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| 34 | "created": "2024-11-05", | 34 | "created": "2024-11-05", | ||
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| 61 | "license_title": "Creative Commons Attribution", | 61 | "license_title": "Creative Commons Attribution", | ||
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| 63 | "lineage_source": [ | 63 | "lineage_source": [ | ||
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| 78 | "miteco_data_territory": { | 78 | "miteco_data_territory": { | ||
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| 81 | "miteco_dataset_type": | 81 | "miteco_dataset_type": | ||
| 82 | //publications.europa.eu/resource/authority/dataset-type/STATISTICAL", | 82 | //publications.europa.eu/resource/authority/dataset-type/STATISTICAL", | ||
| 83 | "miteco_geo_level": "1", | 83 | "miteco_geo_level": "1", | ||
| 84 | "modified": "2026-06-23", | 84 | "modified": "2026-06-23", | ||
| 85 | "name": "f3b2e976-449b-58ba-8ce3-7d1841ed8db2", | 85 | "name": "f3b2e976-449b-58ba-8ce3-7d1841ed8db2", | ||
| 86 | "notes": "The performance of CRBR in denitrification with catechol | 86 | "notes": "The performance of CRBR in denitrification with catechol | ||
| 87 | carbon source is presented. The influence of inlet nitrate | 87 | carbon source is presented. The influence of inlet nitrate | ||
| 88 | concentration, hydraulic retention time (HRT), media filling ratio and | 88 | concentration, hydraulic retention time (HRT), media filling ratio and | ||
| 89 | rotational speed of media on the performance of CRBR was investigated. | 89 | rotational speed of media on the performance of CRBR was investigated. | ||
| 90 | The bioreactor could denitrify over 95% of the nitrate at an inlet | 90 | The bioreactor could denitrify over 95% of the nitrate at an inlet | ||
| 91 | concentration up to 1000 mg NO 3 =L and a short HRT as low as 18 h. | 91 | concentration up to 1000 mg NO 3 =L and a short HRT as low as 18 h. | ||
| 92 | The optimum media filling ratio at which the maximum denitrification | 92 | The optimum media filling ratio at which the maximum denitrification | ||
| 93 | was achieved in the CRBR was 30% and the con tribution of media at | 93 | was achieved in the CRBR was 30% and the con tribution of media at | ||
| 94 | this condition was around 36%. The optimum ratio of media filling at | 94 | this condition was around 36%. The optimum ratio of media filling at | ||
| 95 | which the maximum denitrification was 20 rpm and the contribution of | 95 | which the maximum denitrification was 20 rpm and the contribution of | ||
| 96 | rotational speed under this condition was around 17%. According to the | 96 | rotational speed under this condition was around 17%. According to the | ||
| 97 | findings, the CRBR is a high rate bioreactor and thus serves as an | 97 | findings, the CRBR is a high rate bioreactor and thus serves as an | ||
| 98 | appro priate technology for denitrification of wastewaters containing | 98 | appro priate technology for denitrification of wastewaters containing | ||
| 99 | a high concentration of nitrate and toxic organic compounds.", | 99 | a high concentration of nitrate and toxic organic compounds.", | ||
| 100 | "notes_translated": { | 100 | "notes_translated": { | ||
| 101 | "es": "The performance of CRBR in denitrification with catechol | 101 | "es": "The performance of CRBR in denitrification with catechol | ||
| 102 | carbon source is presented. The influence of inlet nitrate | 102 | carbon source is presented. The influence of inlet nitrate | ||
| 103 | concentration, hydraulic retention time (HRT), media filling ratio and | 103 | concentration, hydraulic retention time (HRT), media filling ratio and | ||
| 104 | rotational speed of media on the performance of CRBR was investigated. | 104 | rotational speed of media on the performance of CRBR was investigated. | ||
| 105 | The bioreactor could denitrify over 95% of the nitrate at an inlet | 105 | The bioreactor could denitrify over 95% of the nitrate at an inlet | ||
