{"id":47344,"date":"2019-11-04T02:56:35","date_gmt":"2019-11-04T01:56:35","guid":{"rendered":"https:\/\/www.thermal-engineering.org\/o-que-e-ebulicao-nuclear-definicao\/"},"modified":"2021-06-05T16:37:39","modified_gmt":"2021-06-05T15:37:39","slug":"o-que-e-ebulicao-nuclear-definicao","status":"publish","type":"post","link":"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-ebulicao-nuclear-definicao\/","title":{"rendered":"O que \u00e9 ebuli\u00e7\u00e3o nucleada &#8211; defini\u00e7\u00e3o"},"content":{"rendered":"<div class=\"su-quote su-quote-style-default\">\n<div class=\"su-quote-inner su-clearfix\">A ebuli\u00e7\u00e3o do nucleado ocorre a taxas de fluxo significativas atrav\u00e9s do reator.\u00a0Na ebuli\u00e7\u00e3o nucleada, formam-se bolhas de vapor na superf\u00edcie de transfer\u00eancia de calor e depois se separam e s\u00e3o transportadas para a corrente principal<\/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<\/h2>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Nucleate-Boiling-Boiling-Modes.png\"><img loading=\"lazy\" class=\"alignright size-medium wp-image-20782 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Nucleate-Boiling-Boiling-Modes-300x234.png\" alt=\"Ebuli\u00e7\u00e3o Nucleada - Modos de Ebuli\u00e7\u00e3o\" width=\"300\" height=\"234\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Nucleate-Boiling-Boiling-Modes-300x234.png\" \/><\/a>O tipo mais comum de ebuli\u00e7\u00e3o local encontrado em instala\u00e7\u00f5es nucleares \u00e9 a\u00a0<strong>ebuli\u00e7\u00e3o nucleada<\/strong>\u00a0.\u00a0Por\u00e9m, no caso de reatores nucleares, a\u00a0<strong>ebuli\u00e7\u00e3o nucleada<\/strong>\u00a0ocorre a taxas de fluxo significativas atrav\u00e9s do reator.\u00a0Na\u00a0<strong>ebuli\u00e7\u00e3o nucleada<\/strong>\u00a0, as bolhas de vapor se formam na superf\u00edcie de transfer\u00eancia de calor e depois se separam e s\u00e3o transportadas para a corrente principal do fluido.\u00a0Esse movimento melhora a transfer\u00eancia de calor porque o calor gerado na superf\u00edcie \u00e9 transportado diretamente para a corrente de fluido.\u00a0Uma vez na corrente principal de fluido, as bolhas colapsam porque a temperatura do fluido n\u00e3o \u00e9 t\u00e3o alta quanto a temperatura da superf\u00edcie de transfer\u00eancia de calor onde as bolhas foram criadas.\u00a0Como foi escrito, a\u00a0<strong>ebuli\u00e7\u00e3o nucleada<\/strong>na superf\u00edcie interrompe efetivamente essa camada estagnada e, portanto, a ebuli\u00e7\u00e3o nucleada\u00a0<strong>melhora<\/strong>\u00a0significativamente\u00a0\u00a0a capacidade de uma superf\u00edcie de transferir\u00a0<a href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/thermodynamics\/what-is-energy-physics\/internal-energy-thermal-energy\/\">energia t\u00e9rmica<\/a>\u00a0para o fluido a granel.\u00a0\u00c0s vezes, esse processo de transfer\u00eancia de calor \u00e9 desej\u00e1vel porque a energia criada na superf\u00edcie de transfer\u00eancia de calor \u00e9 r\u00e1pida e eficientemente &#8220;transportada&#8221;.