2015
DOI: 10.1016/j.biortech.2015.06.115
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Characterization of products from hydrothermal carbonization of orange pomace including anaerobic digestibility of process liquor

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Cited by 204 publications
(101 citation statements)
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“…Methane production began immediately in assays 1–2, 1–1 and 2.5–2, reaching final figures of 144±1, 158±4 and 177±5 mL CH 4 STP g ‐1 COD added , respectively. These yield values are lower than the observed for the anaerobic digestion of the liquid fraction from HTC of agricultural residues like thin stillage or orange pomace, where 300 and 213 mL CH 4 STP g ‐1 COD, were reported, respectively, or mixed sewage sludge, with 257 mL CH 4 g ‐1 COD, but fairly similar to that obtained by Weiner et al for the liquid fraction from HTC of chaff using organosolv as the liquid source for carbonisation (174±9 mL CH 4 g ‐1 COD) or by Wirth et al for the liquid fraction from HTC of digested sewage sludge as sole substrate operating in continuous feed mode (120–180 mL CH 4 STP g ‐1 COD added ). For all the other conditions tested, inhibition of the methanogenic stage occurred, suggesting that not only the ISR but also the IC affect methane production.…”
Section: Resultssupporting
confidence: 82%
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“…Methane production began immediately in assays 1–2, 1–1 and 2.5–2, reaching final figures of 144±1, 158±4 and 177±5 mL CH 4 STP g ‐1 COD added , respectively. These yield values are lower than the observed for the anaerobic digestion of the liquid fraction from HTC of agricultural residues like thin stillage or orange pomace, where 300 and 213 mL CH 4 STP g ‐1 COD, were reported, respectively, or mixed sewage sludge, with 257 mL CH 4 g ‐1 COD, but fairly similar to that obtained by Weiner et al for the liquid fraction from HTC of chaff using organosolv as the liquid source for carbonisation (174±9 mL CH 4 g ‐1 COD) or by Wirth et al for the liquid fraction from HTC of digested sewage sludge as sole substrate operating in continuous feed mode (120–180 mL CH 4 STP g ‐1 COD added ). For all the other conditions tested, inhibition of the methanogenic stage occurred, suggesting that not only the ISR but also the IC affect methane production.…”
Section: Resultssupporting
confidence: 82%
“…Besides, the HTC conditions (temperature and time) affect the CODt. Values around 60 g L ‐1 have been reported from HTC of food waste or orange pomace and somewhat lower values (40–50 g L ‐1 ) have been obtained from agro‐industrial residues like chaff, corn silage or thin stillage, while for HTC of primary sewage, mixture of primary and secondary sludge and digested municipal sewage sludge, values of 23, 52.5 and 34 g L ‐1 , respectively, have been reported . Therefore, the liquid fraction from HTC, needs to be conveniently managed before final discharge and moreover its high organic load offers potential interest for the sake of valorisation.…”
Section: Introductionmentioning
confidence: 99%
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“…The diagram provided further evidence about the transformation (dehydration, decarboxylation, and demethanation reactions) that took place in the chemical structure of glucose during the microwave-assisted hydrothermal carbonization process. The transformation from the starting material (glucose) to the hydrochar samples follows a diagonal line due to decrease in the O/C and H/C ratios, suggesting dehydration reactions as prevalent reaction during the process, which is consistent with previous reports [9,28].…”
Section: Elemental Composition Of the Prepared Hydrocharssupporting
confidence: 91%
“…Hydrothermal carbonization (HTC) is a simple biomass carbonization process, which offers many advantages such as generation of carbon at lower temperatures (<250 °C) than that required for other carbonization protocols such as ignition, pyrolysis, and gasification . During HTC, biomass is processed in hot pressurized water, excluding the energy intensive pre‐drying step .…”
Section: Introductionmentioning
confidence: 99%