


{"id":29504,"date":"2018-06-15T23:35:12","date_gmt":"2018-06-15T23:35:12","guid":{"rendered":"\/forum\/forums\/topic\/porous-zone-function\/"},"modified":"2018-06-15T23:35:12","modified_gmt":"2018-06-15T23:35:12","slug":"porous-zone-function","status":"closed","type":"topic","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/topic\/porous-zone-function\/","title":{"rendered":"porous zone function"},"content":{"rendered":"<p><span style=\"color: #000000; font-family: verdana, geneva, lucida, 'lucida grande', arial, helvetica, sans-serif; font-size: 13.3333px; background-color: #f7f7f7;\">In my simulation, I&rsquo;m using Porous Media\/<\/span><span style=\"color: #000000; font-family: verdana, geneva, lucida, 'lucida grande', arial, helvetica, sans-serif; font-size: 13.3333px; background-color: #f7f7f7;\">Non-Equilibrium approach. In estimating the interfacial heat transfer coefficient, I use a correlation of the kind:&nbsp;<\/span><span style=\"color: #000000; font-family: verdana, geneva, lucida, 'lucida grande', arial, helvetica, sans-serif; font-size: 13.3333px; background-color: #f7f7f7;\">hfs=C*(Pr^n)*(Ra^m)*(K\/d) to be input as a user-defined-profile. As it is known, Fluent uses double-cell approach in solving the two energy equations (one for the fluid medium and the other for the solid medium). The fluid medium temperature is recalled as Tf=C_T(c,t), but how to recall the solid medium temperature (Ts) needed in&nbsp;<\/span><span style=\"color: #000000; font-family: verdana, geneva, lucida, 'lucida grande', arial, helvetica, sans-serif; font-size: 13.3333px; background-color: #f7f7f7;\">Rayleigh number . Could anybody help with this?&nbsp;<\/span><span style=\"color: #000000; font-family: verdana, geneva, lucida, 'lucida grande', arial, helvetica, sans-serif; font-size: 13.3333px; background-color: #f7f7f7;\">Thank you in advance.<\/span><\/p>\n","protected":false},"template":"","class_list":["post-29504","topic","type-topic","status-closed","hentry"],"aioseo_notices":[],"acf":[],"custom_fields":[{"0":{"_bbp_old_topic_id":["1673"],"_bbp_old_topic_author_name_id":["Anonymous"],"_bbp_old_is_topic_anonymous_id":["false"],"_bbp_old_closed_status_id":["publish"],"_bbp_author_ip":[null],"_bbp_old_sticky_status_id":["normal"],"_bbp_likes_count":["0","0","0","0","0"],"_btv_view_count":["398"],"_bbp_topic_status":["unanswered"],"_bbp_status":["publish"],"_bbp_topic_id":["29504"],"_bbp_forum_id":["27792"],"_bbp_engagement":["25","157152"],"_bbp_voice_count":["2"],"_bbp_reply_count":["1"],"_bbp_last_reply_id":["59565"],"_bbp_last_active_id":["59565"],"_bbp_last_active_time":["2018-06-17 04:45:43"]},"test":"bruon"}],"_links":{"self":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/topics\/29504","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\/29504\/revisions"}],"wp:attachment":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/media?parent=29504"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}