<\/p>\n<p>Perto da parede, a situa\u00e7\u00e3o \u00e9 complexa, pois v\u00e1rios mecanismos aumentam o fluxo de calor acima daquele da\u00a0<a title=\"Condu\u00e7\u00e3o T\u00e9rmica - Condu\u00e7\u00e3o T\u00e9rmica\" href=\"https:\/\/www.thermal-engineering.org\/what-is-thermal-conduction-heat-conduction-definition\/\">pura condu\u00e7\u00e3o<\/a>\u00a0atrav\u00e9s do l\u00edquido.<\/p>\n<ol>\n<li>Observe que, mesmo em\u00a0<a title=\"Fluxo turbulento\" href=\"https:\/\/www.thermal-engineering.org\/what-is-turbulent-flow-definition\/\">fluxo turbulento<\/a>\u00a0, existe uma camada de filme fluido estagnada (subcamada laminar), que isola a superf\u00edcie do trocador de calor.\u00a0O fluxo ascendente (devido \u00e0s for\u00e7as de flutua\u00e7\u00e3o) do vapor que se afasta da parede deve ser equilibrado por um fluxo de massa igual de l\u00edquido, o que aproxima o l\u00edquido mais frio da parede.<\/li>\n<li>A forma\u00e7\u00e3o e o movimento das bolhas turbuliam o l\u00edquido perto da parede e aumentam a transfer\u00eancia de calor da parede para o l\u00edquido.<\/li>\n<li>A ebuli\u00e7\u00e3o difere de outras formas de convec\u00e7\u00e3o, pois depende do calor latente da vaporiza\u00e7\u00e3o, que \u00e9 muito alto para press\u00f5es comuns; portanto, grandes quantidades de calor podem ser transferidas durante a ebuli\u00e7\u00e3o essencialmente a temperatura constante.<\/li>\n<\/ol>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Boiling-Curve-Boiling-Modes.png\"><img loading=\"lazy\" class=\"alignright size-medium wp-image-20779 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Boiling-Curve-Boiling-Modes-208x300.png\" alt=\"Curva de Ebuli\u00e7\u00e3o - Modos de Ebuli\u00e7\u00e3o\" width=\"208\" height=\"300\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Boiling-Curve-Boiling-Modes-208x300.png\" \/><\/a>O\u00a0<strong>fluxo de calor em ebuli\u00e7\u00e3o nucleado<\/strong>\u00a0n\u00e3o pode ser aumentado indefinidamente.\u00a0Em algum valor, chamamos de \u201c\u00a0<strong>fluxo cr\u00edtico de calor<\/strong>\u00a0\u201d (\u00a0<strong>CHF<\/strong>\u00a0), o vapor produzido pode formar uma camada isolante sobre a superf\u00edcie, que por sua vez deteriora o coeficiente de transfer\u00eancia de calor.\u00a0Isso ocorre porque uma grande fra\u00e7\u00e3o da superf\u00edcie \u00e9 coberta por uma pel\u00edcula de vapor, que atua como um isolamento t\u00e9rmico devido \u00e0 baixa condutividade t\u00e9rmica do vapor em rela\u00e7\u00e3o \u00e0 do l\u00edquido.\u00a0Imediatamente ap\u00f3s o\u00a0<strong>fluxo cr\u00edtico de calor<\/strong>\u00a0ter sido atingido, a ebuli\u00e7\u00e3o se torna inst\u00e1vel e a ebuli\u00e7\u00e3o de transi\u00e7\u00e3o ocorre.\u00a0A transi\u00e7\u00e3o da ebuli\u00e7\u00e3o nucleada para a ebuli\u00e7\u00e3o de pel\u00edcula \u00e9 conhecida como &#8221;\u00a0<strong>crise de ebuli\u00e7\u00e3o<\/strong>\u00a0&#8220;.\u00a0Desde al\u00e9m do\u00a0<strong>CHF<\/strong>aponte o coeficiente de transfer\u00eancia de calor diminua, a transi\u00e7\u00e3o para a\u00a0<strong>ebuli\u00e7\u00e3o de pel\u00edcula<\/strong>\u00a0\u00e9 geralmente inevit\u00e1vel.