{"id":16369,"date":"2002-11-04T00:00:00","date_gmt":"2002-11-04T00:00:00","guid":{"rendered":"https:\/\/www.deberes.net\/tesis\/sin-categoria\/transferencia-de-masa-y-calor-en-gotas-en-procesos-de-absorcion-con-nitrato-de-litio-amoniaco-nuevas-tecnologa%c2%adas\/"},"modified":"2002-11-04T00:00:00","modified_gmt":"2002-11-04T00:00:00","slug":"transferencia-de-masa-y-calor-en-gotas-en-procesos-de-absorcion-con-nitrato-de-litio-amoniaco-nuevas-tecnologa%c2%adas","status":"publish","type":"post","link":"https:\/\/www.deberes.net\/tesis\/fisica\/transferencia-de-masa-y-calor-en-gotas-en-procesos-de-absorcion-con-nitrato-de-litio-amoniaco-nuevas-tecnologa%c2%adas\/","title":{"rendered":"Transferencia de masa y calor en gotas en procesos de absorci\u00f3n con nitrato de litio-amoniaco: nuevas tecnolog\u00edas"},"content":{"rendered":"<h2>Tesis doctoral de <strong>  Venegas Bernal M. Carmen <\/strong><\/h2>\n<p>Se parte del estudio termodin\u00e1mico de las disoluciones h2o-nh3, lino3-nh3 y nascn-nh3, y su comportamiento como fluidos de trabajo en ciclos de absorci\u00f3n para la revalorizaci\u00f3n de calor residual, a temperaturas comprendidas entre los 60\u00c2\u00bac y 100\u00c2\u00bac, utilizando como fuente de calor para producir fr\u00edo a temperaturas bajo cero con destino a aplicaciones industriales. De este an\u00e1lisis se deduce que para la climatolog\u00eda de la pen\u00ednsula ib\u00e9rica la disoluci\u00f3n lino3-nh3, es la que ofrece mejores resultados.  se configura un modelo f\u00edsico para investigar la transferencia de calor y masa entre gotas esf\u00e9ricas de disoluci\u00f3n y refrigerante, obteniendo la conclusi\u00f3n que el coeficiente de transferencia de masa en gotas, para la disoluci\u00f3n en agua-amoniaco, es superior en un 100% al obtenido utilizando la absorci\u00f3n en pel\u00edcula, cuando se emplean gotas de 60 m de di\u00e1metro. la diferencia entre los coeficientes de transferencia de masa se incrementa linealmente con la disminuci\u00f3n de las dimensiones de las gotas.  se desarrolla un procedimiento para el dise\u00f1o de absorbedores de gotas, que tiene en cuenta las dimensiones de las gotas y el flujo de disoluci\u00f3n y refrigerante.<\/p>\n<p>&nbsp;<\/p>\n<h3>Datos acad\u00e9micos de la tesis doctoral \u00ab<strong>Transferencia de masa y calor en gotas en procesos de absorci\u00f3n con nitrato de litio-amoniaco: nuevas tecnolog\u00edas<\/strong>\u00ab<\/h3>\n<ul>\n<li><strong>T\u00edtulo de la tesis:<\/strong>\u00a0 Transferencia de masa y calor en gotas en procesos de absorci\u00f3n con nitrato de litio-amoniaco: nuevas tecnolog\u00edas <\/li>\n<li><strong>Autor:<\/strong>\u00a0  Venegas Bernal M. Carmen <\/li>\n<li><strong>Universidad:<\/strong>\u00a0 Carlos III de Madrid<\/li>\n<li><strong>Fecha de lectura de la tesis:<\/strong>\u00a0 11\/04\/2002<\/li>\n<\/ul>\n<p>&nbsp;<\/p>\n<h3>Direcci\u00f3n y tribunal<\/h3>\n<ul>\n<li><strong>Director de la tesis<\/strong>\n<ul>\n<li>Marcelo Izquierdo Mill\u00e1n<\/li>\n<\/ul>\n<\/li>\n<li><strong>Tribunal<\/strong>\n<ul>\n<li>Presidente del tribunal:  Rodr\u00edguez aumente pedro a. <\/li>\n<li>f. Hern\u00e1ndez \u00e1lvarez (vocal)<\/li>\n<li> Rey mart\u00ednez Francisco Javier (vocal)<\/li>\n<li>albert Coronas salcedo (vocal)<\/li>\n<\/ul>\n<\/li>\n<\/ul>\n<p>&nbsp;<\/p>\n","protected":false},"excerpt":{"rendered":"<p>Tesis doctoral de Venegas Bernal M. Carmen Se parte del estudio