2022
DOI: 10.1016/j.biortech.2022.127050
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Low-temperature hydrothermal liquefaction of pomelo peel for production of 5-hydroxymethylfurfural-rich bio-oil using ionic liquid loaded ZSM-5

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Cited by 16 publications
(5 citation statements)
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“…These H + subsequently catalyze cellulose hydrolysis homogeneously to produce cellobiose (6.83 × 10.76 × 10.66 Å 3 ) and glucose. 53 Because of the large diameter of cellulose macromolecules, the cellulose hydrolysis process occurs in the reaction solvent rather than inside the channels of the nanoreactors. However, glucose molecules can enter these channels through shape selectivity of the NiO/PVP-HPA@ SBA-15 nanoreactor and undergo interactions with the NiO nanoparticles inside the channels.…”
Section: ■ Results and Discussionmentioning
confidence: 99%
See 1 more Smart Citation
“…These H + subsequently catalyze cellulose hydrolysis homogeneously to produce cellobiose (6.83 × 10.76 × 10.66 Å 3 ) and glucose. 53 Because of the large diameter of cellulose macromolecules, the cellulose hydrolysis process occurs in the reaction solvent rather than inside the channels of the nanoreactors. However, glucose molecules can enter these channels through shape selectivity of the NiO/PVP-HPA@ SBA-15 nanoreactor and undergo interactions with the NiO nanoparticles inside the channels.…”
Section: ■ Results and Discussionmentioning
confidence: 99%
“…The [BMIM] + cations then ion-exchanged with the Brønsted acid sites HPA of the NiO/PVP-HPA@SBA-15 nanoreactor to release H + into the reaction system. These H + subsequently catalyze cellulose hydrolysis homogeneously to produce cellobiose (6.83 × 10.76 × 10.66 Å 3 ) and glucose . Because of the large diameter of cellulose macromolecules, the cellulose hydrolysis process occurs in the reaction solvent rather than inside the channels of the nanoreactors.…”
Section: Resultsmentioning
confidence: 99%
“…[ 38 , 39 ] The addition of a surfactant to the acid‐catalyzed HTC system probably react with the degraded components in the surfactant domain to form a hydrotchar with improved carbonization strength and surface properties. [ 40 ] In fact, addition of Span 80 as a surfactant to citric acid‐catalyzed HTC significantly increased the mass yield of hydrothermal carbide from 39.04% to 63.45% and HHV from 24.122 to 31.302 MJ kg −1 , respectively. [ 41 ]…”
Section: Hydrothermal Carbonization Processmentioning
confidence: 99%
“…In this case, removing the coexisting impurities and increasing the silica content will yield higher‐quality materials thus research is being conducted on the removal of impurities by acid leaching using hydrochloric acid, sulfuric acid, and carboxylic acids, including citric acid, acetic acid, oxalic acid, and gluconic acid. [ 40 , 41 , 42 , 43 , 44 , 45 ]…”
Section: Separation Technology For Carbon and Silica Componentsmentioning
confidence: 99%
“…PP is rich in monosaccharides (glucose), disaccharides (fructose, sucrose), polysaccharides (cellulose, hemicellulose, pectin), and lignin, which are suitable for biofuel production. Various kinds of thermochemistry and biochemistry, as well as their combined processes, are used to recover bioenergy from PP [16,17]. Among many treatment technologies of PP, HTC is considered to be an environmentally friendly thermochemical conversion technology, which mainly converts PP into hydrochar under autogenous pressure (2-10 MPa) at 150-250 • C in a closed reactor (autoclave).…”
Section: Introductionmentioning
confidence: 99%