<\/p>\n<p>Na se\u00e7\u00e3o a seguir, distinguiremos entre:<\/p>\n<ul>\n<li><strong>ebuli\u00e7\u00e3o da piscina nucleada<\/strong><\/li>\n<li><strong>ebuli\u00e7\u00e3o de fluxo nucleado<\/strong><\/li>\n<\/ul>\n<\/div>\n<\/div>\n<p>&nbsp;<\/p>\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\u00f5es de ebuli\u00e7\u00e3o de nucleados &#8211; Ebuli\u00e7\u00e3o da piscina<\/span><\/h2>\n<p><span>Os regimes de ebuli\u00e7\u00e3o discutidos acima diferem consideravelmente em seu car\u00e1ter.\u00a0Tamb\u00e9m existem correla\u00e7\u00f5es diferentes que descrevem a transfer\u00eancia de calor.\u00a0Nesta se\u00e7\u00e3o, revisamos algumas das correla\u00e7\u00f5es mais amplamente usadas para a ebuli\u00e7\u00e3o de nucleados.<\/span><\/p>\n<p><strong><span>Ebuli\u00e7\u00e3o de Piscina Nucleada<\/span><\/strong><\/p>\n<p><strong><span>Correla\u00e7\u00e3o de Rohsenow<\/span><\/strong><\/p>\n<p><span>A correla\u00e7\u00e3o mais amplamente utilizada para a taxa de transfer\u00eancia de calor na ebuli\u00e7\u00e3o do nucleado foi proposta em 1952 por\u00a0<\/span><strong><span>Rohsenow<\/span><\/strong><span>\u00a0:<\/span><\/p>\n<p><strong><span>Correla\u00e7\u00e3o de Rohsenow<\/span><\/strong><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Rohsenow-correlation-nucleate-boiling.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20786 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Rohsenow-correlation-nucleate-boiling.png\" alt=\"Correla\u00e7\u00e3o de Rohsenow - ebuli\u00e7\u00e3o nucleada\" width=\"403\" height=\"87\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Rohsenow-correlation-nucleate-boiling.png\" \/><\/a><\/p>\n<p><span>Onde<\/span><\/p>\n<ul>\n<li><span>q &#8211; fluxo de calor em ebuli\u00e7\u00e3o da piscina nucleada [W \/ m\u00a0<\/span><sup><span>2<\/span><\/sup><span>\u00a0]<\/span><\/li>\n<li><span>c\u00a0<\/span><sub><span>1<\/span><\/sub><span>\u00a0&#8211; calor espec\u00edfico do l\u00edquido J \/ kg K<\/span><\/li>\n<li><span>\u0394T &#8211; excesso de temperatura \u00b0 C ou K<\/span><\/li>\n<li><span>h\u00a0<\/span><sub><span>fg<\/span><\/sub><span>\u00a0\u00a0&#8211; entalpia de vaporiza\u00e7\u00e3o, J \/ kg<\/span><\/li>\n<li><span>Pr &#8211; n\u00famero Prandtl de l\u00edquido<\/span><\/li>\n<li><span>n &#8211; constante experimental igual a 1 para a \u00e1gua e 1,7 para outros fluidos<\/span><\/li>\n<li><span>C\u00a0<\/span><sub><span>sf<\/span><\/sub><span>\u00a0&#8211; fator de fluido da superf\u00edcie, por exemplo, \u00e1gua e n\u00edquel t\u00eam C\u00a0<\/span><sub><span>sf<\/span><\/sub><span>\u00a0de 0,006<\/span><\/li>\n<li><span>\u03bc\u00a0<\/span><sub><span>1<\/span><\/sub><span>\u00a0&#8211; viscosidade din\u00e2mica do l\u00edquido kg \/ ms<\/span><\/li>\n<li><span>g &#8211; acelera\u00e7\u00e3o gravitacional m \/ s\u00a0<\/span><sup><span>2<\/span><\/sup><\/li>\n<li><span>g\u00a0<\/span><sub><span>0<\/span><\/sub><span>\u00a0&#8211; fator de convers\u00e3o de for\u00e7a kgm \/ Ns\u00a0<\/span><sup><span>2<\/span><\/sup><\/li>\n<li><span>\u03c1\u00a0<\/span><sub><span>1<\/span><\/sub><span>\u00a0&#8211; densidade do l\u00edquido kg \/ m\u00a0<\/span><sup><span>3<\/span><\/sup><\/li>\n<li><span>\u03c1\u00a0<\/span><sub><span>v<\/span><\/sub><span>\u00a0&#8211; densidade do vapor kg \/ m\u00a0<\/span><sup><span>3<\/span><\/sup><\/li>\n<li><span>\u03c3 &#8211; interface tens\u00e3o superficial-vapor-l\u00edquido N \/ m<\/span><\/li>\n<\/ul>\n<p><span>Como pode ser visto, \u0394T \u221d (q)\u00a0<\/span><sup><span>\u2153<\/span><\/sup><span>\u00a0.