{"id":51102,"date":"2020-01-24T10:28:54","date_gmt":"2020-01-24T09:28:54","guid":{"rendered":"https:\/\/www.thermal-engineering.org\/o-que-e-conveccao-transferencia-de-calor-por-conveccao-definicao\/"},"modified":"2020-01-24T10:35:16","modified_gmt":"2020-01-24T09:35:16","slug":"o-que-e-conveccao-transferencia-de-calor-por-conveccao-definicao","status":"publish","type":"post","link":"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-conveccao-transferencia-de-calor-por-conveccao-definicao\/","title":{"rendered":"O que \u00e9 convec\u00e7\u00e3o &#8211; transfer\u00eancia de calor por convec\u00e7\u00e3o &#8211; defini\u00e7\u00e3o"},"content":{"rendered":"<div class=\"su-quote su-quote-style-default\">\n<div class=\"su-quote-inner su-clearfix\">A convec\u00e7\u00e3o \u00e9 a transfer\u00eancia de massa ou a transfer\u00eancia de calor devido ao movimento a granel.\u00a0O processo de transfer\u00eancia de calor entre uma superf\u00edcie e um fluido que flui em contato com ela \u00e9 chamado de transfer\u00eancia de calor por convec\u00e7\u00e3o.\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>O que \u00e9 convec\u00e7\u00e3o<\/h2>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Convection-Convective-Heat-Transfer-comparison-min.png\"><img loading=\"lazy\" class=\"alignright size-medium wp-image-20378 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Convection-Convective-Heat-Transfer-comparison-min-281x300.png\" alt=\"Convec\u00e7\u00e3o - Transfer\u00eancia de calor por convec\u00e7\u00e3o\" width=\"281\" height=\"300\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Convection-Convective-Heat-Transfer-comparison-min-281x300.png\" \/><\/a>Em geral, a\u00a0<strong>convec\u00e7\u00e3o<\/strong>\u00a0\u00e9 a\u00a0<strong>transfer\u00eancia de massa<\/strong>\u00a0ou a\u00a0<strong>transfer\u00eancia de calor<\/strong>\u00a0devido ao\u00a0<strong>movimento em massa<\/strong>\u00a0de mol\u00e9culas dentro de fluidos, como gases e l\u00edquidos.\u00a0Embora l\u00edquidos e gases geralmente n\u00e3o sejam bons condutores de calor, eles podem transferir calor rapidamente\u00a0<strong>por convec\u00e7\u00e3o<\/strong>\u00a0.<\/p>\n<p><strong>A convec\u00e7\u00e3o<\/strong>\u00a0ocorre atrav\u00e9s de\u00a0<strong>advec\u00e7\u00e3o<\/strong>\u00a0,\u00a0<strong>difus\u00e3o<\/strong>\u00a0ou ambos.\u00a0A convec\u00e7\u00e3o n\u00e3o pode ocorrer na maioria dos s\u00f3lidos, porque nem a difus\u00e3o significativa da mat\u00e9ria nem os fluxos de corrente a granel podem ocorrer.\u00a0A difus\u00e3o do calor ocorre em s\u00f3lidos r\u00edgidos, mas isso \u00e9 chamado\u00a0<a title=\"Condu\u00e7\u00e3o T\u00e9rmica - Condu\u00e7\u00e3o T\u00e9rmica\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-conducao-termica-conducao-termica-definicao\/\">de condu\u00e7\u00e3o t\u00e9rmica<\/a>\u00a0.<\/p>\n<p>O processo de transfer\u00eancia de calor entre uma superf\u00edcie e um fluido que flui em contato com ela \u00e9 chamado de\u00a0<strong>transfer\u00eancia de calor por convec\u00e7\u00e3o<\/strong>\u00a0.\u00a0Na engenharia, a transfer\u00eancia de calor por convec\u00e7\u00e3o \u00e9 um dos principais mecanismos de\u00a0<a title=\"Transfer\u00eancia de calor\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-transferencia-de-calor-definicao\/\"><strong>transfer\u00eancia<\/strong><\/a>\u00a0de\u00a0<a title=\"Heat Transfer\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-transferencia-de-calor-definicao\/\"><strong>calor<\/strong><\/a>\u00a0.\u00a0Quando o calor \u00e9 transferido de um fluido para outro atrav\u00e9s de uma barreira, a convec\u00e7\u00e3o \u00e9 envolvida em ambos os lados da barreira.\u00a0Na maioria dos casos, a principal\u00a0<a title=\"Resist\u00eancia t\u00e9rmica - analogia \u00e0 resist\u00eancia el\u00e9trica\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/heat-transfer\/thermal-conduction\/thermal-resistance-thermal-resistivity\/thermal-resistance-analogy-to-electric-resistance\/\">resist\u00eancia<\/a>\u00a0ao fluxo de calor \u00e9 por convec\u00e7\u00e3o.\u00a0<strong>A transfer\u00eancia de calor por convec\u00e7\u00e3o<\/strong>\u00a0ocorre tanto por difus\u00e3o t\u00e9rmica (o movimento aleat\u00f3rio das mol\u00e9culas de fluido) quanto por advec\u00e7\u00e3o, na qual a mat\u00e9ria ou o calor \u00e9 transportado pelo movimento em larga escala das correntes no fluido.<\/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>Mecanismo de Convec\u00e7\u00e3o<\/h2>\n<p>Na\u00a0<a title=\"Condu\u00e7\u00e3o T\u00e9rmica - Condu\u00e7\u00e3o T\u00e9rmica\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-conducao-termica-conducao-termica-definicao\/\"><strong>condu\u00e7\u00e3o t\u00e9rmica<\/strong><\/a>\u00a0, a\u00a0<a title=\"O que \u00e9 energia - F\u00edsica\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/thermodynamics\/what-is-energy-physics\/\">energia<\/a>\u00a0\u00e9 transferida como\u00a0<a title=\"Calor na Termodin\u00e2mica\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-calor-na-fisica-calor-definicao\/\">calor<\/a>\u00a0devido \u00e0\u00a0<strong>migra\u00e7\u00e3o de el\u00e9trons livres<\/strong>\u00a0ou\u00a0<strong>ondas vibracionais em treli\u00e7a (\u00a0<a title=\"O que \u00e9 Phonon - Defini\u00e7\u00e3o\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-phonon-definicao\/\">f\u00f4nons<\/a>\u00a0).\u00a0<\/strong>N\u00e3o h\u00e1 movimento de massa na dire\u00e7\u00e3o do fluxo de energia.\u00a0<a href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-transferencia-de-calor-definicao\/\">A transfer\u00eancia de calor<\/a>\u00a0por\u00a0<strong>condu\u00e7\u00e3o<\/strong>\u00a0depende da \u201cfor\u00e7a\u201d motriz da\u00a0<strong>diferen\u00e7a<\/strong>\u00a0de\u00a0<strong>temperatura.\u00a0<\/strong><strong>A condu\u00e7\u00e3o<\/strong>\u00a0e a\u00a0<strong>convec\u00e7\u00e3o<\/strong>\u00a0s\u00e3o semelhantes, pois ambos os mecanismos requerem a presen\u00e7a de um meio material (em compara\u00e7\u00e3o com a radia\u00e7\u00e3o t\u00e9rmica).\u00a0Por outro lado, eles s\u00e3o diferentes, pois a convec\u00e7\u00e3o requer a presen\u00e7a de movimento fluido.<\/p>\n<p>Deve-se enfatizar que\u00a0<strong>, na superf\u00edcie,<\/strong>\u00a0o fluxo de energia ocorre\u00a0\u00a0<strong>puramente por condu\u00e7\u00e3o,<\/strong>\u00a0mesmo em condu\u00e7\u00e3o.\u00a0Isso ocorre porque sempre h\u00e1 uma\u00a0<strong>fina camada de filme estagnado\u00a0na superf\u00edcie da transfer\u00eancia de calor.