


{"id":162925,"date":"2021-10-08T13:07:44","date_gmt":"2021-10-08T13:07:44","guid":{"rendered":"\/forum\/forums\/topic\/mesh-study-heat-transfer-in-gap-flow\/"},"modified":"2021-10-15T07:38:30","modified_gmt":"2021-10-15T07:38:30","slug":"mesh-study-heat-transfer-in-gap-flow","status":"closed","type":"topic","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/topic\/mesh-study-heat-transfer-in-gap-flow\/","title":{"rendered":"Mesh study heat transfer in gap flow"},"content":{"rendered":"<div class=\"Item-Body\">\n<div class=\"Message userContent\">\n<p>Hello, <\/p>\n<p>I am simulating a 2D gap flow of air. The simulation is steady state, incompressible and the flow is laminar. The domain is 0.1 m long (x-dir) and 0.001 m wide (y-dir). At x=0 there is the inlet with a constant velocity and at x=0.1 m there is the outlet. At y=0 there is a wall and at y=0.001 m there is a symmetry BC. I am adding the energy equation. The temperature at the inlet is fixed with 293.15 K (20 &deg;C) and and the wall it is set to be 283.15 K (10 &deg;C). The mesh I am using has hexahedral nonuniform cells. I started with 300 cells in x-dir and 30 cells in y-dir (in total 9000 cells) and refined the mesh by increasing the amount of cells in both directions.<\/p>\n<p>I now compare the outlet temperature and the mean heat flux density at the wall between the different meshes. The outlet temperature I calculate as a mass flow weighted average at the outlet. For the heat flux density I take the heat transferred at the wall and divide it by the area of the wall interface.<\/p>\n<p>Neither the outlet temperature, nor the mean heat flux density seem to converge to a &quot;constant&quot; value. I increased the amount of cells until I hit 81.000 (900 x 90), which feels very fine to me. Residuals of the simulation are all great (&lt;1e-9). I compared the mean heat flux density to correlations given in the VDI-W&auml;rmeatlas and the absolute value seems to be fine (~ 1 % abbreviation).<\/p>\n<p>Any ideas why the solution does not converge to a &quot;constant&quot; value? Here is a plot of the mean heat flux density in dependency of the amount of cells used:<\/p>\n<div class=\"embedExternal embedImage\">\n<div class=\"embedExternal-content\">\n<a class=\"embedImage-link\" href=\"\/forum\/wp-content\/uploads\/forum-uploads\/475\/1A9XOT96QV82.jpg\" rel=\"nofollow noopener\" target=\"_blank\"><br \/>\n<img decoding=\"async\" class=\"embedImage-img\" src=\"\/forum\/wp-content\/uploads\/forum-uploads\/475\/1A9XOT96QV82.jpg\" alt=\"meanHeatFlowRateFluent.jpg\" \/><br \/>\n<\/a><\/p>\n","protected":false},"template":"","class_list":["post-162925","topic","type-topic","status-closed","hentry","topic-tag-2d","topic-tag-heat-flux","topic-tag-heat-transfer","topic-tag-mesh-refinement"],"aioseo_notices":[],"acf":[],"custom_fields":[{"0":{"_bbp_author_ip":[""],"_bbp_old_reply_author_name_id":["Anonymous"],"_bbp_old_is_reply_anonymous_id":["false"],"_btv_view_count":["590"],"_bbp_likes_count":["0"],"_bbp_subscription":["232426"],"_bbp_topic_status":["unanswered"],"_bbp_status":["publish"],"_bbp_topic_id":["162925"],"_bbp_forum_id":["27792"],"_bbp_engagement":["25","232426"],"_bbp_voice_count":["2"],"_bbp_reply_count":["6"],"_bbp_last_reply_id":["194298"],"_bbp_last_active_id":["194298"],"_bbp_last_active_time":["2021-10-15 07:38:30"]},"test":"felix-hochwallnerait-ac-at"}],"_links":{"self":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/topics\/162925","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\/162925\/revisions"}],"wp:attachment":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/media?parent=162925"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}