmed Body)

Experiments by H. Lienhart, S. Becker, C. Stoots

----------

Flow Configuration

The experiments were performed in the LSTM low-speed wind-tunnel, which has a cross
section of 1.87×1.4 m2. The geometry of the Ahmed body is illustrated in \(15 \times 10^{-6}\)\(U_b = 40\)\(h = 288\)\(Re = 768,000\)\(x=0\)\(y=0\)\(z=0\)\(y\)\(y=0\)\(y=200\)\(y=400\)\(x\)\(z\)\(y\)\(z\)\(y=0\)\(x=-178\)\(y=0\)\(x=-138\)\(y=100\)\(x=-88\)\(y=180\)\(x=-38\)\(y=195\)\(x…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case083-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case083-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case083-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Wall-Mounted 2-D Hump with Oscillatory Zero-Mass-Flux Jet or Suction through a Slot

Sample Data Plots

The plot below shows mean wall \(C_p\) profiles for the no-flow-control case, the
suction control case, and time-averaged wall \(C_p\) for the oscillatory control case.\(C_p\)\(U\)\(\overline{u^2}\)\(\overline{v^2}\)\(\overline{uv}\)\(U\)\(\overline{u^2}\)\(\overline{uv}\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case083&amp;rev=1727180754&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2024-09-24T12:25:54+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case083</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case083&amp;rev=1727180754&amp;do=diff</link>
        <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>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case084-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case084-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case084-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Turbulent Boundary Layer Flow Over a Cube

Sample Data Plots

The plots below show profiles from the Small wind tunnel of the mean \(U\)
velocity and Reynolds stresses in the undisturbed boundary layer for a number of 
freestream velocities.



The plots below show profiles of the mean pressure coefficient \(C_p\)\(y=0\)\(C_p\)\(y=0\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case084&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case084</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case084&amp;rev=1690371289&amp;do=diff</link>
        <description>Turbulent Boundary Layer Flow Over a Cube

Wind tunnel experiments by Lim, Castro and Hoxey

----------

Flow Configuration

Field experiments at Silsoe Research Institute and experiments in two wind 
tunnels at the University of Southampton (called 'ST' and 'LT' below) were 
performed.  The general tunnel arrangement is shown in \(h=80\)\(240\)\(h=6\)\(1.86 \times 10^4 &lt; U_h h/\nu &lt; 40.6 \times 10^4\)\(\nu = 15 \times 10^{-6}\)\(U_h\)\(z=h\)\(z_o = 0.09\)\(0.35\)\(8\)\(C_p\)\(C_p'\)\(y/h=0\)\(x…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case085-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case085-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case085-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Turbulent Stokes Boundary Layer

Sample Data Plots

The plots below show profiles of the phase-averaged rms \(u'\), \(v'\) and \(w'\) velocities, and
the shear stress \(\overline{uw}\), across the boundary layer at a selection of phase angles 
through the cycle.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case085&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case085</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case085&amp;rev=1690371289&amp;do=diff</link>
        <description>Turbulent Stokes Boundary Layer

LES by Salon, Armenio and Crise

----------

Description

Large-eddy simulations (LES) are employed to investigate the Stokes boundary layer in the 
turbulent regime. The flow is driven by an harmonic pressure gradient in the x-direction: 
\[ \frac{dP}{dx}(t) = -U_o \omega \cos(\omega t)  \]\(P\)\(U_o\)\(\omega\)\[ Re_{\delta} = \frac{U_o \delta_s}{\nu} \]\(\delta_s = \sqrt{2\nu/\omega}\)\(\nu\)\(Re_{\delta} = 1790\)\(Re_{\delta}\)\(L_x = 50 \delta_s\)\(L_y = 25 …</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case086-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case086-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case086-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Surface Pressure in Normal Triangular Tube Arrays

Sample Data Plots

The plots below show profiles of the mean \(C_p\) distribution around the cylinder for
the \(P/d=1.32\) and \(1.97\) pitch ratio cases, for a selection of inlet velocities
(with zero displacement of the instrumented tube).\(C_p\)\(P/d=1.32\)\(1.97\)\(y/d\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case086&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case086</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case086&amp;rev=1690371289&amp;do=diff</link>
        <description>Surface Pressure in Normal Triangular Tube Arrays

Measurements by Mahon and Meskell

----------

Flow Configuration

The experimental facility consists of a draw-down wind tunnel which has a 
tube array installed in the test section. The test-section is 750mm long with 
a cross-section of 300mm x 300mm. Three tube arrays were investigated in this 
study. The configurations tested were five row, normal triangular tube arrays 
with pitch ratios of 1.32, 1.58 and 1.97 subject to air cross-flow. A …</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case087-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case087-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case087-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Combined Flow and Deflection Measurements of FSI-Induced Oscillation of Two Rigid Structures in Turbulent Flows

Sample Data Plots

The plot below shows the inlet velocity profile, at \(x=-55\) mm.



