Production of High Quality Syncrude from Lignocellulosic Biomass

[EN] Wood chips were hydrothermally treated in near critical point water in the presence of a catalyst to yield a raw biocrude, containing a wide range of organic components. This product was subsequently distilled to remove its heaviest fraction, which tends to yield chary products if heated above 350 degrees C. The biocrude obtained has an oxygen content of 12wt% and was subsequently hydrotreated to obtain a hydrocarbon stream. Varying the hydrotreatment operating conditions and catalyst yielded a deoxygenated syncrude which quality improved with operation severity. The hydroprocessed stream produced under very mild conditions can be further upgraded in conventional refinery operations while the stream produced after more severe hydrotreatment can be mixed with conventional diesel. This proof of concept was demonstrated with commercial hydrotreating catalysts, operating between 350 and 380 degrees C, 40 to 120bar pressure and 0.5 to 1h(-1) contact time.The authors thank Licella for material and financial support, as well as providing the biocrude used for the hydrotreating experiments. Licella gratefully acknowledges support from the Australian Government in the form of funding as part of the Advanced Biofuels Investment Readiness Program, received through the Australian Renewable Energy Agency (ARENA). Financial support by the Spanish Government-MINECO through program "Severo Ochoa" (SEV 2012-0267), CTQ2015-70126-R (MINECO/FEDER), and by the Generalitat Valenciana through the Prometeo program (PROMETEOII/2013/011) is also acknowledged.Mathieu, Y.; Sauvanaud, LL.; Humphreys, L.; Rowlands, W.; Maschmeyer, T.; Corma Canós, A. (2017). Production of High Quality Syncrude from Lignocellulosic Biomass. ChemCatChem. 9(9):1574-1578. https://doi.org/10.1002/cctc.201601677S1574157899Huber, G. W., & Corma, A. (2007). Synergies between Bio- and Oil Refineries for the Production of Fuels from Biomass. Angewandte Chemie International Edition, 46(38), 7184-7201. doi:10.1002/anie.200604504Huber, G. W., & Corma, A. (2007). Synergien zwischen Bio- und Ölraffinerien bei der Herstellung von Biomassetreibstoffen. Angewandte Chemie, 119(38), 7320-7338. doi:10.1002/ange.200604504U.S. Department of Energy 2016.2016 Billion-Ton Report: Advancing Domestic Resources for a Thriving Bioeconomy Volume 1: Economic Availability of Feedstocks. M. H. Langholtz B. J. Stokes L. M. Eaton (Leads) ORNL/TM-2016/160. Oak Ridge National Laboratory Oak Ridge TN. 448p. DOI:10.2172/1271651.Klein-Marcuschamer, D., & Blanch, H. W. (2015). Renewable fuels from biomass: Technical hurdles and economic assessment of biological routes. AIChE Journal, 61(9), 2689-2701. doi:10.1002/aic.14755Maitlis, P. M., & de Klerk, A. (2013). New Directions, Challenges, and Opportunities. Greener Fischer-Tropsch Processes for Fuels and Feedstocks, 337-358. doi:10.1002/9783527656837.ch16De Miguel Mercader, F., Groeneveld, M. J., Kersten, S. R. A., Geantet, C., Toussaint, G., Way, N. W. J., … Hogendoorn, K. J. A. (2011). Hydrodeoxygenation of pyrolysis oil fractions: process understanding and quality