| 106 | concentration up to 1000 mg NO 3 =L and a short HRT as low as 18 h. | 106 | concentration up to 1000 mg NO 3 =L and a short HRT as low as 18 h. | ||
| 107 | The optimum media filling ratio at which the maximum denitrification | 107 | The optimum media filling ratio at which the maximum denitrification | ||
| 108 | was achieved in the CRBR was 30% and the con tribution of media at | 108 | was achieved in the CRBR was 30% and the con tribution of media at | ||
| 109 | this condition was around 36%. The optimum ratio of media filling at | 109 | this condition was around 36%. The optimum ratio of media filling at | ||
| 110 | which the maximum denitrification was 20 rpm and the contribution of | 110 | which the maximum denitrification was 20 rpm and the contribution of | ||
| 111 | rotational speed under this condition was around 17%. According to the | 111 | rotational speed under this condition was around 17%. According to the | ||
| 112 | findings, the CRBR is a high rate bioreactor and thus serves as an | 112 | findings, the CRBR is a high rate bioreactor and thus serves as an | ||
| 113 | appro priate technology for denitrification of wastewaters containing | 113 | appro priate technology for denitrification of wastewaters containing | ||
| 114 | a high concentration of nitrate and toxic organic compounds." | 114 | a high concentration of nitrate and toxic organic compounds." | ||
| 115 | }, | 115 | }, | ||
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| 140 | Ministerio para la Transici\u00f3n Ecol\u00f3gica y el Reto | 140 | Ministerio para la Transici\u00f3n Ecol\u00f3gica y el Reto | ||
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| 234 | { | 234 | { | ||
| 235 | "display_name": "gestion_sostenible", | 235 | "display_name": "gestion_sostenible", | ||
| 236 | "id": "ab71cc3e-3c99-4f3f-a20f-d4e8016c3b55", | 236 | "id": "ab71cc3e-3c99-4f3f-a20f-d4e8016c3b55", | ||
| 237 | "name": "gestion_sostenible", | 237 | "name": "gestion_sostenible", | ||
| 238 | "state": "active", | 238 | "state": "active", | ||
| 239 | "vocabulary_id": null | 239 | "vocabulary_id": null | ||
| 240 | }, | 240 | }, | ||
| 241 | { | 241 | { | ||
| 242 | "display_name": "marino", | 242 | "display_name": "marino", | ||
| 243 | "id": "004084d1-68d8-46ca-842a-c10278540bc9", | 243 | "id": "004084d1-68d8-46ca-842a-c10278540bc9", | ||
| 244 | "name": "marino", | 244 | "name": "marino", | ||
| 245 | "state": "active", | 245 | "state": "active", | ||
| 246 | "vocabulary_id": null | 246 | "vocabulary_id": null | ||
| 247 | } | 247 | } | ||
| 248 | ], | 248 | ], | ||
| 249 | "thematic_area": [ | 249 | "thematic_area": [ | ||
| 250 | "espacios_protegidos" | 250 | "espacios_protegidos" | ||
| 251 | ], | 251 | ], | ||
| 252 | "theme_es": [ | 252 | "theme_es": [ | ||
| 253 | "http://datos.gob.es/kos/sector-publico/sector/medio-ambiente" | 253 | "http://datos.gob.es/kos/sector-publico/sector/medio-ambiente" | ||
| 254 | ], | 254 | ], | ||
| 255 | "title": "Enhanced biological denitrification in the cyclic rotating | 255 | "title": "Enhanced biological denitrification in the cyclic rotating | ||
| 256 | bed reactor with catechol as carbon source", | 256 | bed reactor with catechol as carbon source", | ||
| 257 | "title_translated": { | 257 | "title_translated": { | ||
| 258 | "es": "Enhanced biological denitrification in the cyclic rotating | 258 | "es": "Enhanced biological denitrification in the cyclic rotating | ||
| 259 | bed reactor with catechol as carbon source" | 259 | bed reactor with catechol as carbon source" | ||
| 260 | }, | 260 | }, | ||
| 261 | "topic": | 261 | "topic": | ||
| 262 | "http://inspire.ec.europa.eu/metadata-codelist/TopicCategory/biota", | 262 | "http://inspire.ec.europa.eu/metadata-codelist/TopicCategory/biota", | ||
| 263 | "type": "dataset", | 263 | "type": "dataset", | ||
| 264 | "url": | 264 | "url": | ||
| 265 | //iepnb.es:443/catalogo/dataset/f3b2e976-449b-58ba-8ce3-7d1841ed8db2", | 265 | //iepnb.es:443/catalogo/dataset/f3b2e976-449b-58ba-8ce3-7d1841ed8db2", | ||
| 266 | "version_notes": { | 266 | "version_notes": { | ||
| 267 | "es": "" | 267 | "es": "" | ||
| 268 | } | 268 | } | ||
| 269 | } | 269 | } |