\u00a0<\/strong>\u00a0Por\u00e9m, nas pr\u00f3ximas camadas, ocorrem movimentos de condu\u00e7\u00e3o e difus\u00e3o-massa no n\u00edvel molecular ou no n\u00edvel macrosc\u00f3pico.\u00a0Devido ao movimento de massa, a taxa de transfer\u00eancia de energia \u00e9 maior.\u00a0Quanto maior a taxa de movimento de massa, mais fina ser\u00e1 a camada de filme fluido estagnado e maior ser\u00e1 a taxa de fluxo de calor.<\/p>\n<p>Deve-se notar que a\u00a0<strong>ebuli\u00e7\u00e3o nucleada<\/strong>\u00a0na superf\u00edcie interrompe efetivamente essa camada estagnada e, portanto, a ebuli\u00e7\u00e3o nucleada aumenta significativamente a capacidade de uma superf\u00edcie de transferir energia t\u00e9rmica para o fluido a granel.<\/p>\n<p>Como foi escrito, a transfer\u00eancia de calor atrav\u00e9s de um fluido \u00e9 por convec\u00e7\u00e3o na presen\u00e7a de movimento de massa e por condu\u00e7\u00e3o na aus\u00eancia dele.\u00a0Portanto, a condu\u00e7\u00e3o t\u00e9rmica em um fluido pode ser vista como o caso limitador de convec\u00e7\u00e3o, correspondendo ao caso de fluido inativo.<\/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>Convec\u00e7\u00e3o como Condu\u00e7\u00e3o com Movimento Fluido<\/h2>\n<p><span>Alguns especialistas n\u00e3o consideram a convec\u00e7\u00e3o um mecanismo fundamental de transfer\u00eancia de calor, pois \u00e9 essencialmente a condu\u00e7\u00e3o de calor na presen\u00e7a de movimento de fluidos.\u00a0Eles consideram que este \u00e9 um\u00a0<\/span><strong><span>caso especial de condu\u00e7\u00e3o t\u00e9rmica<\/span><\/strong><span>\u00a0, conhecido como &#8221;\u00a0<\/span><strong><span>condu\u00e7\u00e3o com movimento de fluido<\/span><\/strong><span>\u00a0&#8220;.\u00a0Por outro lado, \u00e9\u00a0<\/span><strong><span>pr\u00e1tico<\/span><\/strong><span>\u00a0reconhecer a convec\u00e7\u00e3o como um mecanismo separado de transfer\u00eancia de calor, apesar dos argumentos v\u00e1lidos em contr\u00e1rio.<\/span><\/p>\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\"><span><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/laminar-sublayer-convection-min.png\"><img loading=\"lazy\" class=\"alignright size-medium wp-image-20377 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/laminar-sublayer-convection-min-216x300.png\" alt=\"subcamada laminar - convec\u00e7\u00e3o\" width=\"216\" height=\"300\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/laminar-sublayer-convection-min-216x300.png\" \/><\/a>A transfer\u00eancia de calor por\u00a0<\/span><strong><span>convec\u00e7\u00e3o<\/span><\/strong><span>\u00a0\u00e9 mais dif\u00edcil de analisar do que a transfer\u00eancia de calor por\u00a0<\/span><a title=\"Condu\u00e7\u00e3o T\u00e9rmica - Condu\u00e7\u00e3o T\u00e9rmica\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-conducao-termica-conducao-termica-definicao\/\"><span>condu\u00e7\u00e3o,<\/span><\/a><span>\u00a0porque nenhuma propriedade \u00fanica do meio de transfer\u00eancia de calor, como\u00a0<\/span><a title=\"Condutividade t\u00e9rmica\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-condutividade-termica-definicao\/\"><span>a condutividade t\u00e9rmica<\/span><\/a><span>\u00a0, pode ser definida para descrever o mecanismo.\u00a0<\/span><strong><span>A transfer\u00eancia de calor por convec\u00e7\u00e3o<\/span><\/strong><span>\u00a0\u00e9 complicada pelo fato de envolver\u00a0<\/span><strong><span>movimento de fluidos e condu\u00e7\u00e3o de calor<\/span><\/strong><span>\u00a0.\u00a0A transfer\u00eancia de calor por convec\u00e7\u00e3o varia de situa\u00e7\u00e3o para situa\u00e7\u00e3o (de acordo com as condi\u00e7\u00f5es de fluxo do fluido), e \u00e9 freq\u00fcentemente acoplada ao\u00a0<\/span><a title=\"Regime de fluxo\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/fluid-dynamics\/flow-regime\/\"><span>modo de fluxo do fluido<\/span><\/a><span>\u00a0.\u00a0Na convec\u00e7\u00e3o for\u00e7ada, a taxa de transfer\u00eancia de calor atrav\u00e9s de um fluido \u00e9 muito maior por convec\u00e7\u00e3o do que por condu\u00e7\u00e3o.<\/span><span>Na pr\u00e1tica, a an\u00e1lise da transfer\u00eancia de calor por convec\u00e7\u00e3o \u00e9 tratada\u00a0<\/span><strong><span>empiricamente<\/span><\/strong><span>\u00a0(por observa\u00e7\u00e3o experimental direta).\u00a0A maioria dos problemas pode ser resolvida usando os chamados\u00a0<\/span><a title=\"N\u00fameros de caracter\u00edstica\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/heat-transfer\/introduction-to-heat-transfer\/characteristic-numbers\/\"><span>n\u00fameros de caracter\u00edstica<\/span><\/a><span>\u00a0(por exemplo,\u00a0<\/span><strong><span>n\u00famero de Nusselt<\/span><\/strong><span>\u00a0).\u00a0<\/span><strong><span>N\u00fameros de caracter\u00edstica<\/span><\/strong><span>\u00a0s\u00e3o\u00a0<strong>n\u00fameros sem<\/strong>\u00a0dimens\u00e3o usados \u200b\u200bpara descrever um caractere de transfer\u00eancia de calor e podem ser usados \u200b\u200bpara comparar uma\u00a0<\/span><strong><span>situa\u00e7\u00e3o real<\/span><\/strong><span>\u00a0(por exemplo, transfer\u00eancia de calor em um tubo) com um\u00a0<\/span><strong><span>modelo de pequena escala<\/span><\/strong><span>\u00a0.\u00a0A experi\u00eancia mostra que a transfer\u00eancia de calor por convec\u00e7\u00e3o depende fortemente das propriedades do fluido\u00a0<\/span><strong><span>viscosidade din\u00e2mica<\/span><\/strong><span>\u00a0,\u00a0<\/span><a title=\"Condutividade t\u00e9rmica\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-condutividade-termica-definicao\/\"><strong><span>condutividade t\u00e9rmica<\/span><\/strong><\/a><span>\u00a0,\u00a0<\/span><a title=\"O que \u00e9 densidade - F\u00edsica\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/thermodynamics\/thermodynamic-properties\/what-is-density-physics\/\"><strong><span>densidade<\/span><\/strong><\/a><span>\u00a0e\u00a0<\/span><strong><a title=\"Capacidade t\u00e9rmica - Capacidade t\u00e9rmica espec\u00edfica\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/thermodynamics\/laws-of-thermodynamics\/first-law-of-thermodynamics\/heat-capacity\/\"><span>calor espec\u00edfico<\/span><\/a><\/strong><span>\u00a0, bem como da<\/span><strong><span>velocidade do fluido<\/span><\/strong><span>\u00a0.\u00a0Tamb\u00e9m depende da geometria e da\u00a0<\/span><a title=\"Rugosidade relativa do tubo\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/fluid-dynamics\/major-head-loss-friction-loss\/relative-roughness-of-pipe\/\"><span>rugosidade<\/span><\/a><span>\u00a0da superf\u00edcie s\u00f3lida, al\u00e9m do tipo de fluxo de fluido.