{"id":84520,"date":"2018-03-10T00:08:51","date_gmt":"2018-03-10T00:08:51","guid":{"rendered":"https:\/\/www.deberes.net\/tesis\/sin-categoria\/caracterizacion-de-la-biopelicula-y-del-fango-en-el-proceso-blasf-a-alta-carga\/"},"modified":"2018-03-10T00:08:51","modified_gmt":"2018-03-10T00:08:51","slug":"caracterizacion-de-la-biopelicula-y-del-fango-en-el-proceso-blasf-a-alta-carga","status":"publish","type":"post","link":"https:\/\/www.deberes.net\/tesis\/ciencias-tecnologicas\/caracterizacion-de-la-biopelicula-y-del-fango-en-el-proceso-blasf-a-alta-carga\/","title":{"rendered":"Caracterizacion de la biopelicula y del fango en el proceso blasf a alta carga."},"content":{"rendered":"<h2>Tesis doctoral de <strong>  Sanabria Artunduaga Otoniel Alfonso <\/strong><\/h2>\n<p>Se realiz\u00f3 una investigaci\u00f3n encaminada a verificar la tasa de acumulaci\u00f3n y desprendimiento de biopel\u00edcula en reactores blasf(biopel\u00edcula de lecho aireado sumergido fijo), para el control del atascamiento en operaci\u00f3n a altas cargas org\u00e1nicas. A escala de laboratorio, se utilizaron testigos de soporte de superficie 75 y 131 m2\/m3 con cargas de 5-15 kg dqo\/m3-d\u00eda proveniente de un afluente de aru sin decantaci\u00f3n primario en reactores blas ii, con aireaci\u00f3n de 11-50 m3\/kg dqo aplicada, en flujo contra y co-corriente. se encontr\u00f3 una tasa de crecimiento de 3.7 kg de biopel\u00edcula h\u00fameda\/m2 de superficie disponible en el soporte-d\u00eda. A escala piloto, se experiment\u00f3 con otro soporte (pe-3)de 120 m2\/m3 de superficie espec\u00edfica. Se experiment\u00f3 on cov en el rango de 11-15 kg dqo\/m3-d\u00eda y aireaci\u00f3n de 11-24 m3\/kg dqo aplicada, del mismo afluente. Sometidos a diferentes esfuerzos cortantes (por aireaci\u00f3n) en un banco de pruebas, se evalu\u00f3 la tasa de desprendimiento en funci\u00f3n del tiempo de exposici\u00f3n al cortante, la edad de la biopel\u00edcula y la coa aplicada en un periodo de 5 meses. Se encontr\u00f3 que 33 m3 aire\/m2-superficie de soporte-h, son suficientes para controlar el espesor de la biopel\u00edcula, aplicado durante un periodo de 7 a  16 minutos, con 20 a 25% de desprendimiento de la biomasa acumulada. En la planta piloto se pudo observar que la producci\u00f3n espec\u00edfica de fangos (purgados) del proceso blasf aumenta al aumentar el suministro espec\u00edfico de ox\u00edgeno, 0,14 kg ss\/kg dqoe para 14 m3 aire\/kg kqoapl., Frente a 0,3 (0,21 a 0,39) kg ss\/kg dqoe para 24 m3 aire\/kg dqoapl., con un descenso de la coa desde 13,4 a 11 kg dqo\/m3 relleno-d\u00eda.<\/p>\n<p>&nbsp;<\/p>\n<h3>Datos acad\u00e9micos de la tesis doctoral \u00ab<strong>Caracterizacion de la biopelicula y del fango en el proceso blasf a alta carga.<\/strong>\u00ab<\/h3>\n<ul>\n<li><strong>T\u00edtulo de la tesis:<\/strong>\u00a0 Caracterizacion de la biopelicula y del fango en el proceso blasf a alta carga. <\/li>\n<li><strong>Autor:<\/strong>\u00a0  Sanabria Artunduaga Otoniel Alfonso <\/li>\n<li><strong>Universidad:<\/strong>\u00a0 Cantabria<\/li>\n<li><strong>Fecha de lectura de la tesis:<\/strong>\u00a0 15\/05\/2000<\/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>Juan  Ignacio Tejero Monz\u00f3n<\/li>\n<\/ul>\n<\/li>\n<li><strong>Tribunal<\/strong>\n<ul>\n<li>Presidente del tribunal: diego Sales m\u00e1rquez <\/li>\n<li>joaqu\u00edn Su\u00e1rez l\u00f3pez (vocal)<\/li>\n<li>Emilio Eguia lopez (vocal)<\/li>\n<li>Javier Temprano gonzalez (vocal)<\/li>\n<\/ul>\n<\/li>\n<\/ul>\n<p>&nbsp;<\/p>\n","protected":false},"excerpt":{"rendered":"<p>Tesis doctoral de Sanabria Artunduaga Otoniel Alfonso Se realiz\u00f3 una investigaci\u00f3n encaminada a verificar la tasa de acumulaci\u00f3n y desprendimiento [&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 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