{"id":12806,"date":"2024-06-14T15:16:10","date_gmt":"2024-06-14T15:16:10","guid":{"rendered":"https:\/\/lequia-udg.com\/2024\/06\/14\/achieving-mainstream-partial-nitritation-with-aerobic-granular-sludge-treating-high-rate-activated-sludge-effluent\/"},"modified":"2024-06-14T15:29:13","modified_gmt":"2024-06-14T15:29:13","slug":"achieving-mainstream-partial-nitritation-with-aerobic-granular-sludge-treating-high-rate-activated-sludge-effluent","status":"publish","type":"post","link":"https:\/\/lequia-udg.com\/ca\/2024\/06\/14\/achieving-mainstream-partial-nitritation-with-aerobic-granular-sludge-treating-high-rate-activated-sludge-effluent\/","title":{"rendered":"Achieving mainstream partial nitritation with aerobic granular sludge treating high-rate activated sludge effluent"},"content":{"rendered":"\t\t<div data-elementor-type=\"wp-post\" data-elementor-id=\"12806\" class=\"elementor elementor-12806 elementor-12800\" data-elementor-post-type=\"post\">\n\t\t\t\t\t\t<section class=\"elementor-section elementor-top-section elementor-element elementor-element-5ce16fd1 ts-col-stretched-none ts-bg-color-over-image elementor-section-boxed elementor-section-height-default elementor-section-height-default\" data-id=\"5ce16fd1\" data-element_type=\"section\">\n\t\t\t\t\t\t<div class=\"elementor-container elementor-column-gap-default\">\n\t\t\t\t\t<div class=\"elementor-column elementor-col-100 elementor-top-column elementor-element elementor-element-58d337f0 ts-bg-color-over-image\" data-id=\"58d337f0\" data-element_type=\"column\">\n\t\t\t<div class=\"elementor-widget-wrap elementor-element-populated\">\n\t\t\t\t\t\t<div class=\"elementor-element elementor-element-69df8510 ts-align-left elementor-widget elementor-widget-ts_heading\" data-id=\"69df8510\" data-element_type=\"widget\" data-widget_type=\"ts_heading.default\">\n\t\t\t\t<div class=\"elementor-widget-container\">\n\t\t\t\t\t\t<div class=\"ts-heading-subheading ts-reverse-heading-yes animation-style4\"><h4 class=\"ts-custom-heading ts-custom-subtitle\">\r\n\t\t\t\r\n\t\t\t\tAuthors: Carb\u00f3, Oriol; Teixid\u00f3, Jaume; Canals, Joan; Ord\u00f3\u00f1ez, Antonio; Magr\u00ed, Albert; Baldi, Merc\u00e8; Guti\u00e9rrez, Bel\u00e9n; Colprim, Jes\u00fas                                                                                                    \r\n\t\t\t\r\n\t\t\t<\/h4>\r\n\t\t<h2 class=\"ts-custom-heading ts-custom-heading-title\">\r\n\t\t\t\r\n\t\t\t\tAchieving mainstream partial nitritation with aerobic granular sludge treating high-rate activated sludge effluent\r\n\t\t\t\r\n\t\t\t<\/h2>\r\n\t\t<\/div>\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t\t<\/div>\n\t\t<\/div>\n\t\t\t\t\t<\/div>\n\t\t<\/section>\n\t\t\t\t<section class=\"elementor-section elementor-top-section elementor-element elementor-element-414da0a8 ts-col-stretched-none ts-bg-color-over-image elementor-section-boxed elementor-section-height-default elementor-section-height-default\" data-id=\"414da0a8\" data-element_type=\"section\">\n\t\t\t\t\t\t<div class=\"elementor-container elementor-column-gap-default\">\n\t\t\t\t\t<div class=\"elementor-column elementor-col-100 elementor-top-column elementor-element elementor-element-6d5aff96 ts-bg-color-over-image\" data-id=\"6d5aff96\" data-element_type=\"column\">\n\t\t\t<div class=\"elementor-widget-wrap elementor-element-populated\">\n\t\t\t\t\t\t<div class=\"elementor-element elementor-element-aa6fa03 elementor-widget-tablet__width-initial elementor-widget elementor-widget-text-editor\" data-id=\"aa6fa03\" data-element_type=\"widget\" data-widget_type=\"text-editor.default\">\n\t\t\t\t<div class=\"elementor-widget-container\">\n\t\t\t\t\t\t\t\t\t<p>New configurations for wastewater treatment plants (WWTPs) are under development to increase their self-sufficiency and sustainability. One is the A-B process, in which the A-stage is designed to maximize the