assessment through co-processing in refinery units. Energy & Environmental Science, 4(3), 985. doi:10.1039/c0ee00523aGoudriaan, F., & Peferoen, D. G. R. (1990). Liquid fuels from biomass via a hydrothermal process. Chemical Engineering Science, 45(8), 2729-2734. doi:10.1016/0009-2509(90)80164-aPeterson, A. A., Vogel, F., Lachance, R. P., Fröling, M., Antal, Jr., M. J., & Tester, J. W. (2008). Thermochemical biofuel production in hydrothermal media: A review of sub- and supercritical water technologies. Energy & Environmental Science, 1(1), 32. doi:10.1039/b810100kToor, S. S., Rosendahl, L., & Rudolf, A. (2011). Hydrothermal liquefaction of biomass: A review of subcritical water technologies. Energy, 36(5), 2328-2342. doi:10.1016/j.energy.2011.03.013Oasmaa, A., & Czernik, S. (1999). Fuel Oil Quality of Biomass Pyrolysis OilsState of the Art for the End Users. Energy & Fuels, 13(4), 914-921. doi:10.1021/ef980272bElliott, D. C., Biller, P., Ross, A. B., Schmidt, A. J., & Jones, S. B. (2015). Hydrothermal liquefaction of biomass: Developments from batch to continuous process. Bioresource Technology, 178, 147-156. doi:10.1016/j.biortech.2014.09.132http://www.licella.com.au/commercial-demonstration-plant/.L. J.Humphreys (Ignite Energy Resources Pty Ltd) WO Pat. 2011/032202(A1) 2011.T.Maschmeyer L. J.Humphreys (Licella Pty Ltd) WO Pat. 2011/123897(A1) 2011.Wang, W., Yang, Y., Luo, H., Hu, T., & Liu, W. (2011). Amorphous Co–Mo–B catalyst with high activity for the hydrodeoxygenation of bio-oil. Catalysis Communications, 12(6), 436-440. doi:10.1016/j.catcom.2010.11.001Monnier, J., Sulimma, H., Dalai, A., & Caravaggio, G. (2010). Hydrodeoxygenation of oleic acid and canola oil over alumina-supported metal nitrides. Applied Catalysis A: General, 382(2), 176-180. doi:10.1016/j.apcata.2010.04.035Kubička, D., & Kaluža, L. (2010). Deoxygenation of vegetable oils over sulfided Ni, Mo and NiMo catalysts. Applied Catalysis A: General, 372(2), 199-208. doi:10.1016/j.apcata.2009.10.034Huber, G. W., O’Connor, P., & Corma, A. (2007). Processing biomass in conventional oil refineries: Production of high quality diesel by hydrotreating vegetable oils in heavy vacuum oil mixtures. Applied Catalysis A: General, 329, 120-129. doi:10.1016/j.apcata.2007.07.002Anthonykutty, J. M., Van Geem, K. M., De Bruycker, R., Linnekoski, J., Laitinen, A., Räsänen, J., … Lehtonen, J. (2013). Value Added Hydrocarbons from Distilled Tall Oil via Hydrotreating over a Commercial NiMo Catalyst. Industrial & Engineering Chemistry Research, 52(30), 10114-10125. doi:10.1021/ie400790vH. P.Ruyter J. H. J.Annee (Shell Oil Co) US Pat. no. 4670613A 1987.S. Jones et al. Process Design and Economics for the Conversion of Algal Biomass to Hydrocarbons: Whole Algae Hydrothermal Liquefaction and Upgrading PNNL report 23227 2014.Baker, E. G., & Elliott, D. C. (1988). Catalytic Hydrotreating of Biomass-Derived Oils. Pyrolysis Oils from Biomass, 228-240. doi:10.1021/bk-1988-0376.ch021Kubička, D., & Horáček, J. (2011). Deactivation of HDS catalysts in deoxygenation of vegetable oils. Applied Catalysis A: General, 394(1-2), 9-17. doi:10.1016/j.apcata.2010.10.03

