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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...

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Autores principales: Cheng, Feng, Le Doux, Travis, Treftz, Brian, Woolf, Scott, Yu, Jiuling, Miller, Juanita, Jena, Umakanta, Brewer, Catherine E.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Elsevier 2019
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.
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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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