Abstract
The immediate catalytic conversions of pyrolytic bio-oils from pine sawdust and soybean shell over mesoporous catalysts (silica, alumina, and silica-alumina) and their combinations with Y zeolite, were studied. The effect of mesoporosity and acidity on the bio-oil deoxygenation and conversion into hydrocarbons was investigated. Pyrolysis and immediate catalytic conversion of bio-oil were performed in an integrated pyrolysis–upgrading reactor, for 7 min under a 30-ml/min flow of nitrogen at 550 °C. Important differences were observed in the conversion of the bio-oils, according to the composition of the raw biomasses. Pine sawdust bio-oil produced more coke and less hydrocarbons in the range of gasoline than soybean shell bio-oil over all the catalysts. Mesoporous catalysts showed conversion and deoxygenation between 14 and 29 percentage points higher with the more acidic solid (SiO2-Al2O3) in the case of pine sawdust bio-oil and between 2 and 10 percentage points higher with the solid having the highest specific surface area (SiO2) in the case of soybean shell bio-oil. Among the compound catalysts, the best performance for the case of pine sawdust corresponded to the catalyst with the highest mesoporosity (Y/SiO2), while for soybean shell corresponded to the most acidic catalysts (Y/Al2O3 and Y/SiO2-Al2O3). Soybean shell bio-oil showed more low molecular weight compounds (less than 130 g mol−1), which diffuse more easily in the zeolite channels, thus favoring conversion and deoxygenation mechanisms. On the contrary, for pine sawdust bio-oil, the surface area contributed by the mesopores in the matrix played a key role in pre-cracking bulky molecules.
Similar content being viewed by others
Data Availability
Not applicable.
Code Availability
Not applicable.
References
Kumar R, Strezov V, Weldekidan H, He J, Singh S, Kan T, Dastjerdi B (2009) Lignocellulose biomass pyrolysis for bio-oil production: a review of biomass pre-treatment methods for production of drop-in fuels. Renew Sust Energy Review 123:109763. https://doi.org/10.1016/j.rser.2020.109763
Zacher AH, Elliott DC, Olarte MV, Wang H, Jones SB, Meyer PA (2019) Technology advancements in hydroprocessing of bio-oils. Biomass Bioenergy 12:151–168. https://doi.org/10.1016/j.biombioe.2019.04.015
Valle B, Gayubo AG, Aguayo AT, Olazar M, Bilbao J (2010) Selective production of aromatics by crude bio-oil valorization with a nickel-modified HZSM-5 zeolite catalyst. Energy Fuels 24:2060–2070. https://doi.org/10.1021/ef901231j
Al-Sabawi M, Chen J, Ng S (2012) Fluid catalytic cracking of biomass-derived oils and their blends with petroleum feedstocks: a review. Energy Fuels 26:5355–5372. https://doi.org/10.1021/ef3006417
de Rezende PA, de Almeida MBB, Leal Mendes F, Casavechia LC, Talmadge MS, Kinchin CM, Chum HL (2017) Fast pyrolysis oil from pinewood chips co-processing with vacuum gas oil in an FCC unit for second generation fuel production. Fuel 188:462–473. https://doi.org/10.1016/j.fuel.2016.10.032
Fogassy G, Thegarid N, Toussaint G, van Veen A, Schuurman Y, Mirodatos C (2010) Biomass derived feedstock co-processing with vacuum gas oil for second-generation fuel production in FCC units. Appl Catal B 96:476–485. https://doi.org/10.1016/j.apcatb.2010.03.008
Bertero M, Sedran U (2015) Co-processing of bio-oil in fluid catalytic cracking. In: Pandey A, Bhaskar T, Stocker M (eds.) Recent advances in thermo-chemical conversion of biomass. Amsterdam: Elsevier, pp 355–381. ISBN: 9780444632890