\u00a0Todas essas condi\u00e7\u00f5es afetam especialmente a\u00a0<\/span><strong><span>espessura do filme estagnado<\/span><\/strong><span>\u00a0.<\/span><\/p>\n<p><span>A convec\u00e7\u00e3o envolve a transfer\u00eancia de calor entre uma superf\u00edcie a uma determinada temperatura (\u00a0<\/span><sub><span>parede<\/span><\/sub><span>\u00a0T\u00a0) e fluido a uma temperatura a granel (T\u00a0<\/span><sub><span>b<\/span><\/sub><span>\u00a0).\u00a0A defini\u00e7\u00e3o exata da temperatura do volume (T\u00a0<\/span><sub><span>b<\/span><\/sub><span>\u00a0) varia dependendo dos detalhes da situa\u00e7\u00e3o.<\/span><\/p>\n<ul>\n<li><span>Para o fluxo adjacente a uma superf\u00edcie quente ou fria,\u00a0<\/span><sub><span>Tb<\/span><\/sub><span>\u00a0\u00e9 a temperatura do fluido &#8220;distante&#8221; da superf\u00edcie.<\/span><\/li>\n<li><span>Para ebuli\u00e7\u00e3o ou condensa\u00e7\u00e3o,\u00a0<\/span><sub><span>Tb<\/span><\/sub><span>\u00a0\u00e9 a\u00a0<\/span><a title=\"Satura\u00e7\u00e3o - Ponto de Ebuli\u00e7\u00e3o\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-saturacao-ponto-de-ebulicao-definicao\/\"><span>temperatura<\/span><\/a><span>\u00a0de\u00a0<a title=\"Satura\u00e7\u00e3o - Ponto de Ebuli\u00e7\u00e3o\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-saturacao-ponto-de-ebulicao-definicao\/\">satura\u00e7\u00e3o<\/a>\u00a0do fluido.<\/span><\/li>\n<li><span>Para o fluxo em um tubo, T\u00a0<\/span><sub><span>b<\/span><\/sub><span>\u00a0\u00e9 a temperatura m\u00e9dia medida em uma se\u00e7\u00e3o transversal espec\u00edfica do tubo.<\/span><\/li>\n<\/ul>\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>Lei de Newton de resfriamento<\/span><\/h2>\n<p><span>Apesar da complexidade da\u00a0<\/span><strong><span>convec\u00e7\u00e3o<\/span><\/strong><span>\u00a0, a taxa de transfer\u00eancia de calor por convec\u00e7\u00e3o \u00e9 observada\u00a0<\/span><strong><span>proporcional<\/span><\/strong><span>\u00a0\u00e0\u00a0<\/span><strong><span>diferen\u00e7a de temperatura<\/span><\/strong><span>\u00a0e \u00e9 convenientemente expressa pela\u00a0<\/span><strong><span>lei do resfriamento de Newton<\/span><\/strong><span>\u00a0, que afirma que:<\/span><\/p>\n<p><em><span>A taxa de perda de calor de um corpo \u00e9 diretamente proporcional \u00e0 diferen\u00e7a de temperatura entre o corpo e seus arredores, desde que a diferen\u00e7a de temperatura seja pequena e a natureza da superf\u00edcie radiante permane\u00e7a a mesma.<\/span><\/em><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/newtons-law-of-cooling-convection-equation.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20387 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/newtons-law-of-cooling-convection-equation.png\" alt=\"lei de newton do resfriamento - equa\u00e7\u00e3o da convec\u00e7\u00e3o\" width=\"269\" height=\"137\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/newtons-law-of-cooling-convection-equation.png\" \/><\/a><\/p>\n<p><span>Observe que\u00a0<\/span><strong><span>\u0394T<\/span><\/strong><span>\u00a0\u00e9 dado pela\u00a0<\/span><strong><span>temperatura<\/span><\/strong><span>\u00a0da superf\u00edcie ou da\u00a0<strong>parede<\/strong>\u00a0,\u00a0<strong><sub>parede<\/sub><\/strong><\/span><strong><span>\u00a0T<\/span>\u00a0<\/strong><span>e\u00a0<\/span><strong><span>temperatura<\/span><\/strong><span>\u00a0do\u00a0<strong>volume<\/strong>\u00a0,\u00a0<\/span><strong><span>T\u00a0<\/span><sub><span>\u221e<\/span><\/sub><\/strong><span>\u00a0, que \u00e9 a temperatura do fluido suficientemente longe da superf\u00edcie.<\/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>Coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o<\/span><\/h2>\n<p><span>Como pode ser visto, a\u00a0<\/span><strong><span>constante de proporcionalidade<\/span><\/strong><span>\u00a0ser\u00e1 crucial nos c\u00e1lculos e \u00e9 conhecida como\u00a0<\/span><strong><span>coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o<\/span><\/strong><span>\u00a0,\u00a0<\/span><strong><span>h<\/span><\/strong><span>\u00a0.\u00a0O\u00a0<\/span><strong><span>coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o,<\/span><\/strong><span>\u00a0h, pode ser definido como:<\/span><\/p>\n<p><em><span>A taxa de transfer\u00eancia de calor entre uma superf\u00edcie s\u00f3lida e um fluido por unidade de superf\u00edcie e por diferen\u00e7a de temperatura da unidade.<\/span><\/em><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/convective-heat-transfer-coefficient-equation.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20388 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/convective-heat-transfer-coefficient-equation.png\" alt=\"coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o - equa\u00e7\u00e3o\" width=\"265\" height=\"167\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/convective-heat-transfer-coefficient-equation.png\" \/><\/a><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/convective-heat-transfer-coefficient-examples.png\"><img loading=\"lazy\" class=\"alignright size-full wp-image-20389 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/convective-heat-transfer-coefficient-examples.png\" alt=\"coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o - exemplos\" width=\"337\" height=\"277\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/convective-heat-transfer-coefficient-examples.png\" \/><\/a><span>O\u00a0<\/span><strong><span>coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o<\/span><\/strong><span>\u00a0depende das propriedades f\u00edsicas do fluido e da situa\u00e7\u00e3o f\u00edsica.\u00a0O coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o n\u00e3o \u00e9 uma propriedade do fluido.\u00a0\u00c9 um par\u00e2metro determinado experimentalmente, cujo valor depende de todas as vari\u00e1veis \u200b\u200bque influenciam a convec\u00e7\u00e3o, como a\u00a0<\/span><strong><span>geometria<\/span><\/strong><span>\u00a0da\u00a0<strong>superf\u00edcie<\/strong>\u00a0, a\u00a0<\/span><strong><span>natureza do movimento do fluido<\/span><\/strong><span>\u00a0, as\u00a0<\/span><strong><span>propriedades do fluido<\/span><\/strong><span>\u00a0e a\u00a0<\/span><strong><span>velocidade do fluido<\/span><\/strong><span>\u00a0a\u00a0<strong>granel<\/strong>\u00a0.