Recent Advances in Hydroliquefaction of Biomass for Bio-oil Production Using In Situ Hydrogen Donors

2020 ◽  
Vol 59 (39) ◽  
pp. 16987-17007 ◽  
Author(s):  
Bojun Zhao ◽  
Yulin Hu ◽  
Jihui Gao ◽  
Guangbo Zhao ◽  
Madhumita B. Ray ◽  
...  
2020 ◽  
Vol 149 ◽  
pp. 104845
Author(s):  
Leilei Dai ◽  
Nan Zhou ◽  
Hui Li ◽  
Wenyi Deng ◽  
Yanling Cheng ◽  
...  

2022 ◽  
Vol 518 ◽  
pp. 112052
Author(s):  
Ana Alice Farias da Costa ◽  
Luiza Helena de Oliveira Pires ◽  
Daily Rodríguez Padrón ◽  
Alina M. Balu ◽  
Geraldo Narciso da Rocha Filho ◽  
...  

2009 ◽  
Vol 2 (1) ◽  
pp. 34-39
Author(s):  
Walfrido Alonso-Pippo ◽  
Carlos A. Luengo ◽  
Felix F. Fonseca ◽  
Pietro Garzone ◽  
Giacinto Cornacchia

2017 ◽  
Vol 60 ◽  
pp. 357-362 ◽  
Author(s):  
Jia Wang ◽  
Zhaoping Zhong ◽  
Bo Zhang ◽  
Kuan Ding ◽  
Zeyu Xue ◽  
...  

2020 ◽  
Vol 7 (1) ◽  
pp. 29-36
Author(s):  
Antonina A. Stepacheva ◽  
Mariia E. Markova ◽  
Yury V. Lugovoy ◽  
Kirill V. Chalov ◽  
Mikhail G. Sulman ◽  
...  

AbstractHydrotreatment of bio-oil oxygen compounds allows the final product to be effectively used as a liquid transportation fuel from biomass. Deoxygenation is considered to be one of the most promising ways for bio-oil upgrading. In the current work, we describe a novel approach for the deoxygenation of bio-oil model compounds (anisole, guaiacol) using supercritical fluids as both the solvent and hydrogen-donors. We estimated the possibility of the use of complex solvent consisting of non-polar n-hexane with low critical points (Tc = 234.5 ºC, Pc = 3.02 MPa) and propanol-2 used as H-donor. The experiments were performed without catalysts and in the presence of noble and transition metals hydrothermally deposited on the polymeric matrix of hypercrosslinked polystyrene (HPS). The experiments showed that the presence of 20 vol. % of propanol-2 in n-hexane results in the highest (up to 99%) conversion of model compounds. When the process was carried out without a catalyst, phenols were found to be a major product yielding up to 95 %. The use of Pd- and Co-containing catalyst yielded 90 % of aromatic compounds (benzene and toluene) while in the presence of Ru and Ni cyclohexane and methylcyclohexane (up to 98 %) were the main products.


2021 ◽  
Vol 657 (1) ◽  
pp. 012023
Author(s):  
Zengtong Deng ◽  
Yi Wang ◽  
Song Hu ◽  
Sheng Su ◽  
Long Jiang ◽  
...  
Keyword(s):  

2019 ◽  
Vol 12 (1) ◽  
Author(s):  
Pratik Prashant Pawar ◽  
Annamma Anil Odaneth ◽  
Rajeshkumar Natwarlal Vadgama ◽  
Arvind Mallinath Lali

Abstract Background Recent trends in bioprocessing have underlined the significance of lignocellulosic biomass conversions for biofuel production. These conversions demand at least 90% energy upgradation of cellulosic sugars to generate renewable drop-in biofuel precursors (Heff/C ~ 2). Chemical methods fail to achieve this without substantial loss of carbon; whereas, oleaginous biological systems propose a greener upgradation route by producing oil from sugars with 30% theoretical yields. However, these oleaginous systems cannot compete with the commercial volumes of vegetable oils in terms of overall oil yields and productivities. One of the significant challenges in the commercial exploitation of these microbial oils lies in the inefficient recovery of the produced oil. This issue has been addressed using highly selective oil capturing agents (OCA), which allow a concomitant microbial oil production and in situ oil recovery process. Results Adsorbent-based oil capturing agents were employed for simultaneous in situ oil recovery in the fermentative production broths. Yarrowia lipolytica, a model oleaginous yeast, was milked incessantly for oil production over 380 h in a media comprising of glucose as a sole carbon and nutrient source. This was achieved by continuous online capture of extracellular oil from the aqueous media and also the cell surface, by fluidizing the fermentation broth over an adsorbent bed of oil capturing agents (OCA). A consistent oil yield of 0.33 g per g of glucose consumed, corresponding to theoretical oil yield over glucose, was achieved using this approach. While the incorporation of the OCA increased the oil content up to 89% with complete substrate consumptions, it also caused an overall process integration. Conclusion The nondisruptive oil capture mediated by an OCA helped in accomplishing a trade-off between microbial oil production and its recovery. This strategy helped in realizing theoretically efficient sugar-to-oil bioconversions in a continuous production process. The process, therefore, endorses a sustainable production of molecular drop-in equivalents through oleaginous yeasts, representing as an absolute microbial oil factory.


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