Synthesis of Nanophased Metal Oxides in Supercritical Water: Catalysts for Biomass Conversion

2014 ◽  
pp. 217-224
Author(s):  
Caroline Levy ◽  
Masaru Watanabe ◽  
Yuichi Aizawa ◽  
Hiroshi Inomata ◽  
Kiwamu Sue
2006 ◽  
Vol 3 (5) ◽  
pp. 337-344 ◽  
Author(s):  
Caroline Levy ◽  
Masaru Watanabe ◽  
Yuichi Aizawa ◽  
Hiroshi Inomata ◽  
Kiwamu Sue

MRS Bulletin ◽  
2008 ◽  
Vol 33 (4) ◽  
pp. 429-435 ◽  
Author(s):  
Bruce C. Gates ◽  
George W. Huber ◽  
Christopher L. Marshall ◽  
Phillip N. Ross ◽  
Jeffrey Siirola ◽  
...  

AbstractCatalysis is the essential technology for chemical transformation, including production of fuels from the fossil resources petroleum, natural gas, and coal. Typical catalysts for these conversions are robust porous solids incorporating metals, metal oxides, and/or metal sulfides. As efforts are stepping up to replace fossil fuels with biomass, new catalysts for the conversion of the components of biomass will be needed. Although the catalysts for biomass conversion might be substantially different from those used in the conversion of fossil feedstocks, the latter catalysts are a starting point in today's research. Major challenges lie ahead in the discovery of efficient biomass conversion catalysts, as well as in the discovery of catalysts for conversion of CO2 and possibly water into liquid fuels.


2004 ◽  
Vol 98 (1-2) ◽  
pp. 105-113 ◽  
Author(s):  
Wei Feng ◽  
Hedzer J van der Kooi ◽  
Jakob de Swaan Arons

1997 ◽  
Vol 124 (1) ◽  
pp. 129-145 ◽  
Author(s):  
Marcel G.E. Goemans ◽  
Frank M. Tiller ◽  
Lixiong Li ◽  
Earnest F. Gloyna

Energies ◽  
2020 ◽  
Vol 13 (17) ◽  
pp. 4553 ◽  
Author(s):  
Ane Caroline Pereira Borges ◽  
Jude Azubuike Onwudili ◽  
Heloysa Andrade ◽  
Carine Alves ◽  
Andrew Ingram ◽  
...  

Nickel iron oxide (NiFe2O4) catalyst was prepared by the combustion reaction method and characterized by XRD, N2 adsorption/desorption, thermogravimetric analysis (TG), and temperature programmed reduction (TPR). The catalyst presented a mixture of oxides, including the NiFe2O4 spinel and specific surface area of 32.4 m2 g−1. The effect of NiFe2O4 catalyst on the supercritical water gasification (SCWG) of eucalyptus wood chips was studied in a batch reactor at 450 and 500 °C without catalyst and with 1.0 g and 2.0 g of catalyst and 2.0 g of biomass for 60 min. In addition, the recyclability of the catalyst under the operating conditions was also tested using recovered and recalcined catalysts over three reaction cycles. The highest amount of H2 was 25 mol% obtained at 450 °C, using 2 g of NiFe2O4 catalyst. The H2 mol% was enhanced by 45% when compared to the non-catalytic test, showing the catalytic activity of NiFe2O4 catalyst in the WGS and the steam reforming reactions. After the third reaction cycle, the results of XRD demonstrated formation of coke which caused the deactivation of the NiFe2O4 and consequently, a 13.6% reduction in H2 mol% and a 5.6% reduction in biomass conversion.


Author(s):  
Niloufar Ghavami ◽  
Karhan Özdenkçi ◽  
Gabriel Salierno ◽  
Margareta Björklund-Sänkiaho ◽  
Cataldo De Blasio

AbstractBiomass is often referred to as a carbon–neutral energy source, and it has a role in reducing fossil fuel depletion. In addition, biomass can be converted efficiently into various forms of biofuels. The biomass conversion processes involve several thermochemical, biochemical, and hydrothermal methods for biomass treatment integration. The most common conversion routes to produce biofuels include pyrolysis and gasification processes. On the other hand, supercritical water gasification (SCWG) and hydrothermal liquefaction (HTL) are best suitable for converting biomass and waste with high moisture content. Despite promising efficiencies, SCWG and HTL processes introduce operational issues as obstacles to the industrialization of these technologies. The issues include process safety aspects due to operation conditions, plugging due to solid deposition, corrosion, pumpability of feedstock, catalyst sintering and deactivation, and high production costs. The methods to address these issues include various reactor configurations to avoid plugging and optimizing process conditions to minimize other issues. However, there are only a few studies investigating the operational issues as the main scope, and reviews are seldomly available in this regard. Therefore, further research is required to address operational problems. This study reviews the main operational problems in SCWG and HTL. The objective of this study is to enhance the industrialization of these processes by investigating the operational issues and the potential solutions, i.e., contributing to the elimination of the obstacles. A comprehensive study on the operational issues provides a holistic overview of the biomass conversion technologies and biorefinery concepts to promote the industrialization of SCWG and HTL.


2020 ◽  
Vol 157 ◽  
pp. 24-32 ◽  
Author(s):  
Changqing Cao ◽  
Yupeng Xie ◽  
Liuhao Mao ◽  
Wenwen Wei ◽  
Jinwen Shi ◽  
...  

2015 ◽  
Vol 17 (1) ◽  
pp. 610-618 ◽  
Author(s):  
Danilo A. Cantero ◽  
Celia Martínez ◽  
M. D. Bermejo ◽  
M. J. Cocero

A contribution to biomass conversion into sugars and lignin using a compact reactor that is easy to scale-up was made. Wheat bran was continuously fractionated under supercritical water conditions.


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