{"id":366922,"date":"2024-05-15T10:11:47","date_gmt":"2024-05-15T10:11:47","guid":{"rendered":"\/forum\/forums\/topic\/heat-transfer-simulation-with-convection-film-coefficient-as-a-result\/"},"modified":"2024-05-15T10:11:47","modified_gmt":"2024-05-15T10:11:47","slug":"heat-transfer-simulation-with-convection-film-coefficient-as-a-result","status":"closed","type":"topic","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/topic\/heat-transfer-simulation-with-convection-film-coefficient-as-a-result\/","title":{"rendered":"Heat transfer simulation with convection film coefficient as a result"},"content":{"rendered":"<p><span lang=\"EN-US\">I&#8217;m trying to create a Tool in Ansys mechanical using the steady state thermal simulation, with which experimental data can be evaluated. The experiment contains a multiphase Fluid, which flows over a heated steel plate. During the experiments we want to measure the temperature at defined places inside the metal block and calculate the film coefficient from the temperature differences. Since Ansys mechanical needs the film coefficient for a convection boundary condition, I&#8217;m not sure how to implement this problem, due to the desired result being a required boundary condition.<\/span><\/p>\n<p><span lang=\"EN-US\">I&#8217;ve thought about adding a APDL-Command with a surface temperature dependent heat flow (20&deg;C leads to 0W,..,150&deg;C leads to 200W) to emulate a convection. But with this approach the energy balance is not accounted for, which leads to my questions.<\/span><\/p>\n<p><span lang=\"EN-US\">How can I define a temperature dependent heat flow with the condition that the accumulated heat flow is equal to the input heat flow?<\/span><\/p>\n<p><span lang=\"EN-US\">Would the results of this approach be not only qualitatively but also quantifiable accurate?<\/span><\/p>\n<p><span lang=\"EN-US\">Would using Ansys Fluent make the setup of this simulation simpler?<\/span><\/p>\n<p><span lang=\"EN-US\">Attached is a picture of the geometry, where A is the induced heat flow and B is one of the temperature measure points and C is the area over which the fluid is flowing.&nbsp;<\/span><\/p>\n<p><img decoding=\"async\" style=\"font-size: 14pt\" src=\"\/forum\/wp-content\/uploads\/sites\/2\/2024\/05\/15-05-2024-1715767339-Block_T_fix.png\" alt=\"\"><\/p>\n<p>&nbsp;<\/p>\n","protected":false},"template":"","class_list":["post-366922","topic","type-topic","status-closed","hentry","topic-tag-convection-coefficient","topic-tag-fluid-solid-heat-transfer","topic-tag-steady-state-thermal"],"aioseo_notices":[],"acf":[],"custom_fields":[{"0":{"_bbp_subscription":["348860","20905"],"_bbp_author_ip":["184.24.96.207"]," _bbp_last_reply_id":["0"]," _bbp_likes_count":["0"],"_btv_view_count":["619"],"_bbp_topic_status":["unanswered"],"_bbp_topic_id":["366922"],"_bbp_forum_id":["27791"],"_bbp_engagement":["20905","348860"],"_bbp_voice_count":["2"],"_bbp_reply_count":["1"],"_bbp_last_reply_id":["367175"],"_bbp_last_active_id":["367175"],"_bbp_last_active_time":["2024-05-16 14:44:47"]},"test":"jakob-heubnermailbox-tu-dresden-de"}],"_links":{"self":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/topics\/366922","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/topics"}],"about":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/types\/topic"}],"version-history":[{"count":0,"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/topics\/366922\/revisions"}],"wp:attachment":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/media?parent=366922"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}