Opportunities in upgrading biomass crudes

[EN] An unconventional crude from biomass (biocrude) has been processed to yield a hydrocarbon stream that is not only fully processable in conventional refineries but is already close to the specification of commercial fuels such as transportation diesel. The upgrading of biocrude was carried out with a combination of hydrotreatment and catalytic cracking, yielding middle distillate as the main product.The authors thank Licella for material and financial support, as well as providing the biocrude used for the hydrotreating experiments. Licella gratefully acknowledges support from the Australian Government in the form of funding as part of the Advanced Biofuels Investment Readiness Program, received through the Australian Renewable Energy Agency (ARENA). Financial support by the Spanish Government-MINECO through program "Severo Ochoa" (SEV 2012-0267), CTQ2015-70126-R (MINECO/FEDER), and by the Generalitat Valenciana through the Prometeo program (PROMETEOII/2013/011) is also acknowledged.Mathieu, Y.; Sauvanaud, LL.; Humphreys, L.; Rowlands, W.; Maschmeyer, T.; Corma Canós, A. (2017). Opportunities in upgrading biomass crudes. Faraday Discussions. 197:389-401. https://doi.org/10.1039/c6fd00208kS389401197U.S. Department of Energy. 2016. 2016 Billion-Ton Report: Advancing Domestic Resources for a Thriving Bioeconomy, Volume 1: Economic Availability of Feedstocks. M. H. Langholtz, B. J. Stokes, and L. M. Eaton (Leads), ORNL/TM-2016/160. Oak Ridge National Laboratory, Oak Ridge, TN. 448ppP. M. Maitlis and A.de Klerk, Greener Fischer-Tropsch Processes for Fuels and Feedstocks, Wiley, 2013, ch. 16De Miguel Mercader, F., Groeneveld, M. J., Kersten, S. R. A., Geantet, C., Toussaint, G., Way, N. W. J., … Hogendoorn, K. J. A. (2011). Hydrodeoxygenation of pyrolysis oil fractions: process understanding and quality assessment through co-processing in refinery units. Energy & Environmental Science, 4(3), 985. doi:10.1039/c0ee00523aGoudriaan, F., & Peferoen, D. G. R. (1990). Liquid fuels from biomass via a hydrothermal process. Chemical Engineering Science, 45(8), 2729-2734. doi:10.1016/0009-2509(90)80164-aPeterson, A. A., Vogel, F., Lachance, R. P., Fröling, M., Antal, Jr., M. J., & Tester, J. W. (2008). Thermochemical biofuel production in hydrothermal media: A review of sub- and supercritical water technologies. Energy & Environmental Science, 1(1), 32. doi:10.1039/b810100kToor, S. S., Rosendahl, L., & Rudolf, A. (2011). Hydrothermal liquefaction of biomass: A review of subcritical water technologies. Energy, 36(5), 2328-2342. doi:10.1016/j.energy.2011.03.013Oasmaa, A., & Czernik, S. (1999). Fuel Oil Quality of Biomass Pyrolysis OilsState of the Art for the End Users. Energy & Fuels, 13(4), 914-921. doi:10.1021/ef980272bhttp://www.licella.com.au/commercial-demonstration-plant/Bridgwater, A. V. (1994). Catalysis in thermal biomass conversion. Applied Catalysis A: General, 116(1-2), 5-47. doi:10.1016/0926-860x(94)80278-5De Miguel Mercader, F., Groeneveld, M. J., Kersten, S. R. A., Way, N. W. J., Schaverien, C. J., & Hogendoorn, J. A. (2010). Production of advanced biofuels: Co-processing of upgraded pyrolysis oil in standard refinery units. Applied Catalysis B: Environmental, 96(1-2), 57-66. doi:10.1016/j.apcatb.2010.01.033Wang, C., Li, M., & Fang, Y. (2016). Coprocessing of Catalytic-Pyrolysis-Derived Bio-Oil with VGO in a Pilot-Scale FCC Riser. Industrial & Engineering Chemistry Research, 55(12), 3525-3534. doi:10.1021/acs.iecr.5b03008Fogassy, G., Thegarid, N., Schuurman, Y., & Mirodatos, C. (2012). The fate of bio-carbon in FCC co-processing products. Green Chemistry, 14(5), 1367. doi:10.1039/c2gc35152hRezaei, P. S., Shafaghat, H., & Daud, W. M. A. W. (2014). Production of green aromatics and olefins by catalytic cracking of oxygenate compounds derived from biomass pyrolysis: A review. Applied Catalysis A: General, 469, 490-511. doi:10.1016/j.apcata.2013.09.036Hughes, R., Hutchings, G. J., Koon, C. L., McGhee, B., Snape, C. E., & Yu, D. (1996). Deactivation of FCC catalysts using n-hexadecane feed with various additives. Applied Catalysis A: General, 144(1-2), 269-279. doi:10.1016/0926-860x(96)00106-8Huber, G. W., O’Connor, P., & Corma, A. (2007). Processing biomass in conventional oil refineries: Production of high quality diesel by hydrotreating vegetable oils in heavy vacuum oil mixtures. Applied Catalysis A: General, 329, 120-129. doi:10.1016/j.apcata.2007.07.002Anthonykutty, J. M., Van Geem, K. M., De Bruycker, R., Linnekoski, J., Laitinen, A., Räsänen, J., … Lehtonen, J. (2013). Value Added Hydrocarbons from Distilled Tall Oil via Hydrotreating over a Commercial NiMo Catalyst. Industrial & Engineering Chemistry Research, 52(30), 10114-10125. doi:10.1021/ie400790vS. Jones , Y.Zu, D.Anderson, R.Allen, D.Elliot, A.Schmidt, K.Albrecht, T.Hart, M.Butcher, C.Drennan, L.Snowden-Swan, R.Davis and C.Kinchin, PNNL report 23227, March 2014Corma, A., González-Alfaro, V., & Orchillés, A. . (2001). Decalin and Tetralin as Probe Molecules for Cracking and Hydrotreating the Light Cycle Oil. Journal of Catalysis, 200(1), 34-44. doi:10.1006/jcat.2001.3181CORMA, A., & ORTEGA, F. (2005). Influence of adsorption parameters on catalytic cracking and catalyst decay. Journal of Catalysis, 233(2), 257-265. doi:10.1016/j.jcat.2005.04.02