redirection of influent chemical oxygen demand (COD) to the production of biogas. A promising A-stage alternative is the high-rate activated sludge (HRAS). B-stage, on the other hand, can consist of the combined partial nitritation (PN)-anaerobic ammonium oxidation (anammox). In this study, PN with aerobic granular sludge (AGS) was attempted under mainstream conditions at pilot scale. The effluent of a HRAS system \u2013 ideally operating at 2 g\/L of total suspended solids, 0.5 mg\/L of dissolved oxygen and 1 h of hydraulic retention time (52 \u00b1 13 % COD removal) \u2013 was fed to the PN-AGS reactor initially inoculated with floccular sludge. Granulation and PN were studied with daily\/seasonal fluctuations and without adding external reagents. Selective wasting from the top of the settled sludge bed was found a successful strategy to trigger granular sludge formation. The maintenance of a low sludge volume index (SVI &lt; 100 mL\/g) was helpful enough for improved operation of the system (i.e., COD removal and PN). Stable PN was achieved due to the suppression of the nitrite oxidizing bacteria activity by inhibitory levels of free nitrous acid. Finally, working with fast settling biomass at long settling times reduced the influent-biomass-nitrite contact and, thus, denitritation.\u00a0<\/p>\n\t\t\t\t\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t\t<\/div>\n\t\t<\/div>\n\t\t\t\t\t<\/div>\n\t\t<\/section>\n\t\t\t\t<section class=\"elementor-section elementor-top-section elementor-element elementor-element-b62324c ts-col-stretched-none ts-bg-color-over-image elementor-section-boxed elementor-section-height-default elementor-section-height-default\" data-id=\"b62324c\" data-element_type=\"section\">\n\t\t\t\t\t\t<div class=\"elementor-container elementor-column-gap-default\">\n\t\t\t\t\t<div class=\"elementor-column elementor-col-100 elementor-top-column elementor-element elementor-element-4e7668c0 ts-bg-color-over-image\" data-id=\"4e7668c0\" data-element_type=\"column\">\n\t\t\t<div class=\"elementor-widget-wrap elementor-element-populated\">\n\t\t\t\t\t\t<div class=\"elementor-element elementor-element-5e01cd30 elementor-widget elementor-widget-accordion\" data-id=\"5e01cd30\" data-element_type=\"widget\" data-widget_type=\"accordion.default\">\n\t\t\t\t<div class=\"elementor-widget-container\">\n\t\t\t\t\t\t\t<div class=\"elementor-accordion\">\n\t\t\t\t\t\t\t<div class=\"elementor-accordion-item\">\n\t\t\t\t\t<div id=\"elementor-tab-title-1571\" class=\"elementor-tab-title\" data-tab=\"1\" role=\"button\" aria-controls=\"elementor-tab-content-1571\" aria-expanded=\"false\">\n\t\t\t\t\t\t\t\t\t\t\t\t\t<span class=\"elementor-accordion-icon elementor-accordion-icon-left\" aria-hidden=\"true\">\n\t\t\t\t\t\t\t\t\t\t\t\t\t\t\t<span class=\"elementor-accordion-icon-closed\"><i class=\"fas fa-plus\"><\/i><\/span>\n\t\t\t\t\t\t\t\t<span class=\"elementor-accordion-icon-opened\"><i class=\"fas fa-minus\"><\/i><\/span>\n\t\t\t\t\t\t\t\t\t\t\t\t\t\t<\/span>\n\t\t\t\t\t\t\t\t\t\t\t\t<a class=\"elementor-accordion-title\" tabindex=\"0\">Informaci\u00f3 addicional<\/a>\n\t\t\t\t\t<\/div>\n\t\t\t\t\t<div id=\"elementor-tab-content-1571\" class=\"elementor-tab-content elementor-clearfix\" data-tab=\"1\" role=\"region\" aria-labelledby=\"elementor-tab-title-1571\"><table style=\"border: hidden;\">\n<tbody>\n<tr style=\"border-bottom: 1px solid #efefef;\">\n<td align=\"right\" width=\"200\"><strong>Any:<\/strong><\/td>\n<td>2024<\/td>\n<\/tr>\n<tr style=\"border-bottom: 1px solid #efefef;\">\n<td align=\"right\" width=\"200\"><strong>Autors:<\/strong><\/td>\n<td>Carb\u00f3, Oriol; Teixid\u00f3, Jaume; Canals, Joan; Ord\u00f3\u00f1ez, Antonio; Magr\u00ed, Albert; Baldi, Merc\u00e8; Guti\u00e9rrez, Bel\u00e9n; Colprim, Jes\u00fas<span style=\"font-family: inherit; font-size: inherit;\">\u00a0<\/span><\/td>\n<\/tr>\n<tr style=\"border-bottom: 