Commit 9644296d authored by William D. Fullmer's avatar William D. Fullmer
Browse files

gallery - add cluster video

parent e588c6b7

docs/webroot/gallery.html

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        <header class="major">

          <h2>Dilute Riser Flow</h2>

          <p>Falling clusters in the near-wall region</p>

        </header>

        <div class="row 50% uniform">

          <div class="8u 12u(small)">

            Circulating fluidized beds (CFBs) span a wide range of operating ranges throughout 

            their subsystems. The riser section is typically characterized by dilute transport. 

            Here, a 1.8 m section (~9M particles) of a pilot-scale CFB riser at 

            <a href="https://psri.org">PSRI</a> is modeled, just 1/10th of the physical 

            system's length. As high speed (15 m/s) gas flow drives the verically, denser than 

            average (1%) regions can form at (or migrate to) the wall and actually fall against 

            the mean flow. This phenomena can be observed on the right in the video while a 

            streamer climbes slowly on the left. We note that the domain is too small as the 

            streamer has interacted with its periodic image. Future work will simulate the full 

            18 m lenght of the riser. 

            Simulated by MFiX-Exa develop (git hash ef171c9d) using 24 GPUs on NETL's Joule2 HPC.

            The animation rendered with <a href="https://www.blender.org">Blender</a>.

            <p><p>



            Animation courtesy of Justin Weber &amp; William D. Fullmer,

            <a href="https://mfix.netl.doe.gov">NETL</a>, Morgantown WV.



            </p>

          </div>

          <div class="4u$ 12u(small)">

            <center>

              <iframe src="https://widgets.figshare.com/articles/11861577/embed?show_title=0" 

               width="250" height="310" allowfullscreen="true" frameborder="0"></iframe>

            </center>

          </div>

        </div>

        <p>





        <header class="major">

          <h2>Boyce Single Bubble</h2>

          <p>Qualitative Benchmarking: Single bubble injection</p>
@@ -85,8 +120,7 @@ END TEMPLATE--> 
            <p><p>



            Animation courtesy William D. Fullmer,

            <a href="https://mfix.netl.doe.gov">Multiphase Flow Science Group</a>,

            NETL, Morgantown WV.

            <a href="https://mfix.netl.doe.gov">NETL</a>, Morgantown WV.



            </p>

          </div>
@@ -110,8 +144,7 @@ END TEMPLATE--> 
            <p><p>



            Animation courtesy of William D. Fullmer,

            <a href="https://mfix.netl.doe.gov">Multiphase Flow Science Group</a>,

            NETL, Morgantown WV.

            <a href="https://mfix.netl.doe.gov">NETL</a>, Morgantown WV.



            </p>

          </div>
@@ -147,8 +180,7 @@ END TEMPLATE--> 
            <p><p>



            Animation courtesy of Justin Weber &amp; William D. Fullmer, 

            <a href="https://mfix.netl.doe.gov">Multiphase Flow Science Group</a>, 

            NETL, Morgantown WV. 

            <a href="https://mfix.netl.doe.gov">NETL</a>, Morgantown WV.



            </p>

          </div>
@@ -173,8 +205,7 @@ END TEMPLATE--> 
            <p><p>



            Animation courtesy of William D. Fullmer,

            <a href="https://mfix.netl.doe.gov">Multiphase Flow Science Group</a>,

            NETL, Morgantown WV.

            <a href="https://mfix.netl.doe.gov">NETL</a>, Morgantown WV.



            </p>

          </div>