The plot below show the time-phase trace of the angle of the models through an oscillation period.\(U\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case087&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case087</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case087&amp;rev=1690371289&amp;do=diff</link>
        <description>Combined Flow and Deflection Measurements of FSI-Induced Oscillation of Two Rigid Structures in Turbulent Flows

Experiments by Pereira Gomes and Lienhart

----------

Description

Characterisation of the FSI-induced two-dimensional limit-cycle oscillation (LCO) 
of two rigid structures in pure rotation in uniform flows. The measurements were performed 
in water at a constant flow velocity of 1.07 m/s.\(\rho_{front body}\)\(2828\)\(\rho_{flat plate}\)\(1475\)\(1475\)\(m\)\(33.4\)\(208.9\)\(I_0\)…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case088-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case088-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case088-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Combined Flow and Deformation Measurements of FSI-Induced Oscillation of a Bluff Flexible Structures in Uniform Flows

Sample Data Plots

The plot below shows the inlet velocity profiles for the three cases, at \(x=-55\) mm.



The plots below show the time-phase trace of the angle of the front body of the models through 
an oscillation period (left), and the path mapped out by the trailing edge coordinates during an 
oscillation (right), for all three cases.\(U\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case088&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case088</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case088&amp;rev=1690371289&amp;do=diff</link>
        <description>Combined Flow and Deformation Measurements of FSI-Induced Oscillation of a Bluff Flexible Structure in Uniform Flows

Experiments by Pereira Gomes and Lienhart

----------

Description

Characterisation of the FSI-induced two-dimensional limit-cycle oscillation (LCO) 
of a flexible structure consisting of a bluff front end in uniform flows. The 
measurements were performed for different fluid viscosities and approaching
flow velocities and covered both laminar and turbulent flow regimes. In tota…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case089-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case089-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case089-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Torque Scaling in Taylor-Couette Flow

Sample Data Plots

The plot below shows profiles of the circumferential angular velocity for a range of
different inner and outer cylinder rotation rates (\(Re_1\) and \(Re_2\)).



The plot below shows profiles of the non-dimensional circumferential angular velocity 
(\(\omega/\Omega_1\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case089&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case089</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case089&amp;rev=1690371289&amp;do=diff</link>
        <description>Torque Scaling in Taylor-Couette Flow

Experiments by Merbold, Fischer and Egbers

----------

Description

The turbulent flow between two concentric cylinders of radii \(R_1\), \(R_2\) and 
length \(L\), which are rotating independently with the angular velocities \(\Omega_1\)
and \(\Omega_2\)\(\eta = R_2/R_1\)\(\Gamma = L/(R_2 - R_1) = L/d\)\(\mu = \Omega_2/\Omega_1\)\(Re_{1,2} = R_{1,2} \Omega_{1,2} d/\nu\)\(\nu\)\(\omega\)\(\omega\)\(T\)\(R_2 = 70 \pm 0.02\)\(R_1 = 35\)\(\eta = 0.5\)\(\Gamma…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case090-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case090-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case090-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Viscous Boundary Layers in Turbulent Rayleigh-Bénard Convection

Sample Data Plots

The plots below show profiles of the mean and rms wall-parallel velocity,
and rms wall-normal velocity, on the cylinder centreline, from the experimental
measurements and \(Ra=3\times 10^9\)\(3\times 10^{10}\)\(Ra\)</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case090&amp;rev=1716805524&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2024-05-27T10:25:24+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case090</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case090&amp;rev=1716805524&amp;do=diff</link>
        <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>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case091-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case091-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case091-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Thermal Boundary Layers in Turbulent Rayleigh-Bénard Convection at Aspect Ratios Between 1 and 9

Sample Data Plots

The plots below show profiles of the mean and rms non-dimensional temperature
on the cylinder centreline, near the cold and heated walls, for a selection
of aspect ratios and Rayleigh numbers.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case091&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case091</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case091&amp;rev=1690371289&amp;do=diff</link>
        <description>Thermal Boundary Layers in Turbulent Rayleigh-Bénard Convection at Aspect Ratios Between 1 and 9

