{"id":41725,"date":"2019-09-29T22:44:55","date_gmt":"2019-09-29T21:44:55","guid":{"rendered":"https:\/\/www.thermal-engineering.org\/que-es-la-correlacion-lockhart-martinelli-definicion\/"},"modified":"2020-01-20T12:35:29","modified_gmt":"2020-01-20T11:35:29","slug":"que-es-la-correlacion-lockhart-martinelli-definicion","status":"publish","type":"post","link":"https:\/\/www.thermal-engineering.org\/es\/que-es-la-correlacion-lockhart-martinelli-definicion\/","title":{"rendered":"\u00bfQu\u00e9 es la correlaci\u00f3n Lockhart-Martinelli? Definici\u00f3n"},"content":{"rendered":"<div class=\"su-quote su-quote-style-default\">\n<div class=\"su-quote-inner su-clearfix\">Correlaci\u00f3n de Lockhart-Martinelli.\u00a0El m\u00e9todo de Lockhart y Martinelli es el m\u00e9todo de flujos separados que predijo la ca\u00edda de presi\u00f3n por fricci\u00f3n en dos fases.\u00a0Ingenieria termal<\/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>Correlaci\u00f3n de Lockhart-Martinelli<\/h2>\n<p>Un enfoque alternativo para calcular la\u00a0<a title=\"Ca\u00edda de presi\u00f3n bif\u00e1sica\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/fluid-dynamics\/two-phase-fluid-flow\/two-phase-pressure-drop\/\">ca\u00edda de presi\u00f3n en dos fases<\/a>\u00a0es\u00a0<strong>el modelo de fases separadas.<\/strong><\/p>\n<p>En este modelo,\u00a0se considera que\u00a0las\u00a0<strong>fases<\/strong>\u00a0fluyen por\u00a0<strong>separado<\/strong>\u00a0en el canal, cada una ocupando una\u00a0<strong>fracci\u00f3n dada<\/strong>\u00a0de la secci\u00f3n transversal del canal y cada una con una\u00a0<strong>velocidad dada<\/strong>\u00a0.\u00a0Es obvio que la predicci\u00f3n de la\u00a0<a title=\"Fracci\u00f3n vac\u00eda: flujo bif\u00e1sico\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/fluid-dynamics\/two-phase-fluid-flow\/void-fraction-two-phase-flow\/\"><strong>fracci\u00f3n vac\u00eda<\/strong><\/a>\u00a0es muy importante para estos m\u00e9todos.\u00a0Numerosos m\u00e9todos est\u00e1n disponibles para predecir la fracci\u00f3n vac\u00eda.<\/p>\n<p>El m\u00e9todo de\u00a0<strong>Lockhart y Martinelli<\/strong>\u00a0es el m\u00e9todo original que predijo la\u00a0<strong>ca\u00edda de presi\u00f3n de fricci\u00f3n en dos fases<\/strong>\u00a0basada en un multiplicador de fricci\u00f3n para la\u00a0<strong>fase l\u00edquida o la fase de vapor<\/strong>\u00a0:<\/p>\n<p><strong>\u2206p\u00a0<sub>frict<\/sub>\u00a0= \u03a6\u00a0<sub>ltt\u00a0<\/sub><sup>2<\/sup>\u00a0.\u00a0\u2206p\u00a0<sub>l<\/sub><\/strong>\u00a0(liquidp en fase l\u00edquida)<\/p>\n<p><strong>\u2206p\u00a0<sub>frict<\/sub>\u00a0= \u03a6\u00a0<sub>gtt\u00a0<\/sub><sup>2<\/sup>\u00a0.\u00a0\u2206p\u00a0<sub>g<\/sub><\/strong>\u00a0(fase de vapor \u2206p)<\/p>\n<p>Los factores de fricci\u00f3n de una sola fase del l\u00edquido\u00a0<strong>f\u00a0<sub>l<\/sub><\/strong>y el vapor\u00a0<strong>f\u00a0<sub>g<\/sub><\/strong>\u00a0se\u00a0<a title=\"Factor de fricci\u00f3n de Darcy\" href=\"https:\/\/www.thermal-engineering.org\/es\/que-es-el-factor-de-friccion-de-darcy-definicion\/\">basan en la \u00fanica fase<\/a>\u00a0que fluye solo en el canal, ya sea en\u00a0<a title=\"Flujo Laminar - Flujo Viscoso\" href=\"https:\/\/www.thermal-engineering.org\/es\/que-es-el-flujo-laminar-flujo-viscoso-definicion\/\">laminar viscoso<\/a>\u00a0(v) o\u00a0<a title=\"Flujo turbulento\" href=\"https:\/\/www.thermal-engineering.org\/es\/que-es-el-flujo-turbulento-definicion\/\">turbulentos<\/a>\u00a0reg\u00edmenes (t).<\/p>\n<p><strong>\u2206p\u00a0<sub>l<\/sub><\/strong>\u00a0se puede calcular de forma cl\u00e1sica, pero con la aplicaci\u00f3n de\u00a0<strong>(1-x)\u00a0<sup>2<\/sup><\/strong>\u00a0en la expresi\u00f3n y\u00a0<strong>\u2206p\u00a0<sub>g<\/sub><\/strong>\u00a0con la aplicaci\u00f3n de la calidad del vapor\u00a0<strong>x\u00a0<sup>2,<\/sup><\/strong>\u00a0respectivamente.<\/p>\n<p>Los multiplicadores de dos fases\u00a0<strong>\u03a6\u00a0<sub>ltt\u00a0<\/sub><sup>2<\/sup><\/strong>\u00a0y\u00a0<strong>\u03a6\u00a0<sub>gtt\u00a0<\/sub><sup>2<\/sup><\/strong>son iguales a:<\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Lockhart-Martinelli-multipliers.