\u00a0Essa proporcionalidade muito importante mostra a capacidade crescente da interface de transferir calor.<\/span><\/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>Ebuli\u00e7\u00e3o Nucleada &#8211; Ebuli\u00e7\u00e3o por Fluxo<\/span><\/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><span>Na\u00a0<\/span><strong><span>fervura de fluxo<\/span><\/strong><span>\u00a0(ou\u00a0<\/span><strong><span>fervura de convec\u00e7\u00e3o for\u00e7ada<\/span><\/strong><span>\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.<\/span><\/p>\n<p><span>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 de duas fases 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 geralmente chamada de\u00a0<\/span><strong><span>fluxo bif\u00e1sico<\/span><\/strong><span>\u00a0.<\/span><\/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\u00f5es de ebuli\u00e7\u00e3o de nucleados &#8211; ebuli\u00e7\u00e3o por fluxo<\/span><\/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><span>Correla\u00e7\u00e3o de McAdams<\/span><\/h2>\n<p><span>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<\/span><a title=\"N\u00famero de Reynolds\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/fluid-dynamics\/reynolds-number\/\"><span>n\u00famero de Reynolds<\/span><\/a><span>\u00a0.\u00a0Para \u00e1gua sub-resfriada a press\u00f5es absolutas entre 0,1 &#8211; 0,6 MPa, a\u00a0<\/span><strong><span>correla\u00e7\u00e3o de McAdams<\/span><\/strong><span>\u00a0fornece:<\/span><\/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<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\/what-is-convective-heat-transfer-coefficient-definition\/\"><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 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>Crise de ebuli\u00e7\u00e3o &#8211; Fluxo cr\u00edtico de calor<\/span><\/h2>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Dryout-DNB-min.png\"><img loading=\"lazy\" class=\"alignright size-medium wp-image-14862 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Dryout-DNB-min-225x300.png\" alt=\"Dryout vs. DNB\" width=\"225\" height=\"300\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Dryout-DNB-min-225x300.png\" \/><\/a><span>Como foi escrito, nos\u00a0<\/span><a href=\"https:\/\/www.nuclear-power.com\/nuclear-power-plant\/nuclear-reactor\/\"><span>reatores nucleares<\/span><\/a><span>\u00a0, as limita\u00e7\u00f5es do\u00a0<\/span><strong><span>fluxo de calor local<\/span><\/strong><span>\u00a0s\u00e3o da maior import\u00e2ncia para a seguran\u00e7a do reator.