{"id":403760,"date":"2025-01-06T16:51:08","date_gmt":"2025-01-06T16:51:08","guid":{"rendered":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/403760\/"},"modified":"2025-01-06T16:51:08","modified_gmt":"2025-01-06T16:51:08","slug":"403760","status":"publish","type":"reply","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/403760\/","title":{"rendered":"Reply To: HET_RXN_RATE UDF"},"content":{"rendered":"<p>&lt;p&gt;That should be phase 0.&nbsp;&lt;\/p&gt;&lt;p&gt;Once you&#8217;ve got that working you may find getting the phase transfer to be an issue as you&#8217;re likely not going to have a clean interface between liquid and gas. You may need to switch to Mixture or Eulerian multiphase models.&nbsp;&lt;\/p&gt;<\/p>\n","protected":false},"template":"","class_list":["post-403760","reply","type-reply","status-publish","hentry"],"aioseo_notices":[],"acf":[],"_links":{"self":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/replies\/403760","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":0,"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/replies\/403760\/revisions"}],"wp:attachment":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/media?parent=403760"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}