{"id":285930,"date":"2023-05-26T11:19:14","date_gmt":"2023-05-26T11:19:14","guid":{"rendered":"\/forum\/forums\/topic\/steady-state-multiphase-simulation\/"},"modified":"2023-05-26T11:19:14","modified_gmt":"2023-05-26T11:19:14","slug":"steady-state-multiphase-simulation","status":"closed","type":"topic","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/topic\/steady-state-multiphase-simulation\/","title":{"rendered":"Steady State Multiphase Simulation"},"content":{"rendered":"<p>Hello,<\/p>\n<p>I am trying to model a multiphase flow with a n2 gas as a fluid and particle droplets as dense discrete particles with no continuous phase interation. The model has three inlets for the n2 gas (and inlet 1 injects the dense particles). I want to study the steady state distribution of the phases on the oultet at the bottom. When I simulate the multiphase flow, and plot the velocity magnitude of phase 1, I notice that the velocity magnitude does not reach the outlet at the bottom. I would expect the fluid phase to focus onto the outlet at the bottom, and would expect the dense particles to follow. Instead the dense particles begin to diverge out of the constricting point. Any help on the model\/model setup would be greatly appreciated<img decoding=\"async\" title=\"Steady state flow of n2 gas (Eulerian) of full model\" src=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/05\/26-05-2023-1685099741-Screenshot 2023-05-25 at 3.29.55 PM.png\" alt=\"steady state flow of full model\"><img decoding=\"async\" title=\"Steady state flow of n2 gas zoomed in at nozzle output\" src=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/05\/26-05-2023-1685099820-Screenshot 2023-05-25 at 3.29.38 PM.png\" alt=\"steady state flow of n2 gas zoomed in at nozzle\"><img decoding=\"async\" title=\"Steady state particle pathlines diverging\" src=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/05\/26-05-2023-1685099851-Screenshot 2023-05-25 at 3.31.30 PM.png\" alt=\"particle distribution\"><\/p>\n","protected":false},"template":"","class_list":["post-285930","topic","type-topic","status-closed","hentry","topic-tag-fluent-ansys-1","topic-tag-dpm","topic-tag-multiphase-eulerian"],"aioseo_notices":[],"acf":[],"custom_fields":[{"0":{"_bbp_subscription":["2382","199"],"_bbp_author_ip":["23.39.172.22"]," _bbp_last_reply_id":["0"]," _bbp_likes_count":["0"],"_btv_view_count":["1105"],"_bbp_topic_status":["unanswered"],"_bbp_status":["publish"],"_bbp_topic_id":["285930"],"_bbp_forum_id":["27792"],"_bbp_engagement":["199","2382"],"_bbp_voice_count":["2"],"_bbp_reply_count":["9"],"_bbp_last_reply_id":["287079"],"_bbp_last_active_id":["287079"],"_bbp_last_active_time":["2023-06-05 08:35:52"]},"test":"aayushyaandrew-cmu-edu"}],"_links":{"self":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/topics\/285930","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\/285930\/revisions"}],"wp:attachment":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/media?parent=285930"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}