dc.contributor.author | Jena, U | en |
dc.contributor.author | Das, KC | en |
dc.date.accessioned | 2014-06-06T06:50:52Z | |
dc.date.available | 2014-06-06T06:50:52Z | |
dc.date.issued | 2011 | en |
dc.identifier.issn | 08870624 | en |
dc.identifier.uri | http://dx.doi.org/10.1021/ef201373m | en |
dc.identifier.uri | http://62.217.125.90/xmlui/handle/123456789/5204 | |
dc.subject.other | Aqueous phase | en |
dc.subject.other | Bio oil | en |
dc.subject.other | Bio-oil yield | en |
dc.subject.other | Char yield | en |
dc.subject.other | Comparative evaluations | en |
dc.subject.other | Fuel properties | en |
dc.subject.other | High moisture | en |
dc.subject.other | High pressure | en |
dc.subject.other | High temperature | en |
dc.subject.other | Higher energy density | en |
dc.subject.other | Liquid products | en |
dc.subject.other | Low temperatures | en |
dc.subject.other | Lower energies | en |
dc.subject.other | Micro-algae | en |
dc.subject.other | Parr reactors | en |
dc.subject.other | Slow pyrolysis | en |
dc.subject.other | Storage stability | en |
dc.subject.other | Algae | en |
dc.subject.other | Atmospheric pressure | en |
dc.subject.other | Carbon steel | en |
dc.subject.other | Energy utilization | en |
dc.subject.other | Feedstocks | en |
dc.subject.other | Fuel storage | en |
dc.subject.other | Liquefaction | en |
dc.subject.other | Moisture | en |
dc.subject.other | Pyrolysis | en |
dc.title | Comparative evaluation of thermochemical liquefaction and pyrolysis for bio-oil production from microalgae | en |
heal.type | journalArticle | en |
heal.identifier.primary | 10.1021/ef201373m | en |
heal.publicationDate | 2011 | en |
heal.abstract | Bio-oil is the liquid product of thermochemical liquefaction or pyrolysis of biomass. Thermochemical liquefaction (TCL) is a low temperature (250-350 °C) and high pressure (5-20 MPa) process particularly suited for high moisture feedstocks, whereas pyrolysis is accomplished at moderate to high temperatures (400-600 °C) and atmospheric pressure and requires drying of the feedstock. In this paper, we present experimental results that provide a critical comparison of TCL and slow pyrolysis processes for producing bio-oil from algae. TCL experiments were performed in a 1.8-L Parr reactor using algae slurry (80% moisture) and pyrolysis runs were carried out in an 8-L mild steel cubical reactor, using dried algal powder as received (∼4% moisture). Yields and composition of bio-oil, char, gases, and aqueous phase were evaluated and compared for TCL and pyrolysis. TCL resulted in higher bio-oil yields (∼41%), lower char yields (∼6.3%), and lower energy consumption ratio compared to pyrolysis, which resulted in 23-29% bio-oil, and 28-40% solids yields. Bio-oil obtained from TCL was found to have higher energy density and superior fuel properties such as thermal and storage stabilities, compared to pyrolysis bio-oil. © 2011 American Chemical Society. | en |
heal.journalName | Energy and Fuels | en |
dc.identifier.issue | 11 | en |
dc.identifier.volume | 25 | en |
dc.identifier.doi | 10.1021/ef201373m | en |
dc.identifier.spage | 5472 | en |
dc.identifier.epage | 5482 | en |
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