Bertero M, García JR, Falco M, Sedran U (2020) Conversion of cow manure pyrolytic tar under FCC conditions over modified equilibrium catalysts. Waste Biomass Valorization 11:2925–2933. https://doi.org/10.1007/s12649-019-00588-y
Thegarid N, Fogassy G, Schuurman Y, Mirodatos C, Stefanidis S, Iliopoulou I, Kalogiannis K, Lappas A (2014) Second generation biofuels by co-processing catalytic pyrolysis oil in FCC units. Appl Catal B Environ. 165:161–166. https://doi.org/10.1016/j.apcatb.2013.01.019
Gueudrè L, Milina M, Mitchell S, Pérez-Ramírez J (2014) Coke chemistry under vacuum gasoil/bio-oil FCC co-processing conditions. Adv Funct Mater 24:209–219. https://doi.org/10.1016/j.cattod.2014.09.001
Rezaei P, Shafaghat H, Ashri W, Daud W (2014) Production of green aromatics and olefins by catalytic cracking of oxygenate compounds derived from biomass pyrolysis: a review. Appl Catal A Gen 469:490–511. https://doi.org/10.1016/j.apcata.2013.09.036
Adam J, Antonakou E, Lappas A, Stöcker M, Nilsen MH, Bouzga A, Hustad JE, Øye G (2006) In situ catalytic upgrading of biomass derived fast pyrolysis vapours in a fixed bed reactor using mesoporous materials. Microporous Mesoporous Mater 96:93–101. https://doi.org/10.1016/j.micromeso.2006.06.021
Adjaye J, Bakhshi N (1995) Production of hydrocarbons by catalytic: upgrading of a fast pyrolysis bio-oil. Part II: comparative catalyst performance and reaction pathways. Fuel Process Technol 45:185–202. https://doi.org/10.1016/0378-3820(95)00040-E
Valle B, Castaño P, Olazar M, Bilbao J, Gayubo AG (2012) Deactivating species in the transformation of crude bio-oil with methanol into hydrocarbons on a HZSM-5 catalyst. J Catal 285:304–314. https://doi.org/10.1016/j.jcat.2011.10.004
García JR, Bertero M, Falco M, Sedran U (2015) Catalytic cracking of bio-oils improved by the formation of mesopores by means of Y zeolite desilication. Appl Catal A Gen 503:1–8. https://doi.org/10.1016/j.apcata.2014.11.005
Eschenbacher A, Jensen PA, Henriksen UB, Ahrenfeldt A, Li C, Duus JØ, Mentzel UV, Jensen AD (2019) Deoxygenation of wheat straw fast pyrolysis vapors using HZSM-5, Al2O3, HZSM-5/Al2O3 extrudates, and desilicated HZSM-5/Al2O3 extrudates. Energy Fuels 33:6405–6420. https://doi.org/10.1021/acs.energyfuels.9b00906
Scherzer J (1989) Octane-enhancing, zeolitic FCC catalysts: scientific and technical aspects. Catal Rev Sci Eng 31:215–254. https://doi.org/10.1080/01614948909349934
Wojciechowski B, Corma A, Dekker M (1986) Catalytic cracking: catalysts, chemistry and kinetics, Meisel SL (ed), New York: AIChE J, 236. https://doi.org/10.1002/aic.690330925
Gayubo AG, Aguayo AT, Atutxa A, Aguado R, Bilbao J (2004) Transformation of oxygenate components of biomass pyrolysis oil on a HZSM-5 zeolite. I. Alcohols and phenols. Ind Eng Chem Res 43:2610–2618. https://doi.org/10.1021/ie030791o
Gayubo AG, Aguayo AT, Atutxa A, Aguado R, Olazar M, Bilbao J (2004) Transformation of oxygenate components of biomass pyrolysis oil on a HZSM-5 Zeolite. II. Aldehydes, ketones and acids. Ind Eng Chem Res 43:2619–2626. https://doi.org/10.1021/ie030792g
Bertero M, Sedran U (2013) Upgrading of bio-oils over equilibrium FCC catalysts. Contribution from alcohols, phenols and aromatic ethers. Catal Today 212:10–15. https://doi.org/10.1016/j.cattod.2013.03.016
