Simulation and Performance Analysis of Integrated Gasification–Syngas Fermentation Plant for Lignocellulosic Ethanol Production
| dc.contributor | Háskóli Íslands | en_US |
| dc.contributor | University of Iceland | en_US |
| dc.contributor.author | Safarian, Sahar | |
| dc.contributor.author | Unnthorsson, Runar | |
| dc.contributor.author | Richter, Christiaan | |
| dc.contributor.department | Iðnaðarverkfræði-, vélaverkfræði- og tölvunarfræðideild (HÍ) | en_US |
| dc.contributor.department | Faculty of Industrial Eng., Mechanical Eng. and Computer Science (UI) | en_US |
| dc.contributor.school | Verkfræði- og náttúruvísindasvið (HÍ) | en_US |
| dc.contributor.school | School of Engineering and Natural Sciences (UI) | en_US |
| dc.date.accessioned | 2020-08-04T16:02:47Z | |
| dc.date.available | 2020-08-04T16:02:47Z | |
| dc.date.issued | 2020-07-14 | |
| dc.description.abstract | This study presents a new simulation model developed with ASPEN Plus of waste biomass gasification integrated with syngas fermentation and product recovery units for bioethanol production from garden waste as a lignocellulosic biomass. The simulation model includes three modules: gasification, fermentation, and ethanol recovery. A parametric analysis is carried out to investigate the effect of gasification temperature (500–1500 °C) and equivalence ratio (0.2–0.6) on the gasification performance and bioethanol production yield. The results reveal that, for efficient gasification and high ethanol production, the operating temperature range should be 700–1000 °C, as well as an equivalence ratio between 0.2 and 0.4. At optimal operating conditions, the bioethanol production yield is 0.114 kg/h per 1 kg/h input garden waste with 50% moisture content. It is worth mentioning that this parameter increases to 0.217 kgbioethanol/kggarden waste under dry-based conditions. | en_US |
| dc.description.sponsorship | This research was funded by the Icelandic Research Fund (IRF) (in Icelandic: Rannsoknasjodur) and the grant number is 196458-051 | en_US |
| dc.description.version | Peer Reviewed | en_US |
| dc.format.extent | 12 | en_US |
| dc.identifier.citation | Safarian, S.; Unnthorsson, R.; Richter, C. Simulation and Performance Analysis of Integrated Gasification–Syngas Fermentation Plant for Lignocellulosic Ethanol Production. Fermentation 2020, 6, 68. doi:10.3390/fermentation6030068 | en_US |
| dc.identifier.doi | 10.3390/fermentation6030068 | |
| dc.identifier.issn | 2311-5637 | |
| dc.identifier.journal | Fermentation | en_US |
| dc.identifier.uri | https://hdl.handle.net/20.500.11815/1917 | |
| dc.language.iso | en | en_US |
| dc.publisher | MDPI AG | en_US |
| dc.relation.ispartofseries | Fermentation;6(3) | |
| dc.relation.url | https://www.mdpi.com/2311-5637/6/3/68/pdf | en_US |
| dc.rights | info:eu-repo/semantics/openAccess | en_US |
| dc.subject | lignocellulosic ethanol production | en_US |
| dc.subject | Waste biomass gasification | en_US |
| dc.subject | syngas fermentation | en_US |
| dc.subject | Process simulation | en_US |
| dc.subject | system performance | en_US |
| dc.subject | Waste to energy | en_US |
| dc.subject | Úrgangur | en_US |
| dc.subject | Orkuframleiðsla | en_US |
| dc.subject | Etanól | en_US |
| dc.title | Simulation and Performance Analysis of Integrated Gasification–Syngas Fermentation Plant for Lignocellulosic Ethanol Production | en_US |
| dc.type | info:eu-repo/semantics/article | en_US |
| dcterms.license | CC BY 4.0 | en_US |
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