<\/span><\/p>\n<p><span>Tipicamente, o\u00a0<\/span><strong><span>coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o<\/span><\/strong><span>\u00a0para\u00a0<\/span><a title=\"Fluxo Laminar - Fluxo Viscoso\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-fluxo-laminar-fluxo-viscoso-definicao\/\"><strong><span>fluxo laminar<\/span><\/strong><\/a><span>\u00a0\u00e9 relativamente baixo comparado com o\u00a0<\/span><strong><span>coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o<\/span><\/strong><span>\u00a0para\u00a0<\/span><a title=\"Fluxo turbulento\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-fluxo-turbulento-definicao\/\"><strong><span>fluxo turbulento<\/span><\/strong><\/a><span>\u00a0.\u00a0Isto \u00e9 devido ao fluxo turbulento que possui uma\u00a0<\/span><strong><span>camada de filme fluido estagnada mais fina<\/span><\/strong><span>\u00a0na superf\u00edcie de transfer\u00eancia de calor.<\/span><\/p>\n<p><span>Deve-se notar que essa\u00a0<\/span><strong><span>camada de filme fluido estagnado<\/span><\/strong><span>\u00a0desempenha papel crucial para o coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o.\u00a0Observa-se que o fluido para\u00a0<\/span><strong><span>completamente na superf\u00edcie<\/span><\/strong><span>\u00a0e assume velocidade zero em rela\u00e7\u00e3o \u00e0 superf\u00edcie.\u00a0Esse fen\u00f4meno \u00e9 conhecido como condi\u00e7\u00e3o antiderrapante e, portanto,\u00a0<\/span><strong><span>na superf\u00edcie,<\/span><\/strong><span>\u00a0o fluxo de energia ocorre\u00a0<\/span><strong><span>puramente por condu\u00e7\u00e3o.\u00a0<\/span><\/strong><span>Por\u00e9m, nas pr\u00f3ximas camadas, ocorrem movimentos de condu\u00e7\u00e3o e difus\u00e3o-massa no n\u00edvel molecular ou no n\u00edvel macrosc\u00f3pico.\u00a0Devido ao movimento de massa, a taxa de transfer\u00eancia de energia \u00e9 maior.\u00a0Como foi escrito, a\u00a0<\/span><strong><span>ebuli\u00e7\u00e3o nucleada<\/span><\/strong><span>na superf\u00edcie interrompe efetivamente essa camada estagnada e, portanto, a ebuli\u00e7\u00e3o nucleada aumenta significativamente a capacidade de uma superf\u00edcie de transferir\u00a0<\/span><a href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-energia-interna-energia-termica-definicao\/\"><span>energia t\u00e9rmica<\/span><\/a><span>\u00a0para o fluido a granel.<\/span><\/p>\n<p><span>Um fen\u00f4meno semelhante ocorre para a temperatura.\u00a0Observa-se que a temperatura do fluido na superf\u00edcie e na superf\u00edcie ter\u00e1 a mesma\u00a0<\/span><a title=\"O que \u00e9 temperatura - F\u00edsica\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-temperatura-fisica-definicao\/\"><span>temperatura<\/span><\/a><span>\u00a0no ponto de contato.\u00a0Esse fen\u00f4meno \u00e9 conhecido como condi\u00e7\u00e3o sem salto de temperatura e \u00e9 muito importante para a teoria da ebuli\u00e7\u00e3o de nucleados\u00a0<\/span><strong><span>.<\/span><\/strong><\/p>\n<p><span>Os valores do\u00a0<\/span><strong><span>coeficiente de transfer\u00eancia de calor<\/span><\/strong><span> , h, foram medidos e tabulados para os fluidos e situa\u00e7\u00f5es de fluxo comumente encontrados que ocorrem durante a transfer\u00eancia de calor por convec\u00e7\u00e3o.<\/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-accordion\">\n<div class=\"su-spoiler su-spoiler-style-default su-spoiler-icon-plus su-spoiler-closed\"><\/div>\n<\/div>\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>N\u00famero Nusselt<\/span><\/h2>\n<p><span>O\u00a0<\/span><strong><span>n\u00famero de Nusselt<\/span><\/strong><span>\u00a0\u00e9 um n\u00famero sem dimens\u00e3o, com o nome de um engenheiro alem\u00e3o Wilhelm Nusselt.\u00a0O\u00a0<\/span><strong><span>n\u00famero de Nusselt<\/span><\/strong><span>\u00a0est\u00e1 intimamente relacionado ao\u00a0<\/span><a title=\"O que \u00e9 o n\u00famero P\u00e9clet\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/heat-transfer\/introduction-to-heat-transfer\/characteristic-numbers\/what-is-peclet-number\/\"><span>n\u00famero de P\u00e9clet<\/span><\/a><span>\u00a0e os dois n\u00fameros s\u00e3o usados \u200b\u200bpara descrever a propor\u00e7\u00e3o da\u00a0<\/span><strong><span>energia t\u00e9rmica convectada<\/span><\/strong><span>\u00a0ao fluido pela\u00a0<\/span><strong><span>energia t\u00e9rmica conduzida<\/span><\/strong><span>\u00a0dentro do fluido.\u00a0<\/span><strong><span>O n\u00famero de Nusselt<\/span><\/strong><span>\u00a0\u00e9 igual ao\u00a0<\/span><strong><span>gradiente de temperatura<\/span><\/strong><span>\u00a0adimensional\u00a0na superf\u00edcie e fornece uma medida da transfer\u00eancia de calor por convec\u00e7\u00e3o que ocorre na superf\u00edcie.\u00a0O componente condutor \u00e9 medido nas mesmas condi\u00e7\u00f5es da convec\u00e7\u00e3o de calor, mas com um fluido estagnado.\u00a0O\u00a0<\/span><strong><span>n\u00famero de Nusselt<\/span><\/strong><span>\u00e9 para a camada limite t\u00e9rmica qual \u00e9 o coeficiente de atrito para a camada limite de velocidade.\u00a0Assim, o n\u00famero de Nusselt \u00e9 definido como:<\/span><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Nusselt-Number-definition.png\"><img loading=\"lazy\" class=\"aligncenter size-medium wp-image-20391 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Nusselt-Number-definition-300x270.png\" alt=\"N\u00famero de Nusselt - defini\u00e7\u00e3o\" width=\"300\" height=\"270\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Nusselt-Number-definition-300x270.png\" \/><\/a><\/p>\n<p><span>Onde:<\/span><\/p>\n<p><strong><em><span>k\u00a0<\/span><\/em><\/strong><strong><em><sub><span>f<\/span><\/sub><\/em><\/strong><span>\u00a0\u00e9<\/span><a href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-condutividade-termica-definicao\/\"><strong><span>\u00a0a condutividade t\u00e9rmica<\/span><\/strong><\/a><span>\u00a0do fluido [W \/ mK]<\/span><\/p>\n<p><strong><em><span>L<\/span><\/em><\/strong><span>\u00a0\u00e9 o<\/span><strong><span>\u00a0comprimento caracter\u00edstico<\/span><\/strong><\/p>\n<p><strong><em><span>h<\/span><\/em><\/strong><span>\u00a0\u00e9 o<\/span><strong><span>\u00a0coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o<\/span><\/strong><span>\u00a0[W \/ m<\/span><sup><span>\u00a02<\/span><\/sup><span>\u00a0.K]<\/span><\/p>\n<p><span>Para ilustra\u00e7\u00e3o, considere uma camada fluida de espessura\u00a0<\/span><strong><span>L<\/span><\/strong><span>\u00a0e diferen\u00e7a de temperatura\u00a0<\/span><strong><span>\u0394T<\/span><\/strong><span>\u00a0.\u00a0A transfer\u00eancia de calor atrav\u00e9s da camada de fluido ser\u00e1 por convec\u00e7\u00e3o quando o fluido envolver algum movimento e por condu\u00e7\u00e3o quando a camada de fluido estiver im\u00f3vel.