Hydrocarbon liquid production via the bioCRACK process and catalytic hydroprocessing of the product oil
Abstract
Continuous hydroprocessing of liquid phase pyrolysis bio-oil, provided by BDI-BioEnergy International bioCRACK pilot plant at OMV Refinery in Schwechat/Vienna Austria was investigated. These hydroprocessing tests showed promising results using catalytic hydroprocessing strategies developed for unfractionated bio-oil. A sulfided base metal catalyst (CoMo on Al2O3) was evaluated. The bed of catalyst was operated at 400 °C in a continuous-flow reactor at a pressure of 12.1 MPa with flowing hydrogen. The condensed liquid products were analyzed and found that the hydrocarbon liquid was significantly hydrotreated so that nitrogen and sulfur were below the level of detection (<0.05), while the residual oxygen ranged from 0.7 to 1.2%. The density of the products varied from 0.71 g/mL up to 0.79 g/mL with a correlated change of the hydrogen to carbon atomic ratio from 2.1 down to 1.9. The product quality remained high throughout the extended tests suggesting minimal loss of catalyst activity through the test. These tests provided the data needed to assess the quality of liquid fuel products obtained from the bioCRACK process as well as the activity of the catalyst for comparison with products obtained from hydrotreated fast pyrolysis bio-oils from fluidized-bed operation.
- Authors:
-
- Graz Univ. of Technology (Austria). Inst. of Chemical Engineering and Environmental Technology; BDI-BioEnergy International, Graz (Austria)
- Pacific Northwest National Lab. (PNNL), Richland, WA (United States)
- BDI-BioEnergy International, Graz (Austria)
- Graz Univ. of Technology (Austria). Inst. of Chemical Engineering and Environmental Technology
- Publication Date:
- Research Org.:
- Pacific Northwest National Lab. (PNNL), Richland, WA (United States)
- Sponsoring Org.:
- USDOE
- OSTI Identifier:
- 1194284
- Report Number(s):
- PNNL-SA-106757
Journal ID: ISSN 1463-9262; GRCHFJ; BM0101010
- Grant/Contract Number:
- AC05-76RL01830
- Resource Type:
- Accepted Manuscript
- Journal Name:
- Green Chemistry
- Additional Journal Information:
- Journal Volume: 17; Journal Issue: 4; Journal ID: ISSN 1463-9262
- Publisher:
- Royal Society of Chemistry
- Country of Publication:
- United States
- Language:
- English
- Subject:
- 09 BIOMASS FUELS; biomass; pyrolysis; hydrotreating; catalysis
Citation Formats
Schwaiger, Nickolaus, Elliott, Douglas C., Ritzberger, Jurgen, Wang, Huamin, Pucher, Peter, and Siebenhofer, Matthaus. Hydrocarbon liquid production via the bioCRACK process and catalytic hydroprocessing of the product oil. United States: N. p., 2015.
Web. doi:10.1039/c4gc02344g.
Schwaiger, Nickolaus, Elliott, Douglas C., Ritzberger, Jurgen, Wang, Huamin, Pucher, Peter, & Siebenhofer, Matthaus. Hydrocarbon liquid production via the bioCRACK process and catalytic hydroprocessing of the product oil. United States. https://doi.org/10.1039/c4gc02344g
Schwaiger, Nickolaus, Elliott, Douglas C., Ritzberger, Jurgen, Wang, Huamin, Pucher, Peter, and Siebenhofer, Matthaus. Thu .
"Hydrocarbon liquid production via the bioCRACK process and catalytic hydroprocessing of the product oil". United States. https://doi.org/10.1039/c4gc02344g. https://www.osti.gov/servlets/purl/1194284.
@article{osti_1194284,
title = {Hydrocarbon liquid production via the bioCRACK process and catalytic hydroprocessing of the product oil},
author = {Schwaiger, Nickolaus and Elliott, Douglas C. and Ritzberger, Jurgen and Wang, Huamin and Pucher, Peter and Siebenhofer, Matthaus},
abstractNote = {Continuous hydroprocessing of liquid phase pyrolysis bio-oil, provided by BDI-BioEnergy International bioCRACK pilot plant at OMV Refinery in Schwechat/Vienna Austria was investigated. These hydroprocessing tests showed promising results using catalytic hydroprocessing strategies developed for unfractionated bio-oil. A sulfided base metal catalyst (CoMo on Al2O3) was evaluated. The bed of catalyst was operated at 400 °C in a continuous-flow reactor at a pressure of 12.1 MPa with flowing hydrogen. The condensed liquid products were analyzed and found that the hydrocarbon liquid was significantly hydrotreated so that nitrogen and sulfur were below the level of detection (<0.05), while the residual oxygen ranged from 0.7 to 1.2%. The density of the products varied from 0.71 g/mL up to 0.79 g/mL with a correlated change of the hydrogen to carbon atomic ratio from 2.1 down to 1.9. The product quality remained high throughout the extended tests suggesting minimal loss of catalyst activity through the test. These tests provided the data needed to assess the quality of liquid fuel products obtained from the bioCRACK process as well as the activity of the catalyst for comparison with products obtained from hydrotreated fast pyrolysis bio-oils from fluidized-bed operation.},
doi = {10.1039/c4gc02344g},
journal = {Green Chemistry},
number = 4,
volume = 17,
place = {United States},
year = {Thu Jan 01 00:00:00 EST 2015},
month = {Thu Jan 01 00:00:00 EST 2015}
}
Web of Science
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Works referencing / citing this record:
Lignocellulose Liquefaction to Biocrude: A Tutorial Review
journal, March 2018
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- ChemSusChem, Vol. 11, Issue 6
High-throughput continuous hydrodeoxygenation of liquid phase pyrolysis oil
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Hydrocarbon production by continuous hydrodeoxygenation of liquid phase pyrolysis oil with biogenous hydrogen rich synthesis gas
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Diesel production from lignocellulosic feed: the bioCRACK process
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