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-14904 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Lockhart-Martinelli-multipliers.png\" alt=\"Lockhart-Martinelli - multiplicadores\" width=\"286\" height=\"112\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Lockhart-Martinelli-multipliers.png\" \/><\/a><\/p>\n<p>donde\u00a0<strong>X\u00a0<sub>tt<\/sub><\/strong>es el\u00a0<strong>par\u00e1metro de Martinelli<\/strong>\u00a0definido como:<\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Martinelli-parameter.png\"><img loading=\"lazy\" class=\"aligncenter size-full wp-image-14905 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Martinelli-parameter.png\" alt=\"Par\u00e1metro Martinelli\" width=\"235\" height=\"68\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Martinelli-parameter.png\" \/><\/a><\/p>\n<p><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Lockhart-Martinelli-table.png\"><img loading=\"lazy\" class=\"alignright size-full wp-image-14906 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Lockhart-Martinelli-table.png\" alt=\"Lockhart-Martinelli - mesa\" width=\"250\" height=\"124\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Lockhart-Martinelli-table.png\" \/><\/a>y el valor de\u00a0<strong>C<\/strong>\u00a0en estas ecuaciones depende de los\u00a0<a title=\"R\u00e9gimen de flujo\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/fluid-dynamics\/flow-regime\/\">reg\u00edmenes<\/a>\u00a0de\u00a0<a title=\"Flow Regime\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/fluid-dynamics\/flow-regime\/\">flujo<\/a>\u00a0del l\u00edquido y el vapor.\u00a0Estos valores est\u00e1n en la siguiente tabla.<\/p>\n<p>Se\u00a0ha encontrado que la\u00a0<strong>correlaci\u00f3n Lockhart-Martinelli\u00a0<\/strong>es adecuada para flujos de dos fases a presiones bajas y moderadas.\u00a0Para aplicaciones a presiones m\u00e1s altas, se recomiendan los modelos revisados \u200b\u200bde Martinelli y Nelson (1948) y Thom (1964).<\/p>\n<figure id=\"attachment_14907\" class=\"wp-caption aligncenter\" aria-describedby=\"caption-attachment-14907\"><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/separated-flow-model-Lockhart-Martinelli-correlation.png\"><img loading=\"lazy\" class=\"size-full wp-image-14907 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/separated-flow-model-Lockhart-Martinelli-correlation.png\" alt=\"modelo de flujo separado - correlaci\u00f3n Lockhart-Martinelli\" width=\"512\" height=\"482\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/separated-flow-model-Lockhart-Martinelli-correlation.png\" \/><\/a><\/figure>\n<p>Correlations for void fraction and frictional pressure drop (Lockhart and Martinelli, 1949)<\/p>\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 art\u00edculo se basa en la traducci\u00f3n autom\u00e1tica del art\u00edculo original en ingl\u00e9s. Para m\u00e1s informaci\u00f3n vea el art\u00edculo en ingl\u00e9s. Puedes ayudarnos. Si desea corregir la traducci\u00f3n, env\u00edela a: translations@nuclear-power.com o complete el formulario de traducci\u00f3n en l\u00ednea. Agradecemos su ayuda, actualizaremos la traducci\u00f3n lo antes posible. Gracias.<\/p>\n","protected":false},"excerpt":{"rendered":"<p>Correlaci\u00f3n de Lockhart-Martinelli.\u00a0El m\u00e9todo de Lockhart y Martinelli es el m\u00e9todo de flujos separados que predijo la ca\u00edda de presi\u00f3n por fricci\u00f3n en dos fases.\u00a0Ingenieria termal Correlaci\u00f3n de Lockhart-Martinelli Un enfoque alternativo para calcular la\u00a0ca\u00edda de presi\u00f3n en dos fases\u00a0es\u00a0el modelo de fases separadas. En este modelo,\u00a0se considera que\u00a0las\u00a0fases\u00a0fluyen por\u00a0separado\u00a0en el canal, cada una ocupando &#8230; <a title=\"\u00bfQu\u00e9 es la correlaci\u00f3n Lockhart-Martinelli? Definici\u00f3n\" class=\"read-more\" href=\"https:\/\/www.thermal-engineering.org\/es\/que-es-la-correlacion-lockhart-martinelli-definicion\/\" aria-label=\"M\u00e1s en \u00bfQu\u00e9 es la correlaci\u00f3n Lockhart-Martinelli? Definici\u00f3n\">Leer m\u00e1s<\/a><\/p>\n","protected":false},"author":1,"featured_media":0,"comment_status":"closed","ping_status":"closed","sticky":false,"template":"","format":"standard","meta":[],"categories":[16],"tags":[],"yoast_head":"<!-- This site is optimized with the Yoast SEO plugin v15.4 - https:\/\/yoast.com\/wordpress\/plugins\/seo\/ -->\n<title>\u00bfQu\u00e9 es la correlaci\u00f3n Lockhart-Martinelli? Definici\u00f3n<\/title>\n<meta name=\"description\" content=\"Correlaci\u00f3n de Lockhart-Martinelli. El m\u00e9todo de Lockhart y Martinelli es el m\u00e9todo de flujos separados que predijo la ca\u00edda de presi\u00f3n por fricci\u00f3n en dos fases. 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