{"id":47232,"date":"2019-11-03T17:26:08","date_gmt":"2019-11-03T16:26:08","guid":{"rendered":"https:\/\/www.thermal-engineering.org\/o-que-e-mcadams-thom-correlacao-de-chen-ebulicao-de-nucleados-definicao\/"},"modified":"2020-01-22T17:01:48","modified_gmt":"2020-01-22T16:01:48","slug":"o-que-e-mcadams-thom-correlacao-de-chen-ebulicao-de-nucleados-definicao","status":"publish","type":"post","link":"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-mcadams-thom-correlacao-de-chen-ebulicao-de-nucleados-definicao\/","title":{"rendered":"O que \u00e9 McAdams &#8211; Thom &#8211; Correla\u00e7\u00e3o de Chen &#8211; Ebuli\u00e7\u00e3o de nucleados &#8211; Defini\u00e7\u00e3o"},"content":{"rendered":"<div class=\"su-quote su-quote-style-default\">\n<div class=\"su-quote-inner su-clearfix\">McAdams &#8211; Thom &#8211; Correla\u00e7\u00e3o de Chen &#8211; Ebuli\u00e7\u00e3o Nucleada.\u00a0Essa correla\u00e7\u00e3o pode ser usada para c\u00e1lculos de transfer\u00eancia de calor na ebuli\u00e7\u00e3o do fluxo (ou na ebuli\u00e7\u00e3o por convec\u00e7\u00e3o for\u00e7ada).\u00a0Engenharia T\u00e9rmica<\/div>\n<\/div>\n<div class=\"su-divider su-divider-style-dotted\"><\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<div class=\"su-spacer\"><\/div>\n<h2>Ebuli\u00e7\u00e3o Nucleada &#8211; Ebuli\u00e7\u00e3o por Fluxo<\/h2>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Flow-Boiling-Boiling-Modes.png\"><img loading=\"lazy\" class=\"alignright size-medium wp-image-20784 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Flow-Boiling-Boiling-Modes-117x300.png\" alt=\"Ebuli\u00e7\u00e3o do fluxo - modos de ebuli\u00e7\u00e3o\" width=\"117\" height=\"300\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Flow-Boiling-Boiling-Modes-117x300.png\" \/><\/a>Na\u00a0<strong>ebuli\u00e7\u00e3o do fluxo<\/strong>\u00a0(ou\u00a0<strong>ebuli\u00e7\u00e3o por convec\u00e7\u00e3o for\u00e7ada<\/strong>\u00a0), o fluxo de fluido \u00e9 for\u00e7ado sobre uma superf\u00edcie por meios externos, como uma bomba, bem como por efeitos de flutuabilidade.\u00a0Portanto, a ebuli\u00e7\u00e3o do fluxo \u00e9 sempre acompanhada por outros efeitos de convec\u00e7\u00e3o.\u00a0As condi\u00e7\u00f5es dependem fortemente da geometria, que pode envolver fluxo externo sobre placas e cilindros aquecidos ou fluxo interno (duto).\u00a0Nos reatores nucleares, a maioria dos regimes de ebuli\u00e7\u00e3o \u00e9 apenas fervura de convec\u00e7\u00e3o for\u00e7ada.\u00a0A ebuli\u00e7\u00e3o do fluxo tamb\u00e9m \u00e9 classificada como ebuli\u00e7\u00e3o externa e interna, dependendo de o fluido ser for\u00e7ado a fluir sobre uma superf\u00edcie aquecida ou dentro de um canal aquecido.<\/p>\n<p>A ebuli\u00e7\u00e3o do fluxo interno \u00e9 muito mais complicada por natureza do que a ebuli\u00e7\u00e3o do fluxo externo, porque n\u00e3o h\u00e1 superf\u00edcie livre para o vapor escapar e, portanto, o l\u00edquido e o vapor s\u00e3o for\u00e7ados a fluir juntos.\u00a0O fluxo bif\u00e1sico em um tubo exibe diferentes regimes de ebuli\u00e7\u00e3o do fluxo, dependendo das quantidades relativas das fases l\u00edquida e de vapor.\u00a0Portanto, a ebuli\u00e7\u00e3o por convec\u00e7\u00e3o for\u00e7ada interna \u00e9 comumente referida como\u00a0<strong>fluxo bif\u00e1sico<\/strong>\u00a0.<\/p>\n<\/div>\n<\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<div class=\"su-spacer\"><\/div>\n<h2>Correla\u00e7\u00f5es de ebuli\u00e7\u00e3o de nucleados &#8211; ebuli\u00e7\u00e3o por fluxo<\/h2>\n<\/div>\n<\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<div class=\"su-spacer\"><\/div>\n<h2>Correla\u00e7\u00e3o de McAdams<\/h2>\n<p>Na ebuli\u00e7\u00e3o de nucleados totalmente desenvolvida com refrigerante saturado, a temperatura da parede \u00e9 determinada pelo fluxo de calor e press\u00e3o locais e depende apenas ligeiramente do\u00a0<a title=\"N\u00famero de Reynolds\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/fluid-dynamics\/reynolds-number\/\">n\u00famero de Reynolds<\/a>\u00a0.