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Modification of a pilot-scale continuous flow reactor for hydrothermal liquefaction of wet biomass
A pilot-scale continuous flow reactor (CFR) was modified for hydrothermal liquefaction (HTL) of algae slurry under subcritical conditions to investigate the feasibility of scaling up from batch to continuous processing. Modifications included a novel dual filter system that can remove solids at syst...
Autores principales: | , , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
Elsevier
2019
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6909004/ https://www.ncbi.nlm.nih.gov/pubmed/31871914 http://dx.doi.org/10.1016/j.mex.2019.11.019 |
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author | Cheng, Feng Le Doux, Travis Treftz, Brian Woolf, Scott Yu, Jiuling Miller, Juanita Jena, Umakanta Brewer, Catherine E. |
author_facet | Cheng, Feng Le Doux, Travis Treftz, Brian Woolf, Scott Yu, Jiuling Miller, Juanita Jena, Umakanta Brewer, Catherine E. |
author_sort | Cheng, Feng |
collection | PubMed |
description | A pilot-scale continuous flow reactor (CFR) was modified for hydrothermal liquefaction (HTL) of algae slurry under subcritical conditions to investigate the feasibility of scaling up from batch to continuous processing. Modifications included a novel dual filter system that can remove solids at system pressure and temperature, and undergo in-situ cleaning. Commissioning was carried out to address potential particle settling and clogging problems, and to estimate reactor transport characteristics. CFR performance was evaluated by running 31.4 L algae slurry with solids loadings of 3−5 wt.% under 325−350 °C and 18 MPa for 7 h. C and N elemental yields in HTL aqueous phase reached 39.0 wt.% and 61.8 wt.%, respectively. Future improvements to the CFR system will focus on higher solids loading and addition of in-line HTL liquid upgrading capabilities following the filtration system. • A high-temperature, high-pressure filtration system was designed to remove solids from HTL liquid/gaseous products at near reaction conditions to keep heavy oils in the liquid phase. • Uninterrupted reactor operation was achieved by cycling between the dual filter systems and performing in-situ filter cleaning. • Measured reactor residence time distributions were narrow and close to the calculated theoretical mean time. |
format | Online Article Text |
id | pubmed-6909004 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2019 |
publisher | Elsevier |
record_format | MEDLINE/PubMed |
spelling | pubmed-69090042019-12-23 Modification of a pilot-scale continuous flow reactor for hydrothermal liquefaction of wet biomass Cheng, Feng Le Doux, Travis Treftz, Brian Woolf, Scott Yu, Jiuling Miller, Juanita Jena, Umakanta Brewer, Catherine E. MethodsX Chemical Engineering A pilot-scale continuous flow reactor (CFR) was modified for hydrothermal liquefaction (HTL) of algae slurry under subcritical conditions to investigate the feasibility of scaling up from batch to continuous processing. Modifications included a novel dual filter system that can remove solids at system pressure and temperature, and undergo in-situ cleaning. Commissioning was carried out to address potential particle settling and clogging problems, and to estimate reactor transport characteristics. CFR performance was evaluated by running 31.4 L algae slurry with solids loadings of 3−5 wt.% under 325−350 °C and 18 MPa for 7 h. C and N elemental yields in HTL aqueous phase reached 39.0 wt.% and 61.8 wt.%, respectively. Future improvements to the CFR system will focus on higher solids loading and addition of in-line HTL liquid upgrading capabilities following the filtration system. • A high-temperature, high-pressure filtration system was designed to remove solids from HTL liquid/gaseous products at near reaction conditions to keep heavy oils in the liquid phase. • Uninterrupted reactor operation was achieved by cycling between the dual filter systems and performing in-situ filter cleaning. • Measured reactor residence time distributions were narrow and close to the calculated theoretical mean time. Elsevier 2019-11-19 /pmc/articles/PMC6909004/ /pubmed/31871914 http://dx.doi.org/10.1016/j.mex.2019.11.019 Text en © 2019 The Author(s) http://creativecommons.org/licenses/by/4.0/ This is an open access article under the CC BY license (http://creativecommons.org/licenses/by/4.0/). |
spellingShingle | Chemical Engineering Cheng, Feng Le Doux, Travis Treftz, Brian Woolf, Scott Yu, Jiuling Miller, Juanita Jena, Umakanta Brewer, Catherine E. Modification of a pilot-scale continuous flow reactor for hydrothermal liquefaction of wet biomass |
title | Modification of a pilot-scale continuous flow reactor for hydrothermal liquefaction of wet biomass |
title_full | Modification of a pilot-scale continuous flow reactor for hydrothermal liquefaction of wet biomass |
title_fullStr | Modification of a pilot-scale continuous flow reactor for hydrothermal liquefaction of wet biomass |
title_full_unstemmed | Modification of a pilot-scale continuous flow reactor for hydrothermal liquefaction of wet biomass |
title_short | Modification of a pilot-scale continuous flow reactor for hydrothermal liquefaction of wet biomass |
title_sort | modification of a pilot-scale continuous flow reactor for hydrothermal liquefaction of wet biomass |
topic | Chemical Engineering |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6909004/ https://www.ncbi.nlm.nih.gov/pubmed/31871914 http://dx.doi.org/10.1016/j.mex.2019.11.019 |
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