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      Upgrading of Light Bio-oil from Solvothermolysis Liquefaction of an Oil Palm Empty Fruit Bunch in Glycerol by Catalytic Hydrodeoxygenation Using NiMo/Al 2O 3 or CoMo/Al 2O 3 Catalysts

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          Abstract

          Hydrodeoxygenation (HDO) of bio-oil derived from liquefaction of a palm empty fruit bunch (EFB) in glycerol was investigated. To enhance the heating value and reduce the oxygen content of upgraded bio-oil, hydrodeoxygenation of light bio-oil over Ni- and Co-based catalysts on an Al 2O 3 support was performed in a rotating-bed reactor. Two consecutive steps were conducted to produce bio-oil from EFB including (1) microwave-assisted wet torrefaction of EFB and (2) solvothermolysis liquefaction of treated EFB in a Na 2CO 3/glycerol system. The HDO of as-prepared bio-oil was subsequently performed in a unique design reactor possessing a rotating catalyst bed for efficient interaction of a catalyst with bio-oil and facile separation of the catalyst from upgraded bio-oil after the reaction. The reaction was carried out in the presence of each mono- or bimetallic catalyst, namely, Co/Al 2O 3, Ni/Al 2O 3, NiMo/Al 2O 3, and CoMo/Al 2O 3, packed in the rotating-mesh host with a rotation speed of 250 rpm and kept at 300 and 350 °C, 2 MPa hydrogen for 1 h. From the results, the qualities of upgraded bio-oil were substantially improved for all catalysts tested in terms of oxygen reduction and increased high heating value (HHV). Particularly, the NiMo/Al 2O 3 catalyst exhibited the most promising catalyst, providing favorable bio-oil yield and HHV. Remarkably greater energy ratios and carbon recovery together with high H/O, C/O, and H/C ratios were additionally achieved from the NiMo/Al 2O 3 catalyst compared with other catalysts. Cyclopentanone and cyclopentene were the main olefins found in hydrodeoxygenated bio-oil derived from liquefied EFB. It was observed that cyclopentene was first generated and subsequently converted to cyclopentanone under the hydrogenation reaction. These compounds can be further used as a building block in the synthesis of jet-fuel range cycloalkanes.

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          XPS study of as-prepared and reduced molybdenum oxides

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            Recent advances in hydrodeoxygenation of biomass-derived oxygenates over heterogeneous catalysts

            Hydrodeoxygenation (HDO) using heterogeneous catalysts has received considerable attention as a way of converting biomass-derived oxygenates into renewable fuels and chemicals. Hydrodeoxygenation (HDO) using heterogeneous catalysts has received considerable attention as a way of converting biomass-derived oxygenates into renewable fuels and chemicals. HDO involves a combination of different reactions such as hydrogenation, hydrogenolysis, decarbonylation, and dehydration. These reactions occur at different catalytic sites, typically with heterogeneous catalysts ( e.g. , metal, acid, and bifunctional sites), making HDO reactions complex. Therefore, the selection of active site type is critical when designing effective heterogeneous catalysts for HDO processes. Catalyst stability is a major issue in designing HDO catalysts. Traditional catalysts are not stable under HDO conditions ( i.e. , high partial pressure of water). Metal particles are leached and/or sintered. A solid acid support suffers from phase transformation and losses in surface area. The condensation or polymerization of the CC or CO bond within biomass and its derived oxygenates is easy to undertake under high temperatures in the HDO process, causing carbon deposition on the catalyst. Poor catalyst stability is a major challenge that needs to be overcome for innovation in HDO technologies. Therefore, herein, we focus on providing an insight into how to design effective catalysts for use in HDO reactions. First, the roles of different catalytic sites in HDO and strategies to stabilize these active sites are discussed. Current achievements in the HDO of different biomass feedstocks ( e.g. , model compounds and bio-oils) over various heterogeneous catalysts are highlighted. Recent developments in electrochemical HDO processes, which do not require gaseous hydrogen, are discussed. Finally, points to be considered for further research into HDO over heterogeneous catalysts and pending challenges are discussed.
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              Bifunctional transalkylation and hydrodeoxygenation of anisole over a Pt/HBeta catalyst

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                Author and article information

                Journal
                ACS Omega
                ACS Omega
                ao
                acsodf
                ACS Omega
                American Chemical Society
                2470-1343
                21 January 2021
                02 February 2021
                : 6
                : 4
                : 2999-3016
                Affiliations
                []Department of Chemical Engineering, Faculty of Engineering, Mahidol University , 25/25 Putthamonthon 4 Road, Salaya, Phutthamonthon, Nakhon Pathom 73170, Thailand
                []State Key Laboratory of Microbial Metabolism, Joint International Research Laboratory of Metabolic & Developmental Sciences, School of Life Sciences and Biotechnology, Shanghai Jiao Tong University , 800 Dongchuan Road, Shanghai 200240, China
                [§ ]The Joint Graduate School of Energy and Environment, King Mongkut’s University of Technology Thonburi , 126 Pracha Uthit Road, Bang Mot, Thung Khru, Bangkok 10140, Thailand
                Author notes
                [* ]Email: chularat.sak@ 123456mahidol.ac.th . Tel: +66-28892138 ext 6101-2. Fax: +662-4419731.
                Article
                10.1021/acsomega.0c05387
                7860089
                33553918
                9664a9ed-9001-4253-b82d-f5725d5916e4
                © 2021 The Authors. Published by American Chemical Society

                This is an open access article published under a Creative Commons Non-Commercial No Derivative Works (CC-BY-NC-ND) Attribution License, which permits copying and redistribution of the article, and creation of adaptations, all for non-commercial purposes.

                History
                : 04 November 2020
                : 08 January 2021
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                ao0c05387

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