<\/span><\/p>\n<p><span>No caso de\u00a0<\/span><a title=\"Condu\u00e7\u00e3o T\u00e9rmica - Condu\u00e7\u00e3o T\u00e9rmica\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-conducao-termica-conducao-termica-definicao\/\"><span>condu\u00e7\u00e3o<\/span><\/a><span>\u00a0, o\u00a0<\/span><a title=\"Densidade do fluxo de calor - Fluxo t\u00e9rmico\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/heat-transfer\/introduction-to-heat-transfer\/heat-flux-density-thermal-flux\/\"><span>fluxo de calor<\/span><\/a><span>\u00a0pode ser calculado usando\u00a0<\/span><a title=\"Lei de Fourier de condu\u00e7\u00e3o t\u00e9rmica\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-a-lei-de-conducao-termica-de-fourier-definicao\/\"><span>a lei de condu\u00e7\u00e3o de Fourier<\/span><\/a><span>\u00a0.\u00a0Em caso de convec\u00e7\u00e3o, o fluxo de calor pode ser calculado usando a lei de Newton de resfriamento.\u00a0Tomando a sua propor\u00e7\u00e3o d\u00e1:<\/span><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nusselt-number-convection-to-conduction.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20394 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nusselt-number-convection-to-conduction.png\" alt=\"n\u00famero nusselt - convec\u00e7\u00e3o para condu\u00e7\u00e3o\" width=\"353\" height=\"227\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nusselt-number-convection-to-conduction.png\" \/><\/a><\/p>\n<p><span>A equa\u00e7\u00e3o anterior define o\u00a0<\/span><strong><span>n\u00famero de Nusselt<\/span><\/strong><span>\u00a0.\u00a0Portanto, o\u00a0<\/span><strong><span>n\u00famero de Nusselt<\/span><\/strong><span>\u00a0representa o aprimoramento da transfer\u00eancia de calor atrav\u00e9s de uma camada de fluido como resultado da\u00a0<\/span><strong><span>convec\u00e7\u00e3o relativa \u00e0 condu\u00e7\u00e3o<\/span><\/strong><span>\u00a0atrav\u00e9s da mesma camada de fluido.\u00a0Um\u00a0<\/span><strong><span>n\u00famero Nusselt<\/span><\/strong><span>\u00a0de\u00a0<\/span><strong><span>Nu = 1<\/span><\/strong><span>\u00a0para uma camada de fluido representa a transfer\u00eancia de calor atrav\u00e9s da camada por\u00a0<\/span><strong><span>pura condu\u00e7\u00e3o<\/span><\/strong><span>\u00a0.\u00a0Quanto maior o\u00a0<\/span><strong><span>n\u00famero de Nusselt<\/span><\/strong><span>\u00a0, mais eficaz \u00e9 a convec\u00e7\u00e3o.\u00a0Um n\u00famero maior de Nusselt corresponde a uma convec\u00e7\u00e3o mais eficaz, com fluxo turbulento tipicamente na faixa de 100 a 1000.\u00a0Para escoamentos turbulentos, o\u00a0<\/span><strong><span>n\u00famero de Nusselt<\/span><\/strong><span>\u00a0geralmente \u00e9 uma fun\u00e7\u00e3o 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>\u00a0e da<\/span><a title=\"O que \u00e9 o n\u00famero Prandtl\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/heat-transfer\/introduction-to-heat-transfer\/characteristic-numbers\/what-is-prandtl-number\/\"><span>N\u00famero Prandtl<\/span><\/a><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>Exemplo &#8211; Transfer\u00eancia de calor por convec\u00e7\u00e3o &#8211; Temperatura da superf\u00edcie do revestimento<\/span><\/h2>\n<p><strong><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Convection-Convective-Heat-Transfer-example.png\"><img loading=\"lazy\" class=\"alignright size-medium wp-image-20406 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Convection-Convective-Heat-Transfer-example-275x300.png\" alt=\"Convec\u00e7\u00e3o - Transfer\u00eancia de calor por convec\u00e7\u00e3o\" width=\"275\" height=\"300\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Convection-Convective-Heat-Transfer-example-275x300.png\" \/><\/a><span>O<\/span><\/strong><span>\u00a0revestimento \u00e9 a camada externa das barras de combust\u00edvel, situada entre o\u00a0<\/span><strong><span>l\u00edquido de arrefecimento<\/span><\/strong><span>\u00a0do\u00a0<strong>reator<\/strong>\u00a0e o\u00a0<\/span><a title=\"Combust\u00edvel nuclear\" href=\"https:\/\/www.nuclear-power.com\/nuclear-power-plant\/nuclear-fuel\/\"><strong><span>combust\u00edvel nuclear<\/span><\/strong>\u00a0<\/a><span>(isto \u00e9,\u00a0<\/span><strong><span>granulados de combust\u00edvel<\/span><\/strong><span>\u00a0).\u00a0\u00c9 feito de um material resistente \u00e0 corros\u00e3o com se\u00e7\u00e3o transversal de baixa absor\u00e7\u00e3o para\u00a0<\/span><a title=\"N\u00eautron t\u00e9rmico\" href=\"https:\/\/www.nuclear-power.com\/nuclear-power\/reactor-physics\/atomic-nuclear-physics\/fundamental-particles\/neutron\/thermal-neutron\/\"><span>n\u00eautrons t\u00e9rmicos<\/span><\/a><span>\u00a0, geralmente\u00a0<\/span><strong><span>liga de zirc\u00f4nio<\/span><\/strong><span>\u00a0.\u00a0<\/span><strong><span>O revestimento<\/span><\/strong><span>\u00a0evita que produtos de fiss\u00e3o radioativa escapem da matriz de combust\u00edvel para o l\u00edquido de arrefecimento do reator e os contaminem.\u00a0O revestimento constitui uma das barreiras na\u00a0abordagem de\u00a0&#8216;\u00a0<\/span><strong><span>defesa em profundidade<\/span><\/strong><span>\u00a0&#8216;; portanto, sua capacidade de\u00a0<\/span><strong><span>refrigera\u00e7\u00e3o<\/span><\/strong><span>\u00a0\u00e9 um dos principais aspectos de seguran\u00e7a.<\/span><\/p>\n<p><span>Considere o revestimento de combust\u00edvel do raio interno\u00a0<\/span><strong><span>r\u00a0<\/span><\/strong><strong><sub><span>Zr, 2<\/span><\/sub><\/strong><strong><span>\u00a0= 0,408 cm<\/span><\/strong><span>\u00a0e raio externo\u00a0<\/span><strong><span>r\u00a0<\/span><\/strong><strong><sub><span>Zr, 1<\/span><\/sub><\/strong><strong><span>\u00a0= 0,465 cm<\/span><\/strong><span>\u00a0.\u00a0Em compara\u00e7\u00e3o com o pellet de combust\u00edvel, quase n\u00e3o h\u00e1 gera\u00e7\u00e3o de calor no revestimento de combust\u00edvel (o revestimento \u00e9\u00a0<\/span><a href=\"https:\/\/www.nuclear-power.com\/nuclear-power\/fission\/energy-release-from-fission\/\"><span>levemente aquecido pela radia\u00e7\u00e3o<\/span><\/a><span>\u00a0).\u00a0Todo o calor gerado no combust\u00edvel deve ser transferido por\u00a0<\/span><a title=\"Condu\u00e7\u00e3o T\u00e9rmica - Condu\u00e7\u00e3o T\u00e9rmica\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-conducao-termica-conducao-termica-definicao\/\"><strong><span>condu\u00e7\u00e3o<\/span><\/strong><\/a><span>\u00a0atrav\u00e9s do revestimento e, portanto, a superf\u00edcie interna \u00e9 mais quente que a superf\u00edcie externa.