\u00a0Para\u00a0<\/span><a href=\"https:\/\/www.nuclear-power.com\/pwr-pressurized-water-reactor\/\"><span>reatores de \u00e1gua pressurizada<\/span><\/a><span>\u00a0e tamb\u00e9m para\u00a0<\/span><a href=\"https:\/\/www.nuclear-power.com\/bwr-boiling-water-reactor\/\"><span>reatores de \u00e1gua fervente<\/span><\/a><span>\u00a0, existem fen\u00f4menos termo-hidr\u00e1ulicos, que causam uma diminui\u00e7\u00e3o repentina na\u00a0<\/span><strong><span>efici\u00eancia da transfer\u00eancia de calor<\/span><\/strong><span>\u00a0(mais precisamente no\u00a0<\/span><strong><span>coeficiente de transfer\u00eancia de calor<\/span><\/strong><span>\u00a0).\u00a0Esses fen\u00f4menos ocorrem com certo valor do fluxo de calor, conhecido como &#8221;\u00a0<\/span><strong><span>fluxo cr\u00edtico de calor<\/span><\/strong><span>\u00a0&#8220;.\u00a0Os fen\u00f4menos que causam a deteriora\u00e7\u00e3o da transfer\u00eancia de calor s\u00e3o diferentes para PWRs e BWRs.<\/span><\/p>\n<p><span>Nos dois tipos de reatores, o problema est\u00e1 mais ou menos associado \u00e0 sa\u00edda da ebuli\u00e7\u00e3o nucleada.\u00a0O fluxo de calor em ebuli\u00e7\u00e3o nucleado n\u00e3o pode ser aumentado indefinidamente.\u00a0Em algum valor, chamamos de \u201c\u00a0<\/span><strong><span>fluxo cr\u00edtico de calor<\/span><\/strong><span>\u00a0\u201d (\u00a0<\/span><strong><span>CHF<\/span><\/strong><span>\u00a0), o vapor produzido pode formar uma camada isolante sobre a superf\u00edcie, que por sua vez deteriora o coeficiente de transfer\u00eancia de calor.\u00a0Imediatamente ap\u00f3s o fluxo cr\u00edtico de calor ter sido atingido, a ebuli\u00e7\u00e3o se torna inst\u00e1vel e a ebuli\u00e7\u00e3o de pel\u00edcula ocorre.\u00a0A transi\u00e7\u00e3o da ebuli\u00e7\u00e3o nucleada para a ebuli\u00e7\u00e3o de pel\u00edcula \u00e9 conhecida como &#8221;\u00a0<\/span><strong><span>crise de ebuli\u00e7\u00e3o<\/span><\/strong><span>\u00a0&#8220;.\u00a0Como foi escrito, os fen\u00f4menos que causam a deteriora\u00e7\u00e3o da transfer\u00eancia de calor s\u00e3o diferentes para PWRs e BWRs.<\/span><\/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>Partida da Ebuli\u00e7\u00e3o Nucleada &#8211; DNB<\/span><\/h2>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/DNBR-Departure-from-Nucleate-Boiling-Ratio.png\"><img loading=\"lazy\" class=\"alignright size-medium wp-image-20775 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/DNBR-Departure-from-Nucleate-Boiling-Ratio-289x300.png\" alt=\"DNBR - Partida da Raz\u00e3o de Ebuli\u00e7\u00e3o Nucleada\" width=\"289\" height=\"300\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/DNBR-Departure-from-Nucleate-Boiling-Ratio-289x300.png\" \/><\/a><span>No caso de\u00a0<\/span><a href=\"https:\/\/www.nuclear-power.com\/pwr-pressurized-water-reactor\/\"><span>PWRs<\/span><\/a><span>\u00a0, a quest\u00e3o cr\u00edtica de seguran\u00e7a \u00e9 denominada\u00a0<\/span><strong><span>DNB<\/span><\/strong><span>\u00a0(\u00a0<\/span><strong><span>partida da ebuli\u00e7\u00e3o nucleada<\/span><\/strong><span>\u00a0), que causa a forma\u00e7\u00e3o de uma\u00a0<\/span><strong><span>camada de vapor local<\/span><\/strong><span>\u00a0, causando uma redu\u00e7\u00e3o dr\u00e1stica na capacidade de transfer\u00eancia de calor.