[{"command":"settings","settings":{"pluralDelimiter":"\u0003","suppressDeprecationErrors":true,"user":{"uid":0,"permissionsHash":"d9587e6f410d2e7f476e3da6cb10a457c78ab82347f962bf83d9020620f901dd"}},"merge":true},{"command":"add_css","data":[{"rel":"stylesheet","media":"all","href":"\/modules\/contrib\/addtocal\/addtocal.css?t2408i"},{"rel":"stylesheet","media":"all","href":"\/themes\/custom\/cest2025\/css\/components\/node.css?t2408i"}]},{"command":"add_js","selector":"body","data":[{"src":"\/core\/assets\/vendor\/jquery\/jquery.min.js?v=3.7.1"},{"src":"\/core\/assets\/vendor\/once\/once.min.js?v=1.0.1"},{"src":"\/core\/misc\/drupalSettingsLoader.js?v=10.5.1"},{"src":"\/core\/misc\/drupal.js?v=10.5.1"},{"src":"\/core\/misc\/drupal.init.js?v=10.5.1"},{"src":"\/modules\/contrib\/addtocal\/addtocal.js?v=10.5.1"},{"src":"\/modules\/contrib\/addtocal\/addtocal-download.js?v=10.5.1"}]},{"command":"openDialog","selector":"#drupal-modal","settings":null,"data":"\n\u003Carticle class=\u0022node node--type-presentation node--promoted node--view-mode-modal\u0022\u003E\n      \u003Cdiv\u003ESession 13 - Environmental Biotechnology and Bioenergy\u003C\/div\u003E\n  \n      \u003Cb\u003E\u003Cspan\u003EBiogas upgrade with green hydrogen in a semi-pilot trickle bed reactor\u003C\/span\u003E\n\u003C\/b\u003E\n  \n      \u003Cdiv\u003E\u003Cb\u003ECEST ID: cest2025_00436\u003C\/b\u003E\u003C\/div\u003E\n  \n        \u003Cdiv class=\u0022mb-3\u0022\u003E\n      \u003Cb\u003ERoom Panacea | Thu 4 Sep 2025 | 15:55 - 16:05 pm\u003C\/b\u003E\n    \u003C\/div\u003E\n  \n          \n    \n  \n      \u003Cdiv class=\u0022mt-10\u0022\u003E\n            \u003Cdiv class=\u0022clearfix text-formatted field field--name-presentation-body field--type-text-long field--label-hidden field__item\u0022\u003EThe current study investigated the performance of biological methanation of CO2 using green H2 in a mesophilic (37\u2103) trickle bed reactor (TBR) (0.051m3) at ambient pressure. For both phase A and phase B a synthetic gas feed (60\/40 CH4\/CO2) was used to simulate biogas. Nitrogen was used in phase A for better monitoring of the system. For phase A the average productivity of methane was 3.2 m_(CH_4)^3\/(m_(trickle bed)^3*d)  at methane content of 71.3% with 10.3% N2. For phase B no Nitrogen was used, and the average productivity of methane was 1.3 m_(CH_4)^3\/(m_(trickle bed)^3*d)  at methane content of 97.9% with less than 0.1% residual H2.  \u003C\/div\u003E\n      \u003C\/div\u003E\n  \n  \u003Cdiv class=\u0022mt-5 mb-5\u0022\u003E\n          \u003Cspan\u003E\n          \u003Cb\u003EPresenter:\u003C\/b\u003E\n                      \u003Cp\u003E\n            Dr KONSTANTINA Papadopoulou\n            \u003C\/p\u003E\n                  \u003C\/span\u003E\n      \u003C\/div\u003E\n\n  \u003Cdiv class=\u0022mb-5\u0022\u003E\n          \u003Cdiv class=\u0022field__label\u0022\u003E\n        Authors\n      \u003C\/div\u003E\n              \u003Cp\u003E\n          KONSTANTINA Papadopoulou\n        \u003C\/p\u003E\n              \u003Cp\u003E\n          Charalampos Pavlopoulos\n        \u003C\/p\u003E\n              \u003Cp\u003E\n          CHRISTOS Riglis\n        \u003C\/p\u003E\n              \u003Cp\u003E\n          EMMANOUEL Tsilifonis\n        \u003C\/p\u003E\n              \u003Cp\u003E\n          AGGELIKI Markopoulou\n        \u003C\/p\u003E\n              \u003Cp\u003E\n          D. Fotopoulos\n        \u003C\/p\u003E\n              \u003Cp\u003E\n          A. Papathanasiou\n        \u003C\/p\u003E\n              \u003Cp\u003E\n          Gerasimos Lyberatos\n        \u003C\/p\u003E\n            \u003C\/div\u003E\n\n\u003C\/article\u003E\n","dialogOptions":{"width":"700","position":{"my":"right top","at":"right top"},"closeOnEscape":true,"dialogClass":"presentation-dialog","modal":true,"title":"","classes":{"ui-dialog":"presentation-dialog"}}}]