termodin\u00e1mico de las disoluciones h2o-nh3, lino3-nh3 y nascn-nh3, y [&hellip;]<\/p>\n","protected":false},"author":1,"featured_media":0,"comment_status":"open","ping_status":"open","sticky":false,"template":"","format":"standard","meta":{"site-sidebar-layout":"default","site-content-layout":"","ast-site-content-layout":"","site-content-style":"default","site-sidebar-style":"default","ast-global-header-display":"","ast-banner-title-visibility":"","ast-main-header-display":"","ast-hfb-above-header-display":"","ast-hfb-below-header-display":"","ast-hfb-mobile-header-display":"","site-post-title":"","ast-breadcrumbs-content":"","ast-featured-img":"","footer-sml-layout":"","theme-transparent-header-meta":"","adv-header-id-meta":"","stick-header-meta":"","header-above-stick-meta":"","header-main-stick-meta":"","header-below-stick-meta":"","astra-migrate-meta-layouts":"default","ast-page-background-enabled":"default","ast-page-background-meta":{"desktop":{"background-color":"var(--ast-global-color-4)","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-gradient":""},"tablet":{"background-color":"","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-gradient":""},"mobile":{"background-color":"","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-gradient":""}},"ast-content-background-meta":{"desktop":{"background-color":"var(--ast-global-color-5)","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-gradient":""},"tablet":{"background-color":"var(--ast-global-color-5)","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-gradient":""},"mobile":{"background-color":"var(--ast-global-color-5)","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-gradient":""}},"footnotes":""},"categories":[18550,332,199,200,48081,1192,15726,2469,2470,2793],"tags":[51784,51783,51781,12847,51782,51780],"class_list":["post-16369","post","type-post","status-publish","format-standard","hentry","category-carlos-iii-de-madrid","category-ciencias-tecnologicas","category-fisica","category-fisica-de-fluidos","category-fisica-de-la-transmision-del-calor","category-mecanica-de-fluidos","category-procesos-de-transferencia-de-calor","category-procesos-de-transferencia-de-masa","category-procesos-tecnologicos","category-termodinamica","tag-albert-coronas-salcedo","tag-f-hernandez-alvarez","tag-marcelo-izquierdo-millan","tag-rey-Martinez-francisco-javier","tag-rodriguez-aumente-pedro-a","tag-venegas-bernal-m-carmen"],"_links":{"self":[{"href":"https:\/\/www.deberes.net\/tesis\/wp-json\/wp\/v2\/posts\/16369","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/www.deberes.net\/tesis\/wp-json\/wp\/v2\/posts"}],"about":[{"href":"https:\/\/www.deberes.net\/tesis\/wp-json\/wp\/v2\/types\/post"}],"author":[{"embeddable":true,"href":"https:\/\/www.deberes.net\/tesis\/wp-json\/wp\/v2\/users\/1"}],"replies":[{"embeddable":true,"href":"https:\/\/www.deberes.net\/tesis\/wp-json\/wp\/v2\/comments?post=16369"}],"version-history":[{"count":0,"href":"https:\/\/www.deberes.net\/tesis\/wp-json\/wp\/v2\/posts\/16369\/revisions"}],"wp:attachment":[{"href":"https:\/\/www.deberes.net\/tesis\/wp-json\/wp\/v2\/media?parent=16369"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/www.deberes.net\/tesis\/wp-json\/wp\/v2\/categories?post=16369"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/www.deberes.net\/tesis\/wp-json\/wp\/v2\/tags?post=16369"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}