Experiments by du Puits, Resagk and Thess

----------

Description

Highly resolved temperature measurements are reported in turbulent
Rayleigh-Bénard convection in air at a fixed Prandtl number \(Pr = \nu/k = 0.7\)\(\nu\)\(k\)\(\Gamma = D/H\)\(D\)\(H\)\(\Gamma = 1\)\(T_h = 31.2\)\(58.2^o\)\(T_c = 28.8\)\(12.4^o\)\(\Gamma = 1.13\)\(9.00\)\(Ra = (\beta g \Delta \theta H^3)/(\nu k) = 10^{12}\)\(\beta\…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case092-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case092-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case092-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Measurements and Numerical Determination in Differentially Rotating Wide Gap Taylor-Couette Flow

Sample Data Plots

The plots below show experimental measurements of the quasi-Nusselt number vs shear Reynolds
number, for a range of rotation ratios (left), and the quasi-Nusselt number vs rotation ratio
for a selection of shear Reynolds numbers (right).</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case092&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case092</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case092&amp;rev=1690371289&amp;do=diff</link>
        <description>Measurements and Numerical Determination in Differentially Rotating Wide Gap Taylor-Couette Flow

Experiments and DNS by Merbold, Brauckmann and Egbers

----------

Description

Turbulent Taylor-Couette flow with independently rotating cylinders and radius ratio \(\eta = R_2 / R_1 = 0.5\)\(\Gamma = L / (R_2 - R_1) = L / d\)\(L\)\(d\)\(\mu = \Omega_2/ \Omega_1\)\(Re_{1,2} = R_{1,2} \Omega_{1,2} d /\nu\)\(\nu\)\(Re_S = 2 |Re_1 - \eta Re_2 | / (1+\eta) = 2 R_1 R_2 d |\Omega_2 - \Omega_1| / (R_1+R_2…</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case093-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case093-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case093-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>The CoLaPipe-The New Cottbus Large Pipe Test Facility at Brandenburg University of Technology Cottbus-Senftenberg

Sample Data Plots

The plot below shows mean velocity profiles at the inlet of the pipe (without any tripping) for a range of bulk Reynolds numbers.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case093&amp;rev=1715983483&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2024-05-17T22:04:43+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case093</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case093&amp;rev=1715983483&amp;do=diff</link>
        <description>The CoLaPipe-The New Cottbus Large Pipe Test Facility at Brandenburg University of Technology Cottbus-Senftenberg

Experiments by König, Zanoun, Öngüner and Egbers

----------

Description

The CoLaPipe is a novel test facility at the Department of Aerodynamics and Fluid Mechanics, Brandenburg 
University of Technology Cottbus-Senftenberg (BTU Cottbus-Senftenberg), set up to investigate fully 
developed pipe flow at high Reynolds numbers (\(Re_m \le 1.5 \times 10^6\)\(Re_m\)\(L/D = 148\)\(L/D = …</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case094-plots&amp;rev=1690371289&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2023-07-26T11:34:49+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case094-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case094-plots&amp;rev=1690371289&amp;do=diff</link>
        <description>Local and Time-Resolved Wall Heat Flux in Turbulent Rayleigh-Bénard Convection

Sample Data Plots

The plots below show sections of the Nusselt number time series at the two measurement
stations for a selection of Rayleigh numbers.</description>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case094&amp;rev=1716805661&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2024-05-27T10:27:41+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case094</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case094&amp;rev=1716805661&amp;do=diff</link>
        <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>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case095-plots&amp;rev=1716023716&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2024-05-18T09:15:16+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case095-plots</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case095-plots&amp;rev=1716023716&amp;do=diff</link>
        <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>
    </item>
    <item rdf:about="http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case095&amp;rev=1716805754&amp;do=diff">
        <dc:format>text/html</dc:format>
        <dc:date>2024-05-27T10:29:14+00:00</dc:date>
        <dc:creator>Anonymous (anonymous@undisclosed.example.com)</dc:creator>
        <title>case095</title>
        <link>http://cfd.mace.manchester.ac.uk/ercoftac/doku.php?id=cases:case095&amp;rev=1716805754&amp;do=diff</link>
        <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>
    </item>
</rdf:RDF>
