volume 379 pages 141-148

Upgrading of biomass-derived liquids in a biorefinery context: Hydroisomerization and fluid catalytic cracking of heavy naphtha on bench and pilot scale

Publication typeJournal Article
Publication date2021-11-01
scimago Q1
wos Q1
SJR1.050
CiteScore11.2
Impact factor5.3
ISSN09205861, 18734308
General Chemistry
Catalysis
Abstract
Efficient upgrading of low value bio-derived heavy naphtha to high added value products (isomers and olefins) in a biorefinery context. • Successful upgrading of BtL-naphtha to fuels and chemicals in pilot scale. • Good agreement between bench and pilot scale tests in hydroisomerization and FCC. • Isomerization over 0.1 wt% Pt/ZSM-5 leads to efficient production of isoparrafins. • Fluid catalytic cracking of BtL-naphtha requires high temperatures (600–650 °C). • Chemicals yield of ∼27 wt% can be attained with naphtha fluid catalytic cracking. The development of efficient processes for the upgrading of low value bio-derived liquid intermediates to high added value products in biorefineries is critical for the establishment of a robust and competitive bio-based economy. We show in this paper that low quality surrogate heavy naphtha, representative of biofuels from thermochemical biomass conversion processes, can be efficiently converted to high quality fuel and chemicals (olefins) via hydroisomerization and catalytic cracking, respectively. Hydroisomerization over a low loading 0.1 wt% Pt/ZSM-5 catalyst leads to the conversion of normal paraffins to C 5 -C 8 isoparaffins with limited cracking, and produces a fuel with higher octane and lower cetane number, suitable for use in future powertrains such as HCCI engines. Catalytic cracking of the naphtha on a commercial ZSM-5 based FCC catalyst results in the production of a significant amount of olefins at 600 °C, primarily propylene followed by ethylene, n-butene, pentene and i-butene. Both processes are validated on pilot scale. Some differences observed between bench and pilot scale results are due to scalability phenomena and different reaction conditions. Still, excellent agreement with regards to the composition of the products at similar conversion level exists, demonstrating the scalability and applicability of these upgrading processes in thermochemical biorefineries.
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Heracleous E. et al. Upgrading of biomass-derived liquids in a biorefinery context: Hydroisomerization and fluid catalytic cracking of heavy naphtha on bench and pilot scale // Catalysis Today. 2021. Vol. 379. pp. 141-148.
GOST all authors (up to 50) Copy
Heracleous E., Iliopoulou E. F., Drakaki K., Papapetrou M. C., Iatridis D. K., Lappas A. Upgrading of biomass-derived liquids in a biorefinery context: Hydroisomerization and fluid catalytic cracking of heavy naphtha on bench and pilot scale // Catalysis Today. 2021. Vol. 379. pp. 141-148.
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RIS Copy
TY - JOUR
DO - 10.1016/j.cattod.2020.08.006
UR - https://doi.org/10.1016/j.cattod.2020.08.006
TI - Upgrading of biomass-derived liquids in a biorefinery context: Hydroisomerization and fluid catalytic cracking of heavy naphtha on bench and pilot scale
T2 - Catalysis Today
AU - Heracleous, E
AU - Iliopoulou, Eleni F
AU - Drakaki, Kleoniki
AU - Papapetrou, Maria C
AU - Iatridis, Dimitris K
AU - Lappas, A.
PY - 2021
DA - 2021/11/01
PB - Elsevier
SP - 141-148
VL - 379
SN - 0920-5861
SN - 1873-4308
ER -
BibTex
Cite this
BibTex (up to 50 authors) Copy
@article{2021_Heracleous,
author = {E Heracleous and Eleni F Iliopoulou and Kleoniki Drakaki and Maria C Papapetrou and Dimitris K Iatridis and A. Lappas},
title = {Upgrading of biomass-derived liquids in a biorefinery context: Hydroisomerization and fluid catalytic cracking of heavy naphtha on bench and pilot scale},
journal = {Catalysis Today},
year = {2021},
volume = {379},
publisher = {Elsevier},
month = {nov},
url = {https://doi.org/10.1016/j.cattod.2020.08.006},
pages = {141--148},
doi = {10.1016/j.cattod.2020.08.006}
}