\u00a0Para \u00e1gua sub-resfriada a press\u00f5es absolutas entre 0,1 &#8211; 0,6 MPa, a\u00a0<strong>correla\u00e7\u00e3o de McAdams<\/strong>\u00a0fornece:<\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nucleate-boiling-McAdams-Correlation.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20789 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nucleate-boiling-McAdams-Correlation.png\" alt=\"ebuli\u00e7\u00e3o nucleada - Correla\u00e7\u00e3o de McAdams\" width=\"453\" height=\"86\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nucleate-boiling-McAdams-Correlation.png\" \/><\/a><\/p>\n<\/div>\n<\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<div class=\"su-spacer\"><\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights  lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<h2><span>Correla\u00e7\u00e3o de Thom<\/span><\/h2>\n<p><span>A\u00a0<\/span><strong><span>correla\u00e7\u00e3o de Thom<\/span><\/strong><span>\u00a0\u00e9 para a ebuli\u00e7\u00e3o do fluxo (sub-resfriado ou saturado a press\u00f5es de at\u00e9 cerca de 20 MPa) sob condi\u00e7\u00f5es em que a contribui\u00e7\u00e3o da ebuli\u00e7\u00e3o nucleada predomina sobre a convec\u00e7\u00e3o for\u00e7ada.\u00a0Essa correla\u00e7\u00e3o \u00e9 \u00fatil para a estimativa aproximada da diferen\u00e7a de temperatura esperada, dado o fluxo de calor:<\/span><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nucleate-boiling-Thom-Correlation.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20790 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nucleate-boiling-Thom-Correlation.png\" alt=\"ebuli\u00e7\u00e3o de nucleados - Correla\u00e7\u00e3o de Thom\" width=\"377\" height=\"147\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nucleate-boiling-Thom-Correlation.png\" \/><\/a><\/p>\n<\/div>\n<\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights  lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<div class=\"su-spacer\"><\/div>\n<h2><span>Correla\u00e7\u00e3o de Chen<\/span><\/h2>\n<p><span>Em 1963,\u00a0<\/span><strong><span>Chen<\/span><\/strong><span>\u00a0prop\u00f4s a primeira correla\u00e7\u00e3o de ebuli\u00e7\u00e3o do fluxo para a evapora\u00e7\u00e3o em tubos verticais, a fim de obter amplo uso.\u00a0<\/span><strong><span>A correla\u00e7\u00e3o de Chen<\/span><\/strong><span>\u00a0inclui os\u00a0<\/span><a title=\"Coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-coeficiente-de-transferencia-de-calor-por-conveccao-definicao\/\"><span>coeficientes de transfer\u00eancia de calor<\/span><\/a><span>\u00a0devido \u00e0\u00a0<\/span><strong><span>ebuli\u00e7\u00e3o dos nucleados<\/span><\/strong><span>\u00a0, bem como os\u00a0<\/span><strong><span>mecanismos convectivos for\u00e7ados<\/span><\/strong><span>.\u00a0Deve-se notar que, em fra\u00e7\u00f5es de vapor mais altas, o coeficiente de transfer\u00eancia de calor varia fortemente com a vaz\u00e3o.\u00a0A velocidade do fluxo em um n\u00facleo pode ser muito alta, causando turbul\u00eancias muito altas.\u00a0Esse mecanismo de transfer\u00eancia de calor foi referido como &#8220;evapora\u00e7\u00e3o for\u00e7ada por convec\u00e7\u00e3o&#8221;.\u00a0Nenhum crit\u00e9rio adequado foi estabelecido para determinar a transi\u00e7\u00e3o da ebuli\u00e7\u00e3o nucleada para a vaporiza\u00e7\u00e3o por convec\u00e7\u00e3o for\u00e7ada.\u00a0No entanto, Chen desenvolveu uma correla\u00e7\u00e3o \u00fanica v\u00e1lida para a ebuli\u00e7\u00e3o nucleada e a vaporiza\u00e7\u00e3o por convec\u00e7\u00e3o for\u00e7ada, para condi\u00e7\u00f5es de ebuli\u00e7\u00e3o saturada e estendida para incluir a ebuli\u00e7\u00e3o sub-resfriada por outros.\u00a0Chen prop\u00f4s uma correla\u00e7\u00e3o em que o coeficiente de transfer\u00eancia de calor \u00e9 a\u00a0<\/span><strong><span>soma<\/span><\/strong><span>\u00a0de um\u00a0componente de\u00a0<\/span><strong><span>convec\u00e7\u00e3o for\u00e7ada<\/span><\/strong><span>\u00a0e uma\u00a0<\/span><strong><span>ebuli\u00e7\u00e3o nucleada<\/span><\/strong><span>componente.