2021
DOI: 10.1016/j.renene.2021.03.126
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Hydrothermal liquefaction (HTL) processing of unhydrolyzed solids (UHS) for hydrochar and its use for asymmetric supercapacitors with mixed (Mn,Ti)-Perovskite oxides

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Cited by 23 publications
(14 citation statements)
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“…Recently, we reported a novel (Mn:Ti)‐mixed oxide (52.7 wt% TiMnO 3 ‐perovskite and 47.3 wt% TiO 2 ‐rutile phases) cathode electrode for ASCs 24‐29 . As‐fabricated ASCs using this (Mn,Ti)‐mixed oxide material and graphene nanoplatelets showed a maximum specific capacitance of 345 F/g 26 . The unique perovskite phase in (Mn:Ti)‐mixed oxide maybe beneficial for superior energy storage mechanism due to possible bulk intercalation mechanism.…”
Section: Introductionmentioning
confidence: 99%
“…Recently, we reported a novel (Mn:Ti)‐mixed oxide (52.7 wt% TiMnO 3 ‐perovskite and 47.3 wt% TiO 2 ‐rutile phases) cathode electrode for ASCs 24‐29 . As‐fabricated ASCs using this (Mn,Ti)‐mixed oxide material and graphene nanoplatelets showed a maximum specific capacitance of 345 F/g 26 . The unique perovskite phase in (Mn:Ti)‐mixed oxide maybe beneficial for superior energy storage mechanism due to possible bulk intercalation mechanism.…”
Section: Introductionmentioning
confidence: 99%
“…Figure shows the FT-IR analysis of samples. The absorption bands at 1725 cm –1 (CO), 1633 cm –1 (CC), 1551 cm –1 (−COO−), and 1069 cm –1 (C–O) , were typical absorption peaks for acidified CNTs. Multiple sharp absorption peaks were observed at 3224 cm –1 , assigned to the N–H characteristic peak, 2919 cm –1 was the C–H stretching, 1578 and 1493 cm –1 were the polyaniline aromatic ring, 1374, 1302, and 1244 cm –1 were peaks assigned to aromatic amine groups, and 1131 and 799 cm –1 were the in-plane and out-of-plane bending vibration peaks of polyaniline ring, respectively. , These characteristic peaks indicated the successful formation of polyaniline.…”
Section: Resultsmentioning
confidence: 99%
“…An HTL process was used to convert the low-ash content corn stover to value-added products such as biochar, bio-oil, lactic acid, and phenol in a PARR reactor. Details of the HTL conversion process were given elsewhere. ,, The HTL reaction was carried out at a temperature of 275 °C, an initial N 2 pressure of 100 psig., 2 h reaction time, and 1:10 biomass to solvent (water) ratio in the presence of Ni-based catalytic salts at 5 wt % concentration. Throughout the conversion process, anaerobicity in the reaction chamber is maintained by continually purging the contents in the reactor with industrial-grade N 2 for 20 min, and the stirring rate of the PARR reactor was fixed to 1300 rpm.…”
Section: Materials and Methodsmentioning
confidence: 99%