Biodesulfurization of dibenzothiophene and gas oil using a bioreactor containing a catalytic bed with Rhodococcus rhodochrous immobilized on silica
| dc.creator | Universidad San Sebastián | |
| dc.creator | Universidad San Sebastián | |
| dc.creator | Universidad San Sebastián | |
| dc.creator | Universidad San Sebastián | |
| dc.creator | Universidad San Sebastián | |
| dc.creator | Alejandro Dinamarca, M. | |
| dc.creator | Orellana, L. | |
| dc.creator | Aguirre, J. | |
| dc.creator | Baeza, P. | |
| dc.creator | Espinoza, G. | |
| dc.creator | Canales, C. | |
| dc.creator | Ojeda, J. | |
| dc.date.accessioned | 2023-05-24T04:47:54Z | |
| dc.date.available | 2023-05-24T04:47:54Z | |
| dc.date.created | 2023-05-24T04:47:54Z | |
| dc.date.issued | 2014-07 | |
| dc.identifier | 0141-5492 | |
| dc.identifier | https://repositorio.uss.cl/handle/uss/6081 | |
| dc.identifier | 10.1007/s10529-014-1529-y | |
| dc.description.abstract | Biodesulfurization (BDS) in a bioreactor packed with a catalytic bed of silica containing immobilized Rhodococcus rhodochrous was studied. Various bed lengths and support particle sizes were evaluated for BDS of dibenzothiophene (DBT) and gas oil. The sulfur-containing substrates were introduced separately into the bioreactor at different feed flows. Higher removal of sulfur from DBT and gas oil was achieved with a long bed, lower substrate flow, and larger sizes of immobilization particles. The packed bed bioreactor containing metabolic active cells was recycled and maintained BDS activity. | |
| dc.language | eng | |
| dc.relation | Biotechnology Letters | |
| dc.title | Biodesulfurization of dibenzothiophene and gas oil using a bioreactor containing a catalytic bed with Rhodococcus rhodochrous immobilized on silica | |
| dc.type | Artículo |