\u00a0Esse fen\u00f4meno ocorre na regi\u00e3o sub-resfriada ou de baixa qualidade.\u00a0O comportamento da crise de ebuli\u00e7\u00e3o depende de muitas condi\u00e7\u00f5es de fluxo (press\u00e3o, temperatura, taxa de fluxo), mas a crise de ebuli\u00e7\u00e3o ocorre em fluxos de calor relativamente altos e parece estar associado \u00e0 nuvem de bolhas adjacentes \u00e0 superf\u00edcie.\u00a0Essas bolhas ou filme de vapor reduzem a quantidade de \u00e1gua que entra.\u00a0Como esse fen\u00f4meno deteriora o coeficiente de transfer\u00eancia de calor e o fluxo de calor permanece, o calor\u00a0<\/span><strong><span>acumula-se<\/span><\/strong><span>na barra de combust\u00edvel, causando\u00a0<\/span><strong><span>aumento dram\u00e1tico<\/span><\/strong><span>\u00a0do revestimento e da\u00a0<\/span><strong><span>temperatura do<\/span><\/strong><span>\u00a0combust\u00edvel\u00a0.\u00a0Simplesmente, \u00e9 necess\u00e1ria uma diferen\u00e7a de temperatura muito alta para transferir o fluxo de calor cr\u00edtico produzido da superf\u00edcie da barra de combust\u00edvel para o l\u00edquido de arrefecimento do reator (atrav\u00e9s da camada de vapor).<\/span><\/p>\n<p><span>No caso de PWRs, o fluxo cr\u00edtico \u00e9 um fluxo\u00a0<\/span><strong><span>anular invertido<\/span><\/strong><span>\u00a0, enquanto que nos BWRs, o fluxo cr\u00edtico \u00e9 geralmente um fluxo anular.\u00a0A diferen\u00e7a no regime de fluxo entre o fluxo p\u00f3s-secagem e o fluxo p\u00f3s-DNB \u00e9 mostrada na figura.\u00a0Em\u00a0<\/span><strong><span>PWRs<\/span><\/strong><span>\u00a0em\u00a0<\/span><strong><span>opera\u00e7\u00e3o normal,<\/span><\/strong><span>\u00a0o fluxo \u00e9 considerado monof\u00e1sico.\u00a0Por\u00e9m, muitos estudos foram realizados sobre a natureza do\u00a0<\/span><strong><span>fluxo bif\u00e1sico<\/span><\/strong><span>\u00a0em caso de\u00a0<\/span><strong><span>transientes e acidentes<\/span><\/strong><span>\u00a0(como o\u00a0<strong>acidente<\/strong>\u00a0com\u00a0<\/span><strong><span>perda de l\u00edquido refrigerante &#8211; LOCA ou disparo de RCPs<\/span><\/strong><span>\u00a0), que s\u00e3o importantes para a seguran\u00e7a do reator e deve ser comprovado e declarado no\u00a0<\/span><strong><span>Relat\u00f3rio de An\u00e1lise de Seguran\u00e7a<\/span><\/strong><span>\u00a0(SAR).<\/span><\/p>\n<p><span>Nos reatores de \u00e1gua pressurizada, um dos principais requisitos de seguran\u00e7a \u00e9 que a sa\u00edda da ebuli\u00e7\u00e3o nucleada (DNB) n\u00e3o ocorrer\u00e1 durante a opera\u00e7\u00e3o em estado estacion\u00e1rio, transientes operacionais normais e ocorr\u00eancias operacionais previstas (AOOs).\u00a0A integridade do revestimento de combust\u00edvel ser\u00e1 mantida se o DNBR m\u00ednimo permanecer acima do limite de 95\/95 DNBR para PWRs (uma probabilidade de 95% a um n\u00edvel de confian\u00e7a de 95%).\u00a0O crit\u00e9rio DNB \u00e9 um dos crit\u00e9rios de aceita\u00e7\u00e3o nas an\u00e1lises de seguran\u00e7a, al\u00e9m de constituir um dos limites de seguran\u00e7a nas especifica\u00e7\u00f5es t\u00e9cnicas.