Channiwala SA, Parikh PP (2002) A unified correlation for estimating HHV of solid, liquid and gaseous fuels. Fuel 81(8):1051–1063. https://doi.org/10.1016/S0016-2361(01)00131-4
Magee JS, Blazek JJ (1976) Zeolite chemistry and catalysis, Rabo JA (ed.), ACSM N° 171, Washington, 796 p. ISBN 9780841202764
Johnson MFL (1978) Estimation of the zeolite content of a catalyst from nitrogen adsorption isotherms. J Catal 52:425–431. https://doi.org/10.1016/0021-9517(78)90346-9
Bertero M, de la Puente G, Sedran U (2012) Fuels from bio-oils. Bio-oil production from different sources, characterization and thermal conditioning. Fuel 95:263–271. https://doi.org/10.1016/j.fuel.2011.08.041
Gayubo AG, Valle B, Aguayo A, Olazar M, Bilbao J (2010) Olefin production by catalytic transformation of crude bio-oil in a two-step process. Ind Eng Chem Res 49:123–131. https://doi.org/10.1021/ie901204n
Gilbert W, Morgado E, de Abreu M, de la Puente G, Passamonti F, Sedran U (2011) A novel fluid catalytic cracking approach for producing low aromatic LCO. Fuel Process Technol 92:2235–2240. https://doi.org/10.1016/j.fuproc.2011.07.006
Seddegi ZS, Budrthumal U, Al-Arfaj AA, Al-Amer AM, Barri SA (2002) Catalytic cracking of polyethylene over all-silica MCM-41 molecular sieve. App Catal A: Gen 225:167–176. https://doi.org/10.1016/S0926-860X(01)00872-9
Bertero M, Sedran U (2016) Immediate catalytic upgrading of soybean shell bio-oil. Energy 94:171–179. https://doi.org/10.1016/j.energy.2015.10.114
Yang S, Wu M, Wu C (2014) Application of biomass fast pyrolysis part I: pyrolysis characteristics and products. Energy 66:162–171. https://doi.org/10.1016/j.energy.2013.12.063
Pütün A, Apaydin E, Pütün E (2002) Bio-oil production from pyrolysis and steam pyrolysis of soybean cake: products yields and composition. Energy 27:703–710. https://doi.org/10.1016/S0360-5442(02)00015-4
Iliopoulou E, Antonakou E, Karakoulia S, Vasalos I, Lappas A, Triantafyllidis K (2007) Catalytic conversion of biomass pyrolysis products by mesoporous materials: effect of steam stability and acidity of Al-MCM-41 catalysts. Chem Eng J 134:51–57. https://doi.org/10.1016/j.cej.2007.03.066
Cerqueira H, Caeiro G, Costa L, Ramôa Ribeiro F (2008) Deactivation of FCC catalysts. J Molec Catal A: Chemical 292:1–13. https://doi.org/10.1016/j.molcata.2008.06.014
Lappas AA, Samolada MC, Iatridis DK, Voutetakis SS, Vasalos IA (2002) Biomass pyrolysis in a circulating fluid bed reactor for the production of fuels and chemicals. Fuel 81:2087–2095. https://doi.org/10.1016/S0016-2361(02)00195-3
Bertero M, de la Puente G, Sedran U (2013) Products and coke from the conversion of bio-oil acids, esters, aldehydes and ketones over equilibrium FCC catalysts. Renew Energy 60:349–354. https://doi.org/10.1016/j.renene.2013.04.017
Corma A, Huber G, Sauvanaud L, O’Connor P (2007) Processing biomass-derived oxygenates in the oil refinery: catalytic cracking (FCC) reaction pathways and role of catalyst. J Catal 247:307–327. https://doi.org/10.1016/j.jcat.2007.01.023
Moldoveanu SC (2019) Pyrolysis of organic molecules with applications to health and environmental issues - techniques and instrumentation in analytical chemistry. 2nd Edition https://doi.org/10.1016/B978-0-444-64000-0.00001-9
Adjaye JD, Bakhshi NN (1995) Catalytic conversion of a biomass-derived oil to fuels and chemicals I: model compound studies and reaction pathways. Biomass Bioenergy 8:131–149. https://doi.org/10.1016/0961-9534(95)00018-3
