2019
DOI: 10.1016/j.biortech.2018.10.018
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Development of an advanced integrative process to create valuable biosugars including manno-oligosaccharides and mannose from spent coffee grounds

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Cited by 60 publications
(33 citation statements)
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“…A recent study has shown that 15 g of mannose could be obtained for every 100 g of spent coffee ground (SCG) after the removal of the non-saccharide content after delignification and defatting of SCG 43 . In the present study, 57.5 g of mannose could be obtained for every 100 g of in natura açaí seed, with a total mannose recovery of 98.6%.…”
Section: Resultsmentioning
confidence: 99%
“…A recent study has shown that 15 g of mannose could be obtained for every 100 g of spent coffee ground (SCG) after the removal of the non-saccharide content after delignification and defatting of SCG 43 . In the present study, 57.5 g of mannose could be obtained for every 100 g of in natura açaí seed, with a total mannose recovery of 98.6%.…”
Section: Resultsmentioning
confidence: 99%
“…By down-regulating pectin biosynthesis via GAUT4, Biswal et al reported a reduction in the synthesis of homogalacturonan (HG) and rhamnogalacturonan II (RGII), which led to a decrease in recalcitrance in plant cell wall biomass, consequently increasing saccharification [25]. Figure 6 distinguishes between biomass from the wild-type and transgenic tobacco plants, with several apparent differences in their FT-IR spectra, including the disappearance of or significant reduction in peaks representing lignin and other non-saccharide compounds [2]. Adsorption peaks around 3,241.3-3,391.6 cm −1 were clearly observed in the wild-type tobacco plants, but they were reduced in the ChB-1 tobacco plants, indicating a lower abundance of free and intermolecular bonded O-H groups in the ChB-1 plants than in the wild-type plants.…”
Section: Enhanced Saccharification In the Enzymatic Conversion Of Biomentioning
confidence: 99%
“…Lignocellulosic biomass, particularly originating from crops, is abundant and available globally. It acts as an excellent source material for the production of biofuels and value-added products [1,2]. In order to develop biorefineries for processing lignocellulosic biomass, several challenges should be overcome, especially reducing enzyme costs and improving lignocellulosic materials to ensure that they can be hydrolyzed more easily.…”
Section: Introductionmentioning
confidence: 99%
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“…When this residue was pretreated by delignification and defatting and submitted afterwards to an enzymatic hydrolysis with a 10% w/w dry substrate loading at 45 • C and pH 4.8, a maximum oligosaccharides production yield is obtained between 4 h and 6 h after hydrolysis started. The highest yields were observed using a non-commercial pectinase, at 4.1 mg enzyme/g dry biomass, obtaining 38.2 g/L of DP62 MOS and 24.9 g/L of DP6 MOS (total yield 0.63 g/g DS) [117]. Rungruangsaphakun et al, on the other side, produced MOS using 16.52 U/mL of mannanase, with a solid loading of 15% of defatted copra meal, 50 • C and pH 6.…”
Section: Hemicellulosementioning
confidence: 95%