COVID-19 vaccine acceptance and hesitancy in low- and middle-income countries

Widespread acceptance of COVID-19 vaccines is crucial for achieving sufficient immunization coverage to end the global pandemic, yet few studies have investigated COVID-19 vaccination attitudes in lower-income countries, where large-scale vaccination is just beginning. We analyze COVID-19 vaccine acceptance across 15 survey samples covering 10 low- and middle-income countries (LMICs) in Asia, Africa and South America, Russia (an upper-middle-income country) and the United States, including a total of 44,260 individuals. We find considerably higher willingness to take a COVID-19 vaccine in our LMIC samples (mean 80.3%; median 78%; range 30.1 percentage points) compared with the United States (mean 64.6%) and Russia (mean 30.4%). Vaccine acceptance in LMICs is primarily explained by an interest in personal protection against COVID-19, while concern about side effects is the most common reason for hesitancy. Health workers are the most trusted sources of guidance about COVID-19 vaccines. Evidence from this sample of LMICs suggests that prioritizing vaccine distribution to the Global South should yield high returns in advancing global immunization coverage. Vaccination campaigns should focus on translating the high levels of stated acceptance into actual uptake. Messages highlighting vaccine efficacy and safety, delivered by healthcare workers, could be effective for addressing any remaining hesitancy in the analyzed LMICs.Publisher PDFPeer reviewe

Co-processing of lignocellulosic biocrude with petroleum gas oils

[EN] A biocrude was obtained via the catalytic hydrothermal treatment of lignocellulosic biomass. This was further co-hydroprocessed with Straight Run Gas Oil (SRGO) under desulphurization conditions. Amounts of biocrude of up to 20 wt% could be co-processed, while maintaining a diesel stream density within the specifications contained in the road diesel regulation EN 590. The changes in the diesel properties associated with an increasing amount of biocrude were not a simple linear function of biocrude content. Rather, some positive correlations seem to exist between biocrude and SRGO at low biocrude contents, possibly due to intramolecular hydrogen transfer, yielding a diesel stream with a better quality than would be obtained from simply mixing hydrotreated pure streams in a 80% to 20% ratio.The authors thank Licella for providing the Biocrude and financial support. Licella gratefully acknowledges support from the Australian Government in the form of funding as part of the Advanced Biofuels Investment Readiness Program, received through the Australian Renewable Energy Agency (ARENA). Financial support by the Spanish Government-MINECO through program "Severn Ochoa" (SEV 2016-0683), CTQ2015-70126-R (MINECO/FEDER), and by the Generalitat Valenciana through the Prometeo program (PROMETEOII/2013/011) is also acknowledged.Sauvanaud, LL.; Mathieu, Y.; Corma Canós, A.; Humphreys, L.; Rowlands, W.; Maschmeyer, T. (2018). Co-processing of lignocellulosic biocrude with petroleum gas oils. Applied Catalysis A General. 551:139-145. https://doi.org/10.1016/j.apcata.2017.09.029S13914555