Chantal P, Kaliaguine S, Grandmaison JL (1985) Reactions of phenolic compounds over HZSM-5. Appl Catal 18:133–145. https://doi.org/10.1016/S0166-9834(00)80304-8
Wang S, Cai Q, Chen J, Zhang L, Zhu L, Luo Z (2015) Co-cracking of bio-oil model compound mixtures and ethanol over different metal oxide-modified HZSM-5 catalysts. Fuel 160:534–543. https://doi.org/10.1016/j.fuel.2015.08.011
Wang S, Guo Z, Cai Q, Guo L (2012) Catalytic conversion of carboxylic acids in bio-oil for liquid hydrocarbons production. Biomass Bioenergy 45:138–143. https://doi.org/10.1016/j.biombioe.2012.05.023
Chen G, Zhang R, Ma W, Liu B, Li X, Yan B, Cheng Z, Wang T (2018) Catalytic cracking of model compounds of bio-oil over HZSM-5 and the catalyst deactivation. Sci Total Environ 631–632:1611–1622. https://doi.org/10.1016/j.scitotenv.2018.03.147
Chen G, Liu J, Li X, Zhang J, Yin H, Su Z (2020) Investigation on catalytic hydrodeoxygenation of eugenol blend with light fraction in bio-oil over Ni-based catalysts. Renew Energy 157:456–465. https://doi.org/10.1016/j.renene.2020.05.040
Chen W, Luo Z, Yu C, Yang Y, Li G, Zhang J (2014) Catalytic conversion of guaiacol in ethanol for bio-oil upgrading to stable oxygenated organics. Fuel Process Technol 126:420–428. https://doi.org/10.1016/j.fuproc.2014.05.022
Venkatesan K, Krishna JVJ, Anjana S, Selvam P, Vinu R (2021) Hydrodeoxygenation kinetics of syringol, guaiacol and phenol over H-ZSM-5. Catal Commun 148:106–164. https://doi.org/10.1016/j.catcom.2020.106164
Adjaye JD, Katikaneni SPR, Bakhshi NN (1996) Catalytic conversion of a biofuel to hydrocarbons: effect of mixtures of HZSM-5 and silica-alumina catalysts on product distribution. Fuel Proc Tech 48:115–143. https://doi.org/10.1016/S0378-3820(96)01031-4
Olazar M, Aguado R, Barona A, Bilbao J (2000) Pyrolysis of sawdust in a conical spouted bed reactor with a HZSM-5 catalyst. AIChE J 46:1025–1033. https://doi.org/10.1002/aic.690460514
Ibarra A, Hita I, Azkoiti MJ, Arandes JM, Bilbao J (2019) Catalytic cracking of raw bio-oil under FCC unit conditions over different zeolite-based catalysts. J Ind Eng Chem 78:372–382. https://doi.org/10.1016/j.jiec.2019.05.032
Naqvi SR, Uemura Y, Yusup S, Sugiur Y, Nishiyama N, Naqvi M (2015) The role of zeolite structure and acidity in catalytic deoxygenation of biomass pyrolysis vapors. Energy Procedia 75:793–800. https://doi.org/10.1016/j.egypro.2015.07.126
Mochizuki T, Atong D, Chen SY, Toba M, Yoshimura Y (2013) Effect of SiO2 pore size on catalytic fast pyrolysis of Jatropha residues by using pyrolyzer-GC/MS Cat. Comm 26:1–4. https://doi.org/10.1016/j.catcom.2013.02.018
Stefanidis SD, Kalogiannis KG, Iliopoulou EF, Lappas AA, Pilavachi PA (2011) In-situ upgrading of biomass pyrolysis vapors: catalyst screening on a fixed bed reactor. Biores Tech 102:8261–8267. https://doi.org/10.1016/j.biortech.2011.06.032
Carlson T, Tompsett G, Conner W, Huber G (2009) Aromatic production from catalytic fast pyrolysis of biomass-derived feedstocks. Top Catal 52:241–252. https://doi.org/10.1007/s11244-008-9160-6
Park H, Dong J, Jeon J, SeunYoo K, Yim J, Min Sohn J, Park Y (2007) Conversion of the pyrolytic vapor of radiata pine over zeolites. J Ind Eng Chem 13:182–189
Graça I, Ramôa Ribeiro F, Cerqueira HS, Lam YL, de Almeida MBB (2009) Catalytic cracking of mixtures of model bio-oil compounds and gasoil. App Catal B: Env 90:556–563. https://doi.org/10.1016/j.apcatb.2009.04.010