<\/span><\/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>Dryout &#8211; BWRs<\/span><\/h2>\n<p><strong><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Flow-Boiling-Dryout.png\"><img loading=\"lazy\" class=\"alignright size-medium wp-image-20773 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Flow-Boiling-Dryout-257x300.png\" alt=\"Ebuli\u00e7\u00e3o do fluxo - secagem\" width=\"257\" height=\"300\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Flow-Boiling-Dryout-257x300.png\" \/><\/a><\/strong>Nos BWRs, um fen\u00f4meno semelhante \u00e9 conhecido como\u00a0<strong>\u201csecagem\u201d<\/strong>\u00a0e est\u00e1 diretamente associado a\u00a0<strong>altera\u00e7\u00f5es no padr\u00e3o de fluxo<\/strong>\u00a0durante a evapora\u00e7\u00e3o na regi\u00e3o de alta qualidade.\u00a0Em determinadas combina\u00e7\u00f5es de taxa de fluxo atrav\u00e9s de um canal, press\u00e3o, qualidade de fluxo e taxa de calor linear, o\u00a0<strong>filme l\u00edquido\u00a0<\/strong>da parede\u00a0<strong>pode esgotar-se<\/strong>\u00a0e a parede pode ser\u00a0<strong>seca<\/strong>\u00a0.\u00a0Normalmente, a superf\u00edcie do combust\u00edvel \u00e9 efetivamente resfriada com l\u00edquido fervente.\u00a0No entanto, quando o fluxo de calor excede um\u00a0<strong>valor cr\u00edtico<\/strong>\u00a0(CHF &#8211; fluxo de calor cr\u00edtico), o padr\u00e3o de fluxo pode atingir as\u00a0<strong>condi\u00e7\u00f5es de secagem<\/strong>\u00a0(a pel\u00edcula fina de l\u00edquido desaparece).\u00a0A transfer\u00eancia de calor da superf\u00edcie do combust\u00edvel para o refrigerante \u00e9 deteriorada, com o resultado de<strong>aumento dr\u00e1stico da temperatura da superf\u00edcie do combust\u00edvel\u00a0<\/strong>. Na regi\u00e3o de alta qualidade, a crise ocorre com um fluxo de calor menor. Como a velocidade do fluxo no n\u00facleo de vapor \u00e9 alta, a transfer\u00eancia de calor p\u00f3s-CHF \u00e9 muito melhor do que no fluxo cr\u00edtico de baixa qualidade (ou seja, para PWRs, os aumentos de temperatura s\u00e3o mais altos e mais r\u00e1pidos).<\/p>\n<\/div>\n<\/div>\n<p>&nbsp;<\/p>\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>A ebuli\u00e7\u00e3o do nucleado ocorre a taxas de fluxo significativas atrav\u00e9s do reator.\u00a0Na ebuli\u00e7\u00e3o nucleada, formam-se bolhas de vapor na superf\u00edcie de transfer\u00eancia de calor e depois se separam e s\u00e3o transportadas para a corrente principal Ebuli\u00e7\u00e3o Nucleada O tipo mais comum de ebuli\u00e7\u00e3o local encontrado em instala\u00e7\u00f5es nucleares \u00e9 a\u00a0ebuli\u00e7\u00e3o nucleada\u00a0.\u00a0Por\u00e9m, no caso de &#8230; <a title=\"O que \u00e9 ebuli\u00e7\u00e3o nucleada &#8211; defini\u00e7\u00e3o\" class=\"read-more\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-ebulicao-nuclear-definicao\/\" aria-label=\"More on O que \u00e9 ebuli\u00e7\u00e3o nucleada &#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 ebuli\u00e7\u00e3o nucleada - defini\u00e7\u00e3o<\/title>\n<meta name=\"description\" content=\"A ebuli\u00e7\u00e3o do nucleado ocorre a taxas de fluxo significativas atrav\u00e9s do reator. 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