Abstract:Polysaccharide depolymerization is an essential step for valorizing lignocellulosic biomass. In inexpensive systems such as pure water or dilute acid mixtures, carbohydrate monomer degradation rates exceed hemicellulose-and especially cellulose-depolymerization rates at most easily accessible temperatures, limiting sugar yields. Here, we use a reversible stabilization of xylose and glucose by acetal formation with formaldehyde to alter this kinetic paradigm, preventing sugar dehydration to furans and their sub… Show more
“…Alternatively, the ring opening of HMXF could have also lead to the formation of xylulose. 8 In any of these cases, the selectivity of the process decreases, which is what we observed.…”
We demonstrate a catalytic process for xylitol production based on the volatility and unique reactivity of diformylxylose (DFX), which can be produced at near theoretical yield from biomass and, contrary to xylose, can be easily purified by distillation. The apparent rate-limiting step was independent of hydrogen pressure, and catalytic studies showed a slow evolution of the Pt/C catalyst that led to tripling of the xylitol yield. In-depth catalyst characterization attributed this activity increase to the formation of acidic carbon deposits, which created acid sites in close proximity to Pt. These proximal sites accelerated DFX hydrolysis while avoiding unfavorable isomerization reactions.
“…Alternatively, the ring opening of HMXF could have also lead to the formation of xylulose. 8 In any of these cases, the selectivity of the process decreases, which is what we observed.…”
We demonstrate a catalytic process for xylitol production based on the volatility and unique reactivity of diformylxylose (DFX), which can be produced at near theoretical yield from biomass and, contrary to xylose, can be easily purified by distillation. The apparent rate-limiting step was independent of hydrogen pressure, and catalytic studies showed a slow evolution of the Pt/C catalyst that led to tripling of the xylitol yield. In-depth catalyst characterization attributed this activity increase to the formation of acidic carbon deposits, which created acid sites in close proximity to Pt. These proximal sites accelerated DFX hydrolysis while avoiding unfavorable isomerization reactions.
“…1 Transformation of lignin and/or CO 2 into value-added chemicals has attracted great interest. [2][3][4][5][6][7][8][9][10][11][12][13][14][15] Lignin is a major component of lignocellulosic biomass, and its valorization remains a challenge because of the complex and robust structure. 16 Aryl methyl ethers are commonly used as model compounds to study lignin conversion, which has been successfully transformed into various chemicals, such as benzene, phenol, terephthalic acid, cyclohexanone, cyclohexane, methanol, methane, acetates, acetic acid, etc.…”
“…For instance 1,2:3,5-di-O-isopropylidene-α-D-xylofuranose (DX) and 1,2: 5,6- Isopropylidene- α-D -glucofuranose (DG) were produced in high concentration, 50 wt.%. A later publication also applied similar condition to depolymerization wood biomass and avoided undesirable reaction of sugars (Questell-Santiago et al, 2018).…”
Fluidized catalytic cracking (FCC) converts hydrocarbons in the presence of a catalyst based on faujasite zeolite (USY and REY). While hydrocarbon is poorly reactive, biomass and its derived compounds are highly functionalized and not suitable to a typical FCC process. To overcome this limitation biomass was first converted into a dense and stable bio-crude composed mainly of ketal-sugar derivatives by using acetone in diluted acid. Here, a representative compound of this bio-crude, 1,2:3,5-di-O-isopropylidene-α-D-xylofuranose (DX) in n-hexane, was converted by USY and a commercial FCC catalyst containing USY, at 500°C, in a fixed bed and fluidized bed reactors, respectively. Faujasite Y is very efficient in converting DX. More than 95% conversion was observed in all tests. Over 60 wt.% was liquid products, followed by gas products and only around 10% or less in coke. The higher the catalyst activity the greater the aromatics in the liquid products and yet higher coke yields were observed. In particular, simulating more practical application conditions: using deactivated catalyst in a fluidized bed reactor, improved green hydrocarbons production (mono-aromatic up to 10 carbons and light hydrocarbon up to eight carbons) and unprecedented lower coke yield (≈5 wt.%) for bio-feeds. The present results further suggest that catalyst will play a primary role to convert the bio-crude into target hydrocarbons and overcome the transition of a non-renewable to a renewable refinery feed.
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