2008
DOI: 10.1002/cssc.200700167
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Current and Foreseeable Applications of Supercritical Water for Energy and the Environment

Abstract: It is crucial to develop economical and energy-efficient processes for the sustainable transformation of biomass into fuels and chemicals. In this context, supercritical water biomass valorization (SCBV) processes are an alternative way to produce biogas, biofuels, and valuable chemicals. Supercritical water technology has seen much progress over the last fifteen years and an industrial application has merged: the supercritical water oxidation of wastes. The evolution from lab-scale to pilot-scale facilities h… Show more

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Cited by 186 publications
(68 citation statements)
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“…% hydrogen cases was almost 4 times that recorded for the BioSNG cases. Similarly in block A2, the net reactor demand (hydrolysis + gasification) and the internal stepwise heating demand (salt separator heat jacket + SCWG reformer preheater) are significantly higher in the hydrogen cases compared to the BioSNG base case, all of which have a similar SCWG operating temperature of 600 • C. However, it is worth noting that the lower net reactor demand is also partially attributed to the endothermic nature of hydrogen formation pathways at 600 • C compared to the exothermic nature experienced with CH4 formation [7,9]. If the two BioSNG cases are compared, the influence of the SCWG reactor temperature at 450 • C for the 2nd case plays an additional role in the lower demand.…”
Section: Conceptual Plant Simulation-energy Balancementioning
confidence: 74%
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“…% hydrogen cases was almost 4 times that recorded for the BioSNG cases. Similarly in block A2, the net reactor demand (hydrolysis + gasification) and the internal stepwise heating demand (salt separator heat jacket + SCWG reformer preheater) are significantly higher in the hydrogen cases compared to the BioSNG base case, all of which have a similar SCWG operating temperature of 600 • C. However, it is worth noting that the lower net reactor demand is also partially attributed to the endothermic nature of hydrogen formation pathways at 600 • C compared to the exothermic nature experienced with CH4 formation [7,9]. If the two BioSNG cases are compared, the influence of the SCWG reactor temperature at 450 • C for the 2nd case plays an additional role in the lower demand.…”
Section: Conceptual Plant Simulation-energy Balancementioning
confidence: 74%
“…It is worth noting that the organic structure, solid-to-water ratio, residence time, pressure, catalysis and process units' mechanical configurations also influence the specific yields of each product as has been reported [4][5][6]9,11,[13][14][15][16]. However, such information available in literature is diverse and fragmented, and temperature levels remain the governing processing parameter that identify the product phase distribution.…”
Section: Introductionmentioning
confidence: 96%
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“…Due to the complex chemical composition of lignocellulosic biomass, its hydrothermal conversion produces a complex mixture of products. The high polydispersity of these products in terms of oxygenated chemical functions and molecular weights makes their characterization awkward [7][8][9][10][11][12][13][14]. The approach that can be carried out to simplify the reaction pathway investigation consists in studying transformation of compounds representative of lignocellulosic constituents (i.e.…”
Section: Introductionmentioning
confidence: 99%