2018
DOI: 10.1021/acssuschemeng.8b04670
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Electrochemical Membrane Reactor Modeling for Lignin Depolymerization

Abstract: Valorization of lignin into value-added chemicals becomes an interesting research topic for sustainable and renewable product formation. A conceptual study of lignin valorization through an electrochemical membrane reactor process is presented. The membrane reactor model is able to predict a larger aromatic product formation yield because the product is permeating out before it degrades. Different process parameters were examined, in an electrochemical membrane reactor process, via sensitivity analysis. Throug… Show more

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Cited by 15 publications
(12 citation statements)
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“…Park et al and Pintauro et al reported on the electrochemical oxidation and reduction of glucose to gluconic acid and sorbitol. , Governo et al elaborated on the electrochemical oxidation of xylose to xylonic acid in an alkaline medium . Electrochemical degradation of lignin to high value-added products has been exploited since the 20th century and remains popular, because of its high yield of aromatic compounds and carbohydrates, which can serve as feedstock for various platform chemicals. ,,, …”
Section: Introductionmentioning
confidence: 99%
“…Park et al and Pintauro et al reported on the electrochemical oxidation and reduction of glucose to gluconic acid and sorbitol. , Governo et al elaborated on the electrochemical oxidation of xylose to xylonic acid in an alkaline medium . Electrochemical degradation of lignin to high value-added products has been exploited since the 20th century and remains popular, because of its high yield of aromatic compounds and carbohydrates, which can serve as feedstock for various platform chemicals. ,,, …”
Section: Introductionmentioning
confidence: 99%
“…Later, they developed a conceptual model for lignin degradation in an ECMR and found that a membrane pore diameter of 1 nm was optimal, yielding 11 % monomers, <2 % CO 2 , and water versus 70 % organic acids (from continuous degradation of aromatics), 30 % CO 2 , and water in a batch reactor. Monomer yield increased as a function of membrane area (optimal 0.01 m 2 ) and transmembrane pressure (optimal 1.4 bar); going beyond these optimal values would only increase capital cost without any significant effect on product yield …”
Section: Electrocatalytic Treatment Of Ligninmentioning
confidence: 96%
“…[113] Later,t hey developed ac onceptual model for lignin degradation in an ECMR andf ound that am embrane pore diameter of 1nmw as optimal, yielding 11 %m onomers, < 2% CO 2 ,a nd water versus 70 %o rganic acids (from continuous degradation of aromatics), 30 %C O 2 ,a nd water in ab atch reactor.M onomer yield increased as af unction of membrane area (optimal 0.01 m 2 )a nd transmembrane pressure (optimal 1.4 bar);g oing beyondt hese optimal valuesw ould only increase capital cost withouta ny significant effect on product yield. [114] Alternatively, Di Marinoe tal. specifically targeted electrochemicald epolymerization of lignin to carboxylic acids in addition to phenolic monomers in a" swiss roll" electrochemical reactor with Ni foam electrode.…”
Section: Nickel- Cobalt- and Nickel-cobalt-based Electrodesmentioning
confidence: 99%
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“…TGA test shows that Catalpa ovata G. Don. has certain thermal stability, and also has high resource utilization potential and relatively efficient utilization [35].…”
Section: Analysis Of Td-gc-msmentioning
confidence: 99%