{"id":251907,"date":"2023-02-28T11:56:54","date_gmt":"2023-02-28T11:56:54","guid":{"rendered":"\/forum\/forums\/reply\/251907\/"},"modified":"2023-02-28T11:56:54","modified_gmt":"2023-02-28T11:56:54","slug":"251907","status":"publish","type":"reply","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/251907\/","title":{"rendered":"Reply To: Initialization Error &#8211; Droplet Evaporation"},"content":{"rendered":"<p>&lt;p&gt;Hello Rob,&lt;\/p&gt;&lt;p&gt;I&#8217;m having UDM in my UDF but it doesn&#8217;t give me any value since the case is not even getting initialized. Can you have a good look at my UDF and let me know where I&#8217;m wrong? Also, I&#8217;m trying to run this in parallel with 4 processors. I&#8217;m sharing my actual code here.&lt;\/p&gt;&lt;p&gt;Also, is there a way that my udf is causing a cell or value or something similar that doesn&#8217;t exist is getting written to and Fluent then crashes?&lt;span style=&#8221;font-size: 11.0pt; font-family: &#8216;Calibri&#8217;,sans-serif; mso-ascii-theme-font: minor-latin; mso-fareast-font-family: &#8216;Times New Roman&#8217;; mso-hansi-theme-font: minor-latin; mso-bidi-font-family: &#8216;Times New Roman&#8217;; mso-bidi-theme-font: minor-bidi; mso-ansi-language: EN-US; mso-fareast-language: EN-US; mso-bidi-language: AR-SA;&#8221;&gt;? &lt;\/span&gt;&nbsp;&lt;\/p&gt;&lt;div&gt;&lt;div&gt;\/********************************************************&lt;\/div&gt;&lt;div&gt;&nbsp;DEFINITION OF MASS SOURCE TERM FOR LIQUID PHASE&lt;\/div&gt;&lt;div&gt;&nbsp;*******************************************************\/&lt;\/div&gt;&lt;br&gt;&lt;div&gt;DEFINE_SOURCE(liq_src, c, t, ds, eqn)&lt;\/div&gt;&lt;div&gt;{&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;#if !RP_Host&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;real m_dot_l, T_sat;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;real vol = C_VOLUME(c, t); &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; \/\/SIGNIFIES THE CELL VOLUME FOR A CELL AND THREAD&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;Thread *pt = THREAD_SUB_THREAD(t, 0); &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp;\/\/PRIMARY PHASE THREAD&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;Thread *st = THREAD_SUB_THREAD(t, 1); &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp;\/\/SECONDARY PHASE THREAD&lt;\/div&gt;&lt;br&gt;&lt;div&gt;&nbsp; &nbsp;if (C_VOF(c, t) &lt; 0.99 &amp;&amp; C_VOF(c, t) &gt; 0.01)&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;{&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; if (C_T(c,pt) &gt;= T_sat)&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; {&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; m_dot_l = -0.1 * C_VOF(c,t) * C_R(c,t) * fabs(C_T(c,t) &#8211; T_sat) \/ T_sat; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp;\/\/LEE EVAPORATION MODEL&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; ds[eqn] = -0.1 * C_R(c,t) * fabs(C_T(c,t) &#8211; T_sat) \/ T_sat;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; }&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; else&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; {&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; m_dot_l = 0.1 * C_VOF(c,st) * C_R(c,st) * fabs(T_sat &#8211; C_T(c,pt)) \/ T_sat; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp;\/\/LEE CONDENSATION MODEL&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; ds[eqn] = 0;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; }&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;}&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;else&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;{&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; m_dot_l = 0;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; ds[eqn] = 0;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;}&lt;\/div&gt;&lt;br&gt;&lt;div&gt;&nbsp; &nbsp;C_UDMI(c, t, 9) = m_dot_l;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;return m_dot_l;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; #endif&lt;\/div&gt;&lt;div&gt;}&lt;\/div&gt;&lt;br&gt;&lt;div&gt;\/********************************************************&lt;\/div&gt;&lt;div&gt;&nbsp;DEFINITION OF MASS SOURCE TERM FOR VAPOR