2015
DOI: 10.1021/acs.energyfuels.5b01625
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Effects of Mild Alkali Pretreatment and Hydrogen-Donating Solvent on Hydrothermal Liquefaction of Eucalyptus Woodchips

Abstract: Eucalyptus woodchips (EWC) were pretreated with mild aqueous NaOH solution, followed by liquefaction in a water–hydrogen donor (tetralin) mixture at a temperature from 220 to 330 °C to produce bio-oil. As a reference, pure tetralin and water were also used as liquefaction media. Compositional analysis and scanning electron microscopy (SEM) observation were performed to study the effect of the pretreatment on the EWC structural change. The influences of the temperature and tetralin content in mixed solvent on c… Show more

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Cited by 10 publications
(14 citation statements)
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“…[180] In addition to hydrogen donor solvents, non-hydrogen donor solvents (e. g., pyrene and fluoranthene) may also enhance the plastic waste conversion and the quality of fuel, as similar findings were found when converting biomass. [181] Alcohols such as ethanol have a lower dielectric constant than water, providing a better solubility of organic compounds at ambient and supercritical conditions. Most importantly, alcohols have lower corrosivity and also have hydrogen donation capability, preventing char formation and thus leading Figure 14.…”
Section: Reaction Parametersmentioning
confidence: 99%
“…[180] In addition to hydrogen donor solvents, non-hydrogen donor solvents (e. g., pyrene and fluoranthene) may also enhance the plastic waste conversion and the quality of fuel, as similar findings were found when converting biomass. [181] Alcohols such as ethanol have a lower dielectric constant than water, providing a better solubility of organic compounds at ambient and supercritical conditions. Most importantly, alcohols have lower corrosivity and also have hydrogen donation capability, preventing char formation and thus leading Figure 14.…”
Section: Reaction Parametersmentioning
confidence: 99%
“…We recommend initially focusing on non‐supercritical hydrothermal liquefaction as the front‐end for processing the initial candidate feedstocks because of its omnivorism (Elliott, ; Lu, Yang, Wang, & Yang, ), ready scalability (Barreiro, Gómez, Hornung, Kruse, & Prins, ; Inoue, Okuma, Masuda, Yasumuro, & Miura, ), tolerance of wet feedstocks, and demonstrated production of a tractable bio‐oil (Elliott, ; Goudriaan & Peferoen, ) with an attractive greenhouse gas footprint (Connelly, Colosi, Clarens, & Lambert, ) (see Appendix). Examples of feedstocks that have been processed with hydrothermal liquefaction include wood (Zhixia Li et al, ), cellulose (Nan, Shende, Shannon, & Shende, ), microalgae (Barreiro et al, ; Brown, Duan, & Savage, ; Connelly et al, ; Faeth, Valdez, & Savage, ), macroalgae (Zhou, Zhang, Zhang, Fu, & Chen, ), food waste (Anouti, Haarlemmer, Déniel, & Roubaud, ), sewage sludge (Snowden‐Swan et al, ), and municipal solid waste (Chiaberge et al, ). Another process, IH 2 ® from the Gas Technology Institute (Marker et al, ), offers some of those benefits but requires high pressures (>160 bar) of hydrogen, and therefore poses a safety concern and a logistical issue (getting the product to its customers).…”
Section: Technology Roadmapmentioning
confidence: 99%
“…Two feasible methods for the valorization of lignocellulosic biomass for bioenergy applications are: (1) fermentation of sugars from cellulose and hemicellulose components to biofuel [21] or (2) hydrothermal liquefaction and gasification to produce bio-oil [93,94,95] and biogas [96,97] (Figure 1 and Figure 3). In all these methods, pretreatment and solvation are critical steps, and it is important to find green solvents that can substitute the previously used hazardous solvents.…”
Section: Introductionmentioning
confidence: 99%