


{"id":370337,"date":"2024-07-03T14:27:46","date_gmt":"2024-07-03T14:27:46","guid":{"rendered":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/370337\/"},"modified":"2024-07-03T14:27:46","modified_gmt":"2024-07-03T14:27:46","slug":"370337","status":"publish","type":"reply","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/370337\/","title":{"rendered":"Reply To: question on particle deposition with the turbulence dispersion in pipe flow"},"content":{"rendered":"<p>&lt;p&gt;You shouldn&#8217;t need that many integration steps! I think the default is around 50k for a steady model. Otherwise the solver settings look sensible (from a quick look).&nbsp;&lt;\/p&gt;&lt;p&gt;How high is the near wall cell? How does that compare to the droplet diameter? Given the droplet size what mechanism are you expecting to help the droplet penetrate the viscous sub layer?&lt;\/p&gt;<\/p>\n","protected":false},"template":"","class_list":["post-370337","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=\"You shouldn&#039;t need that many integration steps! I think the default is around 50k for a steady model. Otherwise the solver settings look sensible (from a quick look). How high is the near wall cell? How does that compare to the droplet diameter? Given the droplet size what mechanism are you expecting to help the droplet\" \/>\n\t<meta name=\"robots\" content=\"max-image-preview:large\" \/>\n\t<link rel=\"canonical\" href=\"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/370337\/\" \/>\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: question on particle deposition with the turbulence dispersion in pipe flow | Ansys Learning Forum\" \/>\n\t\t<meta property=\"og:description\" content=\"You shouldn&#039;t need that many integration steps! I think the default is around 50k for a steady model. Otherwise the solver settings look sensible (from a quick look). How high is the near wall cell? How does that compare to the droplet diameter? Given the droplet size what mechanism are you expecting to help the droplet\" \/>\n\t\t<meta property=\"og:url\" content=\"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/370337\/\" \/>\n\t\t<meta property=\"article:published_time\" content=\"2024-07-03T14:27:46+00:00\" \/>\n\t\t<meta property=\"article:modified_time\" content=\"2024-07-03T14:27:46+00:00\" \/>\n\t\t<meta name=\"twitter:card\" content=\"summary_large_image\" \/>\n\t\t<meta name=\"twitter:title\" content=\"Reply To: question on particle deposition with the turbulence dispersion in pipe flow | Ansys Learning Forum\" \/>\n\t\t<meta name=\"twitter:description\" content=\"You shouldn&#039;t need that many integration steps! I think the default is around 50k for a steady model. Otherwise the solver settings look sensible (from a quick look). How high is the near wall cell? How does that compare to the droplet diameter? Given the droplet size what mechanism are you expecting to help the droplet\" \/>\n\t\t<script type=\"application\/ld+json\" class=\"aioseo-schema\">\n\t\t\t{\"@context\":\"https:\\\/\\\/schema.org\",\"@graph\":[{\"@type\":\"BreadcrumbList\",\"@id\":\"https:\\\/\\\/innovationspace.ansys.com\\\/forum\\\/forums\\\/reply\\\/370337\\\/#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\\\/370337\\\/#listItem\",\"name\":\"Reply To: question on particle deposition with the turbulence dispersion in pipe flow\"}},{\"@type\":\"ListItem\",\"@id\":\"https:\\\/\\\/innovationspace.ansys.com\\\/forum\\\/forums\\\/reply\\\/370337\\\/#listItem\",\"position\":2,\"name\":\"Reply To: question on particle deposition with the turbulence dispersion in pipe flow\",\"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\\\/370337\\\/#webpage\",\"url\":\"https:\\\/\\\/innovationspace.ansys.com\\\/forum\\\/forums\\\/reply\\\/370337\\\/\",\"name\":\"Reply To: question on particle deposition with the turbulence dispersion in pipe flow | Ansys Learning Forum\",\"description\":\"You shouldn't need that many integration steps! I think the default is around 50k for a steady model. Otherwise the solver settings look sensible (from a quick look). How high is the near wall cell? How does that compare to the droplet diameter? 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I think the default is around 50k for a steady model. Otherwise the solver settings look sensible (from a quick look). How high is the near wall cell? How does that compare to the droplet diameter? Given the droplet size what mechanism are you expecting to help the droplet","canonical_url":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/370337\/","robots":"max-image-preview:large","keywords":"","webmasterTools":{"miscellaneous":""},"schema":{"@context":"https:\/\/schema.org","@graph":[{"@type":"BreadcrumbList","@id":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/370337\/#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\/370337\/#listItem","name":"Reply To: question on particle deposition with the turbulence dispersion in pipe flow"}},{"@type":"ListItem","@id":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/370337\/#listItem","position":2,"name":"Reply To: question on particle deposition with the turbulence dispersion in pipe flow","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\/370337\/#webpage","url":"https:\/\/innovationspace.ansys.com\/forum\/forums\/reply\/370337\/","name":"Reply To: question on particle deposition with the turbulence dispersion in pipe flow | Ansys Learning Forum","description":"You shouldn't need that many integration steps! 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