<\/span><\/p>\n<p><span>Assuma isso:<\/span><\/p>\n<ul>\n<li><span>o di\u00e2metro externo do revestimento \u00e9:\u00a0<\/span><strong><span>d = 2 xr\u00a0<\/span><sub><span>Zr, 1<\/span><\/sub><span>\u00a0= 9,3 mm<\/span><\/strong><\/li>\n<li><span>o passo dos pinos de combust\u00edvel \u00e9:\u00a0<\/span><strong><span>p = 13 mm<\/span><\/strong><\/li>\n<li><span>a\u00a0<\/span><a title=\"Condutividade t\u00e9rmica\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-condutividade-termica-definicao\/\"><span>condutividade t\u00e9rmica<\/span><\/a><span>\u00a0da\u00a0<\/span><a title=\"L\u00edquido saturado e sub-resfriado\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/materials-nuclear-engineering\/properties-steam-what-is-steam\/saturated-and-subcooled-liquid\/\"><span>\u00e1gua saturada<\/span><\/a><span>\u00a0a 300 \u00b0 C \u00e9:\u00a0<\/span><strong><span>k\u00a0<\/span><\/strong><strong><sub><span>H2O<\/span><\/sub><\/strong><strong><span>\u00a0= 0,545 W \/ mK<\/span><\/strong><\/li>\n<li><span>a viscosidade din\u00e2mica da \u00e1gua saturada a 300 \u00b0 C \u00e9:\u00a0<\/span><strong><span>\u03bc = 0,0000859 Ns \/ m\u00a0<\/span><\/strong><strong><sup><span>2<\/span><\/sup><\/strong><\/li>\n<li><span>a\u00a0<\/span><a title=\"O que \u00e9 densidade - F\u00edsica\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/thermodynamics\/thermodynamic-properties\/what-is-density-physics\/\"><span>densidade<\/span><\/a><span>\u00a0do fluido\u00a0\u00e9:\u00a0<\/span><strong><span>\u03c1 = 714 kg \/ m\u00a0<\/span><\/strong><strong><sup><span>3<\/span><\/sup><\/strong><\/li>\n<li><span>o\u00a0<\/span><a href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/thermodynamics\/laws-of-thermodynamics\/first-law-of-thermodynamics\/heat-capacity\/\"><strong><span>calor espec\u00edfico<\/span><\/strong><\/a><span>\u00a0\u00e9:\u00a0<\/span><strong><span>c\u00a0<\/span><\/strong><strong><sub><span>p<\/span><\/sub><\/strong><strong><span>\u00a0= 5,65 kJ \/ kg.K<\/span><\/strong><\/li>\n<li><span>a velocidade de fluxo do n\u00facleo \u00e9 constante e igual a\u00a0<\/span><strong><span>V\u00a0<\/span><\/strong><strong><sub><span>core<\/span><\/sub><\/strong><strong><span>\u00a0= 5 m \/ s<\/span><\/strong><\/li>\n<li><span>a temperatura do l\u00edquido de arrefecimento do reator nesta coordenada axial \u00e9:\u00a0<\/span><strong><span>T a\u00a0<\/span><\/strong><strong><sub><span>granel<\/span><\/sub><\/strong><strong><span>\u00a0= 296 \u00b0 C<\/span><\/strong><\/li>\n<li><span>a taxa linear de calor do combust\u00edvel \u00e9\u00a0<\/span><strong><span>q\u00a0<\/span><\/strong><strong><sub><span>L<\/span><\/sub><\/strong><strong><span>\u00a0= 300 W \/ cm<\/span><\/strong><span>\u00a0(F\u00a0<\/span><sub><span>Q<\/span><\/sub><span>\u00a0\u2248 2.0) e, portanto, a taxa volum\u00e9trica de calor \u00e9 q\u00a0<\/span><sub><span>V<\/span><\/sub><span>\u00a0= 597 x 10\u00a0<\/span><sup><span>6<\/span><\/sup><span>\u00a0W \/ m\u00a0<\/span><sup><span>3<\/span><\/sup><\/li>\n<\/ul>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Hydraulic-Diameter-Fuel-Channel.png\"><img loading=\"lazy\" class=\"alignright size-medium wp-image-20407 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Hydraulic-Diameter-Fuel-Channel-254x300.png\" alt=\"Di\u00e2metro hidr\u00e1ulico - canal de combust\u00edvel\" width=\"254\" height=\"300\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Hydraulic-Diameter-Fuel-Channel-254x300.png\" \/><\/a><span>Calcule o n\u00famero de\u00a0<\/span><a title=\"O que \u00e9 o n\u00famero Prandtl\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/heat-transfer\/introduction-to-heat-transfer\/characteristic-numbers\/what-is-prandtl-number\/\"><span>Prandtl<\/span><\/a><span>\u00a0,\u00a0<\/span><a title=\"N\u00famero de Reynolds\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/fluid-dynamics\/reynolds-number\/\"><span>Reynolds<\/span><\/a><span>\u00a0e Nusselt para esse regime de fluxo (fluxo turbulento for\u00e7ado interno) dentro da estrutura retangular de combust\u00edvel (canal de combust\u00edvel), depois calcule o\u00a0<\/span><strong><span>coeficiente de transfer\u00eancia de calor<\/span><\/strong><span>\u00a0e, finalmente, a\u00a0<\/span><strong><span>temperatura da superf\u00edcie<\/span><\/strong><span>\u00a0do\u00a0<strong>revestimento<\/strong>\u00a0,\u00a0<\/span><strong><span>T\u00a0<\/span><sub><span>Zr, 1<\/span><\/sub><\/strong><span>\u00a0.<\/span><\/p>\n<p><span>Para calcular a\u00a0<\/span><strong><span>temperatura da superf\u00edcie<\/span><\/strong><span>\u00a0do\u00a0<strong>revestimento<\/strong>\u00a0, precisamos calcular o n\u00famero de\u00a0<\/span><strong><span>Prandtl<\/span><\/strong><span>\u00a0,\u00a0<\/span><strong><span>Reynolds<\/span><\/strong><span>\u00a0e\u00a0<\/span><strong><span>Nusselt<\/span><\/strong><span>\u00a0, porque a transfer\u00eancia de calor para esse regime de fluxo pode ser descrita pela\u00a0<\/span><strong><span>equa\u00e7\u00e3o de Dittus-Boelter<\/span><\/strong><span>\u00a0, que \u00e9:<\/span><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Dittus-Boelter-Equation-Formula.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20409 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Dittus-Boelter-Equation-Formula.png\" alt=\"Equa\u00e7\u00e3o de Dittus-Boelter - F\u00f3rmula\" width=\"556\" height=\"278\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Dittus-Boelter-Equation-Formula.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>C\u00e1lculo do n\u00famero Prandtl<\/span><\/h2>\n<p><span>Para calcular o\u00a0<\/span><a title=\"O que \u00e9 o n\u00famero Prandtl\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/heat-transfer\/introduction-to-heat-transfer\/characteristic-numbers\/what-is-prandtl-number\/\"><span>n\u00famero Prandtl<\/span><\/a><span>\u00a0, precisamos saber:<\/span><\/p>\n<ul>\n<li><span>a condutividade t\u00e9rmica da \u00e1gua saturada a 300 \u00b0 C \u00e9:\u00a0<\/span><strong><span>k\u00a0<\/span><\/strong><strong><sub><span>H2O<\/span><\/sub><\/strong><strong><span>\u00a0= 0,545 W \/ mK<\/span><\/strong><\/li>\n<li><span>a viscosidade din\u00e2mica da \u00e1gua saturada a 300 \u00b0 C \u00e9:\u00a0<\/span><strong><span>\u03bc = 0,0000859 Ns \/ m\u00a0<\/span><\/strong><strong><sup><span>2<\/span><\/sup><\/strong><\/li>\n<li><span>o\u00a0<\/span><a href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/thermodynamics\/laws-of-thermodynamics\/first-law-of-thermodynamics\/heat-capacity\/\"><strong><span>calor espec\u00edfico<\/span><\/strong><\/a><span>\u00a0\u00e9:\u00a0<\/span><strong><span>c\u00a0<\/span><\/strong><strong><sub><span>p<\/span><\/sub><\/strong><strong><span>\u00a0= 5,65 kJ \/ kg.K<\/span><\/strong><\/li>\n<\/ul>\n<p><span>Observe que todos esses par\u00e2metros diferem significativamente para a \u00e1gua a 300 \u00b0 C daqueles a 20 \u00b0 C.