Gong F, Yang Z, Hong C, Huang W, Ning S, Zhang Z, Xu Y, Li Q (2011) Selective conversion of bio-oil to light olefins: controlling catalytic cracking for maximum olefins. Bior Tech 102:9247–9254. https://doi.org/10.1016/j.biortech.2011.07.009
Bertero M, García JR, Falco M, Sedran U (2017) Hydrocarbons from bio-oils: performance of the matrix in FCC catalysts in the immediate catalytic upgrading of different raw bio-oils. Waste Biomass Valor 8:933–948. https://doi.org/10.1007/s12649-016-9624-z
de la Puente G, Falabella E, Sousa-Aguiar M, Figueiredo Costa A, Sedran U (2003) The influence on selectivity of the aluminum content in the matrix of FCC catalysts. Appl Catal A: General 242:381–391. https://doi.org/10.1016/S0926-860X(02)00526-4
Samolada M, Papafotica A, Vasalos I (2000) Catalyst evaluation for catalytic biomass pyrolysis. Energy Fuels 14:1161–1167. https://doi.org/10.1021/ef000026b
Fuhse J, Bandermann F (1987) Conversion of organic oxygenated compounds and their mixtures on H-ZSM5. Chem Eng Technol 10:323–329. https://doi.org/10.1002/ceat.270100139
To AT, Resasco D (2014) Role of a phenolic pool in the conversion of m-cresol to aromatics over HY and HZSM-5 zeolites. Appl Catal A: Gral 487:62–71. https://doi.org/10.1016/j.apcata.2014.09.006
Gayubo AG, Aguayo A, Atutxa A, Prieto R, Bilbao J (2004) Deactivation of a HZSM-5 zeolite catalyst in the transformation of the aqueous fraction of biomass pyrolysis oil into hydrocarbons. Energy Fuels 18:1640–1647. https://doi.org/10.1021/ef040027u
Ibáñez M, Valle B, Bilbao J, Gayubo AG, Castaño P (2012) Effect of operating conditions on the coke nature and HZSM-5 catalysts deactivation in the transformation of crude bio-oil into hydrocarbons. Catal Today 195:106–113. https://doi.org/10.1016/j.cattod.2012.04.030
Zhou S, Garcia-Perez M, Pecha B, Kersten SRA, McDonald AG, Westerhof RJM (2013) Effect of the fast pyrolysis temperature on the primary and secondary products of lignin. Energy Fuels 27:5867–5877. https://doi.org/10.1021/ef4001677
Bai X, Kim KH, Brown RC, Dalluge E, Hutchinson C, Lee YJ, Dalluge D (2014) Formation of phenolic oligomers during fast pyrolysis of lignin. Fuel 128:170–179. https://doi.org/10.1016/j.fuel.2014.03.013
Funding
This work was carried out with financial support of the University of Litoral (UNL, Santa Fe, Argentina), Secretary of Science and Technology, Proj. CAID 50420150100068LI, and the National Agency for Scientific and Technological Promotion (ANPCyT), PICT 1208/2016.
Author information
Authors and Affiliations
Contributions
Investigation, formal analysis, writing—original draft, data curation, conceptualization: Melisa Bertero and Juan Rafael García. Visualization, conceptualization, supervision, methodology, resources, project administration: Marisa Falco and Ulises Sedran. Writing—review and editing, funding acquisition: Ulises Sedran.
Corresponding author
Ethics declarations
Competing Interests
The authors declare no competing interests.
Additional information
Publisher's Note
Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.
Supplementary Information
Below is the link to the electronic supplementary material.
Rights and permissions
About this article
Cite this article
Bertero, M., García, J.R., Falco, M. et al. FCC Matrix Components and Their Combination with Y Zeolite to Enhance the Deoxygenation of Bio-oils. Bioenerg. Res. 15, 1327–1341 (2022). https://doi.org/10.1007/s12155-021-10322-z
Received:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s12155-021-10322-z