PHASE&lt;\/div&gt;&lt;div&gt;&nbsp;*******************************************************\/&lt;\/div&gt;&lt;br&gt;&lt;div&gt;DEFINE_SOURCE(vap_src, c, t, ds,eqn)&lt;\/div&gt;&lt;div&gt;{&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; #if !RP_Host&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;real m_dot_v, T_sat;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;real vol = C_VOLUME(c, t); &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; \/\/SIGNIFIES THE CELL VOLUME FOR A CELL AND THREAD&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;Thread *pt = THREAD_SUB_THREAD(t, 0); &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp;\/\/PRIMARY PHASE THREAD&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;Thread *st = THREAD_SUB_THREAD(t, 1); &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp;\/\/SECONDARY PHASE THREAD&lt;\/div&gt;&lt;br&gt;&lt;div&gt;&nbsp; &nbsp;if (C_VOF(c,t) &lt; 0.99 &amp;&amp; C_VOF(c,t) &gt; 0.01)&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;{&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; if (C_T(c,pt) &gt;= T_sat)&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; {&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; m_dot_v = 0.1 * C_VOF(c,t) * C_R(c,t) * fabs(T_sat &#8211; C_T(c,pt)) \/ T_sat; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; \/\/LEE CONDENSATION MODEL&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; ds[eqn] = 0;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; }&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; else&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; {&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; m_dot_v = -0.1 * C_VOF(c,t) * C_R(c,t) * fabs(T_sat &#8211; C_T(c,pt)) \/ T_sat; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp;\/\/LEE CONDENSATION MODEL&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; ds[eqn] = -0.1 * C_R(c,t) * fabs(T_sat &#8211; C_T(c,t)) \/ T_sat;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; }&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;}&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;else&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;{&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; m_dot_v = 0;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; ds[eqn] = 0;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;}&lt;\/div&gt;&lt;br&gt;&lt;div&gt;&nbsp; &nbsp;C_UDMI(c, t, 10) = m_dot_v;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;return m_dot_v;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; #endif&lt;\/div&gt;&lt;div&gt;}&lt;\/div&gt;&lt;br&gt;&lt;div&gt;\/********************************************************&lt;\/div&gt;&lt;div&gt;&nbsp;DEFINITION OF ENERGY SOURCE TERM FOR BOTH PHASES&lt;\/div&gt;&lt;div&gt;&nbsp;*******************************************************\/&lt;\/div&gt;&lt;br&gt;&lt;div&gt;DEFINE_SOURCE(enrg_src, c, mix_th, ds, eqn)&lt;\/div&gt;&lt;div&gt;{&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; #if !RP_Host&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; real m_dot, T_sat, hfg;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; Thread *pt, *st;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; pt = THREAD_SUB_THREAD(mix_th, 0);&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; st = THREAD_SUB_THREAD(mix_th, 1);&lt;\/div&gt;&lt;br&gt;&lt;div&gt;&nbsp; &nbsp; if (C_VOF(c, pt) &lt; 0.99 &amp;&amp; C_VOF(c, pt) &gt; 0.01)&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; {&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; if (C_T(c, mix_th) &gt;= T_sat)&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; {&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; m_dot = -0.1 * C_VOF(c,pt) * C_R(c,pt) * fabs(C_T(c,pt) &#8211; T_sat) \/ T_sat; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp;\/\/LEE EVAPORATION MODEL&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; ds[eqn] = -0.1 * C_VOF(c,pt) * C_R(c,pt) \/ T_sat;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; }&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; }&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; else&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; {&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; m_dot = 0.1 * C_VOF(c,st) * C_R(c,st) * fabs(T_sat &#8211; C_T(c,mix_th)) \/ T_sat; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp;\/\/LEE CONDENSATION MODEL&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; ds[eqn] = -0.1 * C_VOF(c,st) * C_R(c,st) \/ T_sat;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; }&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; else&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; {&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; m_dot = 0;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; &nbsp; &nbsp; ds[eqn] = 0;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; }&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; C_UDMI(c, t, 11) = m_dot;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; return hfg * m_dot;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp;&lt;\/div&gt;&lt;div&gt;&nbsp; &nbsp; #endif&lt;\/div&gt;&lt;div&gt;}&lt;\/div&gt;&lt;\/div&gt;&lt;p&gt;&nbsp;&lt;\/p&gt;<\/p>\n","protected":false},"template":"","class_list":["post-251907","reply","type-reply","status-publish","hentry"],"aioseo_notices":[],"aioseo_head":"\n\t\t<!-- All in One SEO 4.9.10 - aioseo.com -->\n\t<meta name=\"description\" content=\"Hello Rob,I&#039;m having UDM in my UDF but it doesn&#039;t give me any value since the case is not even getting initialized. Can you have a good look at my UDF and let me know where I&#039;m wrong? Also, I&#039;m trying to run this in parallel with 4 processors. I&#039;m sharing my actual code here.Also,\" \/>\n\t<meta name=\"robots\" content=\"max-image-preview:large\" \/>\n\t<link rel=\"canonical\" href=\"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/251907\/\" \/>\n\t<meta name=\"generator\" content=\"All in One SEO (AIOSEO) 4.9.10\" \/>\n\t\t<meta property=\"og:locale\" content=\"en_US\" \/>\n\t\t<meta property=\"og:site_name\" content=\"Ansys Learning Forum | Ansys Innovation Space\" \/>\n\t\t<meta property=\"og:type\" content=\"article\" \/>\n\t\t<meta property=\"og:title\" content=\"Reply To: Initialization Error \u2013 Droplet Evaporation | Ansys Learning Forum\" \/>\n\t\t<meta property=\"og:description\" content=\"Hello Rob,I&#039;m having UDM in my UDF but it doesn&#039;t give me any value since the case is not even getting initialized. 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Can you have a good look at my UDF and let me know where I'm wrong? Also, I'm trying to run this in parallel with 4 processors. 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Can you have a good look at my UDF and let me know where I'm wrong? Also, I'm trying to run this in parallel with 4 processors. I'm sharing my actual code here.Also,","canonical_url":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/251907\/","robots":"max-image-preview:large","keywords":"","webmasterTools":{"miscellaneous":""},"schema":{"@context":"https:\/\/schema.org","@graph":[{"@type":"BreadcrumbList","@id":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/251907\/#breadcrumblist","itemListElement":[{"@type":"ListItem","@id":"https:\/\/innovationspace.ansys.com\/forum#listItem","position":1,"name":"Home","item":"https:\/\/innovationspace.ansys.com\/forum","nextItem":{"@type":"ListItem","@id":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/251907\/#listItem","name":"Reply To: Initialization Error &#8211; Droplet Evaporation"}},{"@type":"ListItem","@id":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/251907\/#listItem","position":2,"name":"Reply To: Initialization Error &#8211; Droplet Evaporation","previousItem":{"@type":"ListItem","@id":"https:\/\/innovationspace.ansys.com\/forum#listItem","name":"Home"}}]},{"@type":"Organization","@id":"https:\/\/innovationspace.ansys.com\/forum\/#organization","name":"Ansys Learning Forum","description":"Ansys Innovation Space","url":"https:\/\/innovationspace.ansys.com\/forum\/"},{"@type":"WebPage","@id":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/251907\/#webpage","url":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/251907\/","name":"Reply To: Initialization Error \u2013 Droplet Evaporation | Ansys Learning Forum","description":"Hello Rob,I'm having UDM in my UDF but it doesn't give me any value since the case is not even getting initialized. Can you have a good look at my