\u00a0Deve-se observar que a correla\u00e7\u00e3o de ebuli\u00e7\u00e3o de nucleados de Forster e Zuber (1955) \u00e9 usada para calcular o coeficiente de transfer\u00eancia de calor em ebuli\u00e7\u00e3o de nucleados, h\u00a0<\/span><sub><span>FZ<\/span><\/sub><span>\u00a0e a correla\u00e7\u00e3o de fluxo turbulento de Dittus-Boelter (1930) \u00e9 usada para calcular a fase l\u00edquida coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o, h\u00a0<\/span><sub><span>l<\/span><\/sub><span>\u00a0.<\/span><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Chens-Correlation-Forster-Zuber-and-Dittus-Boelter.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20774 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Chens-Correlation-Forster-Zuber-and-Dittus-Boelter.png\" alt=\"Correla\u00e7\u00e3o de Chens - Forster-Zuber\" width=\"720\" height=\"669\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Chens-Correlation-Forster-Zuber-and-Dittus-Boelter.png\" \/><\/a><\/p>\n<p><span>O fator de supress\u00e3o de ebuli\u00e7\u00e3o dos nucleados, S, \u00e9 a raz\u00e3o entre o superaquecimento efetivo e o superaquecimento da parede.\u00a0\u00c9 respons\u00e1vel pela diminui\u00e7\u00e3o da transfer\u00eancia de calor em ebuli\u00e7\u00e3o porque o superaquecimento efetivo na camada limite \u00e9 menor que o superaquecimento com base na temperatura da parede.\u00a0O multiplicador bif\u00e1sico, F, \u00e9 uma fun\u00e7\u00e3o do par\u00e2metro Martinelli \u03c7\u00a0<\/span><sub><span>tt<\/span><\/sub><span>\u00a0.<\/span><\/p>\n<\/div>\n<\/div>\n<\/div>\n<\/div>\n<p>&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;.<\/p>\n<p>Este artigo \u00e9 baseado na tradu\u00e7\u00e3o autom\u00e1tica do artigo original em ingl\u00eas. Para mais informa\u00e7\u00f5es, consulte o artigo em ingl\u00eas. Voc\u00ea pode nos ajudar. Se voc\u00ea deseja corrigir a tradu\u00e7\u00e3o, envie-a para: translations@nuclear-power.com ou preencha o formul\u00e1rio de tradu\u00e7\u00e3o on-line. Agradecemos sua ajuda, atualizaremos a tradu\u00e7\u00e3o o mais r\u00e1pido poss\u00edvel. Obrigado.<\/p>\n","protected":false},"excerpt":{"rendered":"<p>McAdams &#8211; Thom &#8211; Correla\u00e7\u00e3o de Chen &#8211; Ebuli\u00e7\u00e3o Nucleada.\u00a0Essa correla\u00e7\u00e3o pode ser usada para c\u00e1lculos de transfer\u00eancia de calor na ebuli\u00e7\u00e3o do fluxo (ou na ebuli\u00e7\u00e3o por convec\u00e7\u00e3o for\u00e7ada).\u00a0Engenharia T\u00e9rmica Ebuli\u00e7\u00e3o Nucleada &#8211; Ebuli\u00e7\u00e3o por Fluxo Na\u00a0ebuli\u00e7\u00e3o do fluxo\u00a0(ou\u00a0ebuli\u00e7\u00e3o por convec\u00e7\u00e3o for\u00e7ada\u00a0), o fluxo de fluido \u00e9 for\u00e7ado sobre uma superf\u00edcie por meios externos, &#8230; <a title=\"O que \u00e9 McAdams &#8211; Thom &#8211; Correla\u00e7\u00e3o de Chen &#8211; Ebuli\u00e7\u00e3o de nucleados &#8211; Defini\u00e7\u00e3o\" class=\"read-more\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-mcadams-thom-correlacao-de-chen-ebulicao-de-nucleados-definicao\/\" aria-label=\"More on O que \u00e9 McAdams &#8211; Thom &#8211; Correla\u00e7\u00e3o de Chen &#8211; Ebuli\u00e7\u00e3o de nucleados &#8211; Defini\u00e7\u00e3o\">Ler mais<\/a><\/p>\n","protected":false},"author":1,"featured_media":0,"comment_status":"closed","ping_status":"closed","sticky":false,"template":"","format":"standard","meta":[],"categories":[14],"tags":[],"yoast_head":"<!-- This site is optimized with the Yoast SEO plugin v15.4 - https:\/\/yoast.com\/wordpress\/plugins\/seo\/ -->\n<title>O que \u00e9 McAdams - Thom - Correla\u00e7\u00e3o de Chen - Ebuli\u00e7\u00e3o de nucleados - Defini\u00e7\u00e3o<\/title>\n<meta name=\"description\" content=\"McAdams - Thom - Correla\u00e7\u00e3o de Chen - Ebuli\u00e7\u00e3o de Nucleados. 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