\u00a0O n\u00famero de prandtl para\u00a0<\/span><a href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/materials-nuclear-engineering\/properties-of-water\/\"><span>\u00e1gua<\/span><\/a><span>\u00a0a 20 \u00b0 C \u00e9 de cerca de\u00a0<\/span><strong><span>6,91.\u00a0<\/span><\/strong><span>O n\u00famero de Prandtl para o l\u00edquido de refrigera\u00e7\u00e3o do reator a 300 \u00b0 C \u00e9 ent\u00e3o:<\/span><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/prandtl-number-example.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20411 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/prandtl-number-example.png\" alt=\"n\u00famero prandtl - exemplo\" width=\"469\" height=\"80\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/prandtl-number-example.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>C\u00e1lculo do n\u00famero de Reynolds<\/span><\/h2>\n<p><span>Para calcular o n\u00famero de Reynolds, precisamos saber:<\/span><\/p>\n<ul>\n<li><span>o di\u00e2metro externo do revestimento \u00e9:\u00a0<\/span><strong><span>d = 2 xr\u00a0<\/span><sub><span>Zr, 1<\/span><\/sub><span>\u00a0= 9,3 mm<\/span><\/strong><span>\u00a0(para calcular o di\u00e2metro hidr\u00e1ulico)<\/span><\/li>\n<li><span>o passo dos pinos de combust\u00edvel \u00e9:\u00a0<\/span><strong><span>p = 13 mm<\/span><\/strong><span>\u00a0\u00a0(para calcular o di\u00e2metro hidr\u00e1ulico)<\/span><\/li>\n<li><span>a viscosidade din\u00e2mica da \u00e1gua saturada a 300 \u00b0 C \u00e9:\u00a0<\/span><strong><span>\u03bc = 0,0000859 Ns \/ m\u00a0<\/span><\/strong><strong><sup><span>2<\/span><\/sup><\/strong><\/li>\n<li><span>a densidade do fluido \u00e9:\u00a0<\/span><strong><span>\u03c1 = 714 kg \/ m\u00a0<\/span><\/strong><strong><sup><span>3<\/span><\/sup><\/strong><\/li>\n<\/ul>\n<p><strong><span>O di\u00e2metro hidr\u00e1ulico, D\u00a0<\/span><\/strong><strong><sub><span>h<\/span><\/sub><\/strong><span>\u00a0, \u00e9 um termo comumente usado ao manipular o fluxo em\u00a0<\/span><strong><span>tubos e canais n\u00e3o circulares<\/span><\/strong><span>\u00a0.\u00a0O\u00a0<\/span><strong><span>di\u00e2metro hidr\u00e1ulico do canal de combust\u00edvel<\/span><\/strong><span>\u00a0,\u00a0<\/span><em><span>D\u00a0<\/span><\/em><em><sub><span>h<\/span><\/sub><\/em><span>\u00a0, \u00e9 igual a 13,85 mm.<\/span><\/p>\n<p><span>Veja tamb\u00e9m:\u00a0<\/span><a title=\"Di\u00e2metro hidr\u00e1ulico\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/fluid-dynamics\/internal-flow\/hydraulic-diameter-2\/\"><span>Di\u00e2metro hidr\u00e1ulico<\/span><\/a><\/p>\n<p><span>O\u00a0<\/span><strong><span>n\u00famero de Reynolds<\/span><\/strong><span>\u00a0dentro do canal de combust\u00edvel \u00e9 ent\u00e3o igual a:<\/span><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/reynolds-number-example.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20412 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/reynolds-number-example.png\" alt=\"n\u00famero de reynolds - exemplo\" width=\"593\" height=\"78\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/reynolds-number-example.png\" \/><\/a><\/p>\n<p><span>Isso satisfaz plenamente as\u00a0<\/span><a title=\"Fluxo turbulento\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-fluxo-turbulento-definicao\/\"><strong><span>condi\u00e7\u00f5es turbulentas<\/span><\/strong><\/a><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>C\u00e1lculo do n\u00famero de Nusselt usando a equa\u00e7\u00e3o de Dittus-Boelter<\/span><\/h2>\n<p><span>Para um fluxo turbulento totalmente desenvolvido (hidrodinamicamente e termicamente) em um tubo circular liso, o\u00a0<\/span><strong><span>n\u00famero<\/span><\/strong><span>\u00a0local de\u00a0<strong>Nusselt<\/strong>\u00a0pode ser obtido a partir da conhecida\u00a0<\/span><strong><span>equa\u00e7\u00e3o Dittus\u00ae Boelter<\/span><\/strong><span>\u00a0.<\/span><\/p>\n<p><span>Para calcular o\u00a0<\/span><strong><span>n\u00famero de Nusselt<\/span><\/strong><span>\u00a0, precisamos saber:<\/span><\/p>\n<ul>\n<li><span>o\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, que \u00e9\u00a0<\/span><strong><span>Re\u00a0<\/span><sub><span>Dh<\/span><\/sub><span>\u00a0= 575600<\/span><\/strong><\/li>\n<li><span>o\u00a0<\/span><a title=\"O que \u00e9 o n\u00famero Prandtl\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/heat-transfer\/introduction-to-heat-transfer\/characteristic-numbers\/what-is-prandtl-number\/\"><span>n\u00famero Prandtl<\/span><\/a><span>\u00a0, que \u00e9\u00a0<\/span><strong><span>Pr = 0,89<\/span><\/strong><\/li>\n<\/ul>\n<p><span>O\u00a0<\/span><strong><span>n\u00famero de Nusselt<\/span><\/strong><span>\u00a0para a convec\u00e7\u00e3o for\u00e7ada dentro do canal de combust\u00edvel \u00e9 ent\u00e3o igual a:<\/span><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nusselt-number-example.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20413 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nusselt-number-example.png\" alt=\"n\u00famero nusselt - exemplo\" width=\"387\" height=\"58\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/nusselt-number-example.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>C\u00e1lculo do coeficiente de transfer\u00eancia de calor e da temperatura da superf\u00edcie do revestimento, T\u00a0<\/span><sub><span>Zr, 1<\/span><\/sub><\/h2>\n<p><span>O conhecimento detalhado da geometria, par\u00e2metros do fluido, raio externo do revestimento, taxa de calor linear, coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o nos permite calcular a diferen\u00e7a de temperatura\u00a0<\/span><strong><span>\u2206T<\/span><\/strong><span>\u00a0entre o l\u00edquido de arrefecimento (T a\u00a0<\/span><sub><span>granel<\/span><\/sub><span>\u00a0) e a superf\u00edcie do revestimento (T\u00a0<\/span><sub><span>Zr, 1<\/span><\/sub><span>\u00a0).