{"id":367862,"date":"2024-05-21T13:47:46","date_gmt":"2024-05-21T13:47:46","guid":{"rendered":"\/forum\/forums\/reply\/367862\/"},"modified":"2024-05-21T13:50:03","modified_gmt":"2024-05-21T13:50:03","slug":"367862","status":"publish","type":"reply","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/367862\/","title":{"rendered":"Reply To: Divergence detected in AMG solver: pressure correction temperature limited to&#8230;"},"content":{"rendered":"<p>&lt;p&gt;&nbsp;&lt;\/p&gt;&lt;p&gt;I added air as primary phase and, water and vapor as secondary phases. I saw in one of the tutorials online that the reason for including a phase with air is that if only water liquid and vapor are defined, the calculation starts as if there is already water vapor inside the pipe (don&rsquo;t know how true is this?)&nbsp; I used explicit vof formulation. Also, the geometry dimension is in order of micrometer.&nbsp;&nbsp;&lt;\/p&gt;&lt;p&gt;&nbsp;&lt;\/p&gt;<\/p>\n","protected":false},"template":"","class_list":["post-367862","reply","type-reply","status-publish","hentry"],"aioseo_notices":[],"acf":[],"_links":{"self":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/replies\/367862","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/replies"}],"about":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/types\/reply"}],"version-history":[{"count":1,"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/replies\/367862\/revisions"}],"predecessor-version":[{"id":367863,"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/replies\/367862\/revisions\/367863"}],"wp:attachment":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/media?parent=367862"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}