1px solid #efefef;\">\n<td align=\"right\" width=\"200\"><strong>Refer\u00e8ncia:<\/strong><\/td>\n<td><span class=\"Typography-module__lVnit Typography-module__Nfgvc Button-module__Imdmt\">Journal of Water Process Engineering, <\/span><span class=\"Typography-module__lVnit Typography-module__fRnrd Typography-module__Nfgvc\">Volume 60<\/span><span class=\"Typography-module__lVnit Typography-module__fRnrd Typography-module__Nfgvc\">April 2024, <\/span><span class=\"Typography-module__lVnit Typography-module__fRnrd Typography-module__Nfgvc\">Article number\u00a0105165<\/span><\/td>\n<\/tr>\n<tr style=\"border-bottom: 1px solid #efefef;\">\n<td align=\"right\" width=\"200\"><strong>Enlla\u00e7:<\/strong><\/td>\n<td>http:\/\/dx.doi.org\/10.1016\/j.jwpe.2024.105165<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t\t\t\t\t<\/div>\n\t\t\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t<div class=\"elementor-element elementor-element-77e21a46 elementor-widget elementor-widget-spacer\" data-id=\"77e21a46\" data-element_type=\"widget\" data-widget_type=\"spacer.default\">\n\t\t\t\t<div class=\"elementor-widget-container\">\n\t\t\t\t\t\t\t<div class=\"elementor-spacer\">\n\t\t\t<div class=\"elementor-spacer-inner\"><\/div>\n\t\t<\/div>\n\t\t\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t\t<\/div>\n\t\t<\/div>\n\t\t\t\t\t<\/div>\n\t\t<\/section>\n\t\t\t\t<\/div>\n\t\t","protected":false},"excerpt":{"rendered":"<p>Authors: Carb\u00f3, Oriol; Teixid\u00f3, Jaume; Canals, Joan; Ord\u00f3\u00f1ez, Antonio; Magr\u00ed, Albert; Baldi, Merc\u00e8; Guti\u00e9rrez, Bel\u00e9n; Colprim, Jes\u00fas Achieving mainstream partial nitritation with aerobic granular sludge treating high-rate activated sludge effluent New configurations for wastewater treatment plants (WWTPs) are under development to increase their self-sufficiency and sustainability. One is the A-B process, in which the A-stage &hellip; <a href=\"https:\/\/lequia-udg.com\/ca\/2024\/06\/14\/achieving-mainstream-partial-nitritation-with-aerobic-granular-sludge-treating-high-rate-activated-sludge-effluent\/\" class=\"more-link\" title=\"Continue reading <span class=\"screen-reader-text\">Achieving mainstream partial nitritation with aerobic granular sludge treating high-rate activated sludge effluent<\/span>&#8220;>Continue reading <span class=\"screen-reader-text\">Achieving mainstream partial nitritation with aerobic granular sludge treating high-rate activated sludge effluent<\/span><\/a><\/p>\n","protected":false},"author":1,"featured_media":0,"comment_status":"closed","ping_status":"open","sticky":false,"template":"elementor_header_footer","format":"standard","meta":{"footnotes":""},"categories":[64],"tags":[],"class_list":["post-12806","post","type-post","status-publish","format-standard","hentry","category-articles-ca"],"_links":{"self":[{"href":"https:\/\/lequia-udg.com\/ca\/wp-json\/wp\/v2\/posts\/12806","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/lequia-udg.com\/ca\/wp-json\/wp\/v2\/posts"}],"about":[{"href":"https:\/\/lequia-udg.com\/ca\/wp-json\/wp\/v2\/types\/post"}],"author":[{"embeddable":true,"href":"https:\/\/lequia-udg.com\/ca\/wp-json\/wp\/v2\/users\/1"}],"replies":[{"embeddable":true,"href":"https:\/\/lequia-udg.com\/ca\/wp-json\/wp\/v2\/comments?post=12806"}],"version-history":[{"count":1,"href":"https:\/\/lequia-udg.com\/ca\/wp-json\/wp\/v2\/posts\/12806\/revisions"}],"predecessor-version":[{"id":12807,"href":"https:\/\/lequia-udg.com\/ca\/wp-json\/wp\/v2\/posts\/12806\/revisions\/12807"}],"wp:attachment":[{"href":"https:\/\/lequia-udg.com\/ca\/wp-json\/wp\/v2\/media?parent=12806"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/lequia-udg.com\/ca\/wp-json\/wp\/v2\/categories?post=12806"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/lequia-udg.com\/ca\/wp-json\/wp\/v2\/tags?post=12806"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}