UDF and let me know where I'm wrong? Also, I'm trying to run this in parallel with 4 processors. I'm sharing my actual code here.Also,","inLanguage":"en-US","isPartOf":{"@id":"https:\/\/innovationspace.ansys.com\/forum\/#website"},"breadcrumb":{"@id":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/251907\/#breadcrumblist"},"datePublished":"2023-02-28T11:56:54+00:00","dateModified":"2023-02-28T11:56:54+00:00"},{"@type":"WebSite","@id":"https:\/\/innovationspace.ansys.com\/forum\/#website","url":"https:\/\/innovationspace.ansys.com\/forum\/","name":"Ansys Learning Forum","description":"Ansys Innovation Space","inLanguage":"en-US","publisher":{"@id":"https:\/\/innovationspace.ansys.com\/forum\/#organization"}}]},"og:locale":"en_US","og:site_name":"Ansys Learning Forum | Ansys Innovation Space","og:type":"article","og:title":"Reply To: Initialization Error \u2013 Droplet Evaporation | Ansys Learning Forum","og:description":"Hello Rob,I'm having UDM in my UDF but it doesn't give me any value since the case is not even getting initialized. Can you have a good look at my UDF and let me know where I'm wrong? Also, I'm trying to run this in parallel with 4 processors. I'm sharing my actual code here.Also,","og:url":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/251907\/","article:published_time":"2023-02-28T11:56:54+00:00","article:modified_time":"2023-02-28T11:56:54+00:00","twitter:card":"summary_large_image","twitter:title":"Reply To: Initialization Error \u2013 Droplet Evaporation | Ansys Learning Forum","twitter:description":"Hello Rob,I'm having UDM in my UDF but it doesn't give me any value since the case is not even getting initialized. Can you have a good look at my UDF and let me know where I'm wrong? Also, I'm trying to run this in parallel with 4 processors. I'm sharing my actual code here.Also,"},"aioseo_meta_data":{"post_id":"251907","title":null,"description":null,"keywords":null,"keyphrases":null,"primary_term":null,"canonical_url":null,"og_title":null,"og_description":null,"og_object_type":"default","og_image_type":"content","og_image_url":null,"og_image_width":null,"og_image_height":null,"og_image_custom_url":null,"og_image_custom_fields":null,"og_video":null,"og_custom_url":null,"og_article_section":null,"og_article_tags":null,"twitter_use_og":true,"twitter_card":"default","twitter_image_type":"default","twitter_image_url":null,"twitter_image_custom_url":null,"twitter_image_custom_fields":null,"twitter_title":null,"twitter_description":null,"schema":{"blockGraphs":[],"customGraphs":[],"default":{"data":{"Article":[],"Course":[],"Dataset":[],"FAQPage":[],"Movie":[],"Person":[],"Product":[],"ProductReview":[],"Car":[],"Recipe":[],"Service":[],"SoftwareApplication":[],"WebPage":[]},"graphName":"","isEnabled":true},"graphs":[]},"schema_type":"default","schema_type_options":null,"pillar_content":false,"robots_default":true,"robots_noindex":false,"robots_noarchive":false,"robots_nosnippet":false,"robots_nofollow":false,"robots_noimageindex":false,"robots_noodp":false,"robots_notranslate":false,"robots_max_snippet":null,"robots_max_videopreview":null,"robots_max_imagepreview":"large","priority":null,"frequency":null,"local_seo":null,"limit_modified_date":false,"created":"2024-10-28 18:45:44","updated":"2026-09-07 14:57:41","ai":null,"breadcrumb_settings":null,"seo_analyzer_scan_date":null},"aioseo_breadcrumb":"<div class=\"aioseo-breadcrumbs\"><span class=\"aioseo-breadcrumb\">\n\t\t\t<a href=\"https:\/\/innovationspace.ansys.com\/forum\" title=\"Home\">Home<\/a>\n\t\t<\/span><span class=\"aioseo-breadcrumb-separator\">&raquo;<\/span><span class=\"aioseo-breadcrumb\">\n\t\t\tReply To: Initialization Error \u2013 Droplet Evaporation\n\t\t<\/span><\/div>","aioseo_breadcrumb_json":[{"label":"Home","link":"https:\/\/innovationspace.ansys.com\/forum"},{"label":"Reply To: Initialization Error &#8211; Droplet Evaporation","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/251907\/"}],"acf":[],"_links":{"self":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/replies\/251907","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\/251907\/revisions"}],"wp:attachment":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/media?parent=251907"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}