<\/span><\/p>\n<p><span>Para calcular a temperatura da superf\u00edcie do revestimento, precisamos saber:<\/span><\/p>\n<ul>\n<li><span>o di\u00e2metro externo do revestimento \u00e9: d = 2 x\u00a0<\/span><strong><span>r\u00a0<\/span><\/strong><strong><sub><span>Zr, 1<\/span><\/sub><\/strong><strong><span>\u00a0= 9,3 mm<\/span><\/strong><\/li>\n<li><span>o n\u00famero de Nusselt, que \u00e9\u00a0<\/span><strong><span>Nu\u00a0<\/span><\/strong><strong><sub><span>Dh<\/span><\/sub><\/strong><strong><span>\u00a0= 890<\/span><\/strong><\/li>\n<li><span>o di\u00e2metro hidr\u00e1ulico do canal de combust\u00edvel \u00e9:\u00a0<\/span><strong><em><span>D\u00a0<\/span><\/em><\/strong><strong><em><sub><span>h<\/span><\/sub><\/em><\/strong><strong><span>\u00a0= 13,85 mm<\/span><\/strong><\/li>\n<li><span>a condutividade t\u00e9rmica do l\u00edquido de refrigera\u00e7\u00e3o do reator (300 \u00b0 C) \u00e9:\u00a0<\/span><strong><span>k\u00a0<\/span><\/strong><strong><sub><span>H2O<\/span><\/sub><\/strong><strong><span>\u00a0= 0,545 W \/ mK<\/span><\/strong><\/li>\n<li><span>a temperatura a granel do l\u00edquido de refrigera\u00e7\u00e3o do reator nesta coordenada axial \u00e9:\u00a0<\/span><strong><span>T a\u00a0<\/span><\/strong><strong><sub><span>granel<\/span><\/sub><\/strong><strong><span>\u00a0= 296 \u00b0 C<\/span><\/strong><\/li>\n<li><span>a taxa linear de calor do combust\u00edvel \u00e9:\u00a0<\/span><strong><span>q\u00a0<\/span><\/strong><strong><sub><span>L<\/span><\/sub><\/strong><strong><span>\u00a0= 300 W \/ cm<\/span><\/strong><span>\u00a0(F\u00a0<\/span><sub><span>Q<\/span><\/sub><span>\u00a0\u2248 2.0)<\/span><\/li>\n<\/ul>\n<p><span>O coeficiente de transfer\u00eancia de calor convectivo,\u00a0<\/span><strong><span>h<\/span><\/strong><span>\u00a0, \u00e9 dado diretamente pela defini\u00e7\u00e3o do n\u00famero de Nusselt:<\/span><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/convective-heat-transfer-coefficient-example.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20410 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/convective-heat-transfer-coefficient-example.png\" alt=\"coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o - exemplo\" width=\"619\" height=\"92\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/convective-heat-transfer-coefficient-example.png\" \/><\/a><\/p>\n<p><span>Finalmente, podemos calcular a temperatura da superf\u00edcie do revestimento (T\u00a0<\/span><sub><span>Zr, 1<\/span><\/sub><span>\u00a0) simplesmente usando a\u00a0<\/span><strong><span>Lei de Newton de resfriamento<\/span><\/strong><span>\u00a0:<\/span><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Newton-law-of-cooling-example.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-20408 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Newton-law-of-cooling-example.png\" alt=\"Lei de Newton do resfriamento - exemplo\" width=\"377\" height=\"369\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Newton-law-of-cooling-example.png\" \/><\/a><\/p>\n<p><span>Para PWRs em opera\u00e7\u00e3o normal, h\u00e1\u00a0<\/span><a href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/materials-nuclear-engineering\/properties-steam-what-is-steam\/saturated-and-subcooled-liquid\/\"><span>\u00e1gua l\u00edquida comprimida<\/span><\/a><span>\u00a0dentro do n\u00facleo do reator, loops e geradores de vapor.\u00a0A press\u00e3o \u00e9 mantida em aproximadamente\u00a0<\/span><strong><span>16MPa<\/span><\/strong><span>\u00a0.\u00a0A essa press\u00e3o, a \u00e1gua ferve a aproximadamente\u00a0<\/span><strong><span>350 \u00b0 C<\/span><\/strong><span>\u00a0(662 \u00b0 F).\u00a0Como pode ser visto, a temperatura da superf\u00edcie T\u00a0<\/span><sub><span>Zr, 1<\/span><\/sub><span>\u00a0= 325 \u00b0 C garante que mesmo a ebuli\u00e7\u00e3o sub-resfriada n\u00e3o ocorra.\u00a0Observe que a ebuli\u00e7\u00e3o sub-resfriada requer T\u00a0<\/span><sub><span>Zr, 1<\/span><\/sub><span>\u00a0= T\u00a0<\/span><sub><span>sat<\/span><\/sub><span>\u00a0.\u00a0Como as temperaturas de entrada da \u00e1gua s\u00e3o geralmente de cerca de\u00a0<\/span><strong><span>290 \u00b0 C<\/span><\/strong><span>(554 \u00b0 F), \u00e9 \u00f3bvio que este exemplo corresponde \u00e0 parte inferior do n\u00facleo.\u00a0Em eleva\u00e7\u00f5es mais altas do n\u00facleo, a temperatura a granel pode atingir at\u00e9 330 \u00b0 C.\u00a0A diferen\u00e7a de temperatura de 29 \u00b0 C causa a fervura sub-resfriada (330 \u00b0 C + 29 \u00b0 C&gt; 350 \u00b0 C).\u00a0Por outro lado, a\u00a0<\/span><strong><span>ebuli\u00e7\u00e3o nucleada<\/span><\/strong><span>\u00a0na superf\u00edcie interrompe efetivamente a camada estagnada e, portanto, a ebuli\u00e7\u00e3o nucleada aumenta significativamente a capacidade de uma superf\u00edcie de transferir\u00a0<\/span><a href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/thermodynamics\/what-is-energy-physics\/internal-energy-thermal-energy\/\"><span>energia t\u00e9rmica<\/span><\/a><span>\u00a0para o fluido a granel.\u00a0Como resultado, o coeficiente de transfer\u00eancia de calor por convec\u00e7\u00e3o aumenta significativamente e, portanto, em eleva\u00e7\u00f5es mais altas, a diferen\u00e7a de temperatura (T\u00a0<\/span><sub><span>Zr,\u00a0<\/span><\/sub><sub><span>volume\u00a0<\/span><\/sub><span><sub>1<\/sub>\u00a0&#8211; T\u00a0) diminui significativamente.<\/span><\/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 convec\u00e7\u00e3o \u00e9 a transfer\u00eancia de massa ou a transfer\u00eancia de calor devido ao movimento a granel.\u00a0O processo de transfer\u00eancia de calor entre uma superf\u00edcie e um fluido que flui em contato com ela \u00e9 chamado de transfer\u00eancia de calor por convec\u00e7\u00e3o.\u00a0Engenharia T\u00e9rmica O que \u00e9 convec\u00e7\u00e3o Em geral, a\u00a0convec\u00e7\u00e3o\u00a0\u00e9 a\u00a0transfer\u00eancia de massa\u00a0ou a\u00a0transfer\u00eancia de &#8230; <a title=\"O que \u00e9 convec\u00e7\u00e3o &#8211; transfer\u00eancia de calor por convec\u00e7\u00e3o &#8211; defini\u00e7\u00e3o\" class=\"read-more\" href=\"https:\/\/www.thermal-engineering.org\/pt-br\/o-que-e-conveccao-transferencia-de-calor-por-conveccao-definicao\/\" aria-label=\"More on O que \u00e9 convec\u00e7\u00e3o &#8211; transfer\u00eancia de calor por convec\u00e7\u00e3o &#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 convec\u00e7\u00e3o - transfer\u00eancia de calor por convec\u00e7\u00e3o - defini\u00e7\u00e3o<\/title>\n<meta name=\"description\" content=\"A convec\u00e7\u00e3o \u00e9 a transfer\u00eancia de massa ou a transfer\u00eancia de calor devido ao movimento a granel. 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O processo de transfer\u00eancia de calor entre uma superf\u00edcie e um fluido que flui em contato com ela \u00e9 chamado de transfer\u00eancia de calor por convec\u00e7\u00e3o. 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