


{"id":292987,"date":"2023-07-13T19:18:04","date_gmt":"2023-07-13T19:18:04","guid":{"rendered":"\/forum\/forums\/topic\/gas-liquid-mass-transfer-source-term-co2-transfer-from-gas-to-liquid-water\/"},"modified":"2023-07-14T06:40:10","modified_gmt":"2023-07-14T06:40:10","slug":"gas-liquid-mass-transfer-source-term-co2-transfer-from-gas-to-liquid-water","status":"closed","type":"topic","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/topic\/gas-liquid-mass-transfer-source-term-co2-transfer-from-gas-to-liquid-water\/","title":{"rendered":"Gas-Liquid Mass Transfer Source Term (CO2 transfer from gas to Liquid water)"},"content":{"rendered":"<p>Dear Experts,<\/p>\n<p>Your help is needed <em>again<\/em> to clearify a doubt in unit of source term of gas-liquid mass transfer. Requesting your attention.<\/p>\n<p><strong>\/*****Problem description*****\/&nbsp; &nbsp; &nbsp; &nbsp; &nbsp; &nbsp;<\/strong><\/p>\n<p><strong>Transfer of CO2 from gas mixture (CO2+O2+N2) to liquid mixture (CO2+H2O).&nbsp;<\/strong><\/p>\n<p>Species transport equation in multiphase flow (ref. fluent theory guide)<\/p>\n<p><a class=\"wp-colorbox-image cboxElement\" href=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/13-07-2023-1689273849-mceclip0.png\"><img decoding=\"async\" src=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/13-07-2023-1689273849-mceclip0.png\"><\/a><\/p>\n<p><strong>Unit of first term in this equation<\/strong>&nbsp;<\/p>\n<p>&nbsp;<a class=\"wp-colorbox-image cboxElement\" href=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/13-07-2023-1689274057-mceclip4.png\"><img decoding=\"async\" src=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/13-07-2023-1689274057-mceclip4.png\"><\/a><\/p>\n<p>Therefore, Unit for every term in the species transport equation should be the same, i.e., <em>mass of the transferring species per unit cell volume per unit time<\/em><\/p>\n<p><strong>Now, Let&#8217;s look at the last term: From the literature it has the following form using Henry&#8217;s law:<\/strong><\/p>\n<p><a class=\"wp-colorbox-image cboxElement\" href=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/14-07-2023-1689312367-mceclip3.png\"><img decoding=\"async\" src=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/14-07-2023-1689312367-mceclip3.png\"><\/a><\/p>\n<p>In this&nbsp;<strong><em>k<\/em><\/strong> is mass transfer coefficient (m\/s),&nbsp;<strong><em>a<\/em><\/strong> is area density (1\/m) and&nbsp;<strong><em>He<\/em><\/strong> is unit less Henry&#8217;s constant.<\/p>\n<p>Therefore, the unit of mass transfer rate term can be computed as:<\/p>\n<p><a class=\"wp-colorbox-image cboxElement\" href=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/14-07-2023-1689312314-mceclip2.png\"><img decoding=\"async\" src=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/14-07-2023-1689312314-mceclip2.png\"><\/a><\/p>\n<p>Which is similar to&nbsp;<\/p>\n<p><a class=\"wp-colorbox-image cboxElement\" href=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/13-07-2023-1689274614-mceclip10.png\"><img decoding=\"async\" src=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/13-07-2023-1689274614-mceclip10.png\"><\/a><\/p>\n<p><strong>My doubt<\/strong>&#8211; Unit of mass transfer rate, calculated in this way, is not simiilar to the unit of first term. In first term denominator has &#8220;cell volume&#8221; while in mass transfer rate &#8220;phase volume&#8221; appears in the denominator.&nbsp;<\/p>\n<p><strong>Question:<\/strong> Can anyone tell me if the mass transfer rate calculated from the above formula is correct. Or should it involve phase volume fraction also ? For example, it should have a form like&nbsp;<\/p>\n<p><a class=\"wp-colorbox-image cboxElement\" href=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/14-07-2023-1689312275-mceclip1.png\"><img decoding=\"async\" src=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/14-07-2023-1689312275-mceclip1.png\"><\/a><\/p>\n<p><img decoding=\"async\" src=\"\/forum\/wp-content\/uploads\/sites\/2\/2023\/07\/14-07-2023-1689316798-mceclip0.png\"><\/p>\n<p>I have written the following two code line in the <strong>DEFINE_MASS_TRANSFER<\/strong> udf&nbsp;<\/p>\n<p><strong>According to formula-1-&gt;<\/strong>&nbsp; &nbsp;<\/p>\n<p>k*a*(He*C_R(cell,gas)*C_YI(cell,gas,0)-C_R(cell,liq)*C_YI(cell,liq,0));<\/p>\n<p><strong>According to formula-2-&gt;<\/strong> &nbsp;<\/p>\n<p>k*a*(He*C_R(cell,gas)*C_YI(cell,gas,0)*C_VOF(cell,gas)-C_R(cell,liq)*C_YI(cell,liq,0)*C_VOF(cell,liq));<\/p>\n<p><strong>Kindly suggest which of the above code will give me correct gas-liquid mass transfer rate?<\/strong><\/p>\n","protected":false},"template":"","class_list":["post-292987","topic","type-topic","status-closed","hentry","topic-tag-fluent","topic-tag-Interphasemasstransfer-1","topic-tag-multiphase-eulerian","topic-tag-o2-mass-fraction-1","topic-tag-species-mass-transfer-2"],"aioseo_notices":[],"acf":[],"custom_fields":[{"0":{"_bbp_subscription":["184434","852","199"],"_bbp_author_ip":["23.223.149.206"]," _bbp_last_reply_id":["0"]," _bbp_likes_count":["0"],"_btv_view_count":["1351"],"_edit_lock":["1689316813:69626"],"_bbp_topic_status":["unanswered"],"_bbp_status":["publish"],"_bbp_topic_id":["292987"],"_bbp_forum_id":["27792"],"_bbp_engagement":["199","852","184434"],"_bbp_voice_count":["3"],"_bbp_reply_count":["8"],"_bbp_last_reply_id":["296179"],"_bbp_last_active_id":["296179"],"_bbp_last_active_time":["2023-08-02 18:47:04"]},"test":"kavatar"}],"_links":{"self":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/topics\/292987","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\/292987\/revisions"}],"wp:attachment":[{"href":"https:\/\/innovationspace.ansys.com\/forum\/wp-json\/wp\/v2\/media?parent=292987"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}