Continuous Valorization of Glycerol into Solketal

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Continuous Valorization of Glycerol into Solketal ( continuous-valorization-glycerol-into-solketal )

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Sustain. Chem. 2021, 2 323 97. Vivian, A.; Soumoy, L.; Fusaro, L.; Fiorilli, S.; Debecker, D.P.; Aprile, C. Surface-functionalized mesoporous gallosilicate catalysts for the efficient and sustainable upgrading of glycerol to solketal. Green Chem. 2021, 23, 354–366. [CrossRef] 98. Esposito, R.; Raucci, U.; Cucciolito, M.E.; Di Guida, R.; Scamardella, C.; Rega, N.; Ruffo, F. Iron(III) complexes for highly efficient and sustainable ketalization of glycerol: A combined experimental and theoretical study. ACS Omega 2019, 4, 688–698. [CrossRef] 99. Lee, D.-W.; Park, Y.-M.; Lee, K.-Y. Heterogeneous base catalysts for transesterification in biodiesel synthesis. Catal. Surv. Asia 2009, 13, 63–77. [CrossRef] 100. Gomes,I.S.;deCarvalho,D.C.;Oliveira,A.C.;Rodríguez-Castellón,E.;Tehuacanero-Cuapa,S.;Freire,P.T.C.;Filho,J.M.;Saraiva, G.D.; de Sousa, F.F.; Lang, R. On the reasons for deactivation of titanate nanotubes with metals catalysts in the acetalization of glycerol with acetone. Chem. Eng. J. 2018, 334, 1927–1942. [CrossRef] 101. Pinheiro,A.L.G.;doCarmo,J.V.C.;Carvalho,D.C.;Oliveira,A.C.;Rodríguez-Castellón,E.;Tehuacanero-Cuapa,S.;Otubo,L.; Lang, R. Bio-additive fuels from glycerol acetalization over metals-containing vanadium oxide nanotubes (MeVOx-NT in which, Me = Ni, Co, or Pt). Fuel Process. Technol. 2019, 184, 45–56. [CrossRef] 102. Dmitriev,G.S.;Terekhov,A.V.;Zanaveskin,L.N.;Maksimov,A.L.;Khadzhiev,S.N.Kineticsoftheformationofsolketalinthe presence of sulfuric acid. Kinet. Catal. 2018, 59, 504–508. [CrossRef] 103. Taddeo,F.;Esposito,R.;Russo,V.;DiSerio,M.Kineticmodelingofsolketalsynthesisfromglycerolandacetonecatalyzedbyan iron(III) complex. Catalysts 2021, 11, 83. [CrossRef] 104. Li,X.;Lai,J.;Cong,H.;Shu,C.;Zhao,R.;Wang,Y.;Li,H.;Gao,X.Towardsustainableandeco-efficientnovelcatalyticdistillation process for production of solketal using seepage catalytic packing internal. Catal. Today 2020. [CrossRef] 105. Dmitriev,G.S.;Terekhov,A.V.;Khadzhiev,S.N.;Zanaveskin,L.N.SpecificfeaturesofsolketalsynthesisonKU-2-8cation-exchange resin. Russ. J. Appl. Chem. 2016, 89, 45–50. [CrossRef] 106. Oliveira,P.A.;Souza,R.O.M.A.;Mota,C.J.A.Atmosphericpressurecontinuousproductionofsolketalfromtheacid-catalyzed reaction of glycerol with acetone. J. Braz. Chem. Soc. 2016, 27, 1832–1837. [CrossRef] 107. Guidi,S.;Noè,M.;Riello,P.;Perosa,A.;Selva,M.Towardsarationaldesignofacontinuous-flowmethodfortheacetalizationof crude glycerol: Scope and limitations of commercial amberlyst 36 and AlF3·3H2O as model catalysts. Molecules 2016, 21, 657. [CrossRef] 108. Konwar,L.J.;Samikannu,A.;Mäki-Arvela,P.;Boström,D.;Mikkola,J.-P.Lignosulfonate-basedmacro/mesoporoussolidprotonic acids for acetalization of glycerol to bio-additives. Appl. Catal. B 2018, 220, 314–323. [CrossRef] 109. Domínguez-Barroso,V.;Herrera,C.;Larrubia,M.Á.;González-Gil,R.;Cortés-Reyes,M.;Alemany,L.J.Continuous-flowprocess for glycerol conversion to solketal using a brönsted acid functionalized carbon-based catalyst. Catalysts 2019, 9, 609. [CrossRef] 110. Kowalska-Kus ́,J.;Held,A.;Nowin ́ska,K.Solketalformationinacontinuousflowprocessoverhierarchicalzeolites.ChemCatChem 2020, 12, 510–519. [CrossRef] 111. Kowalska-Kus ́,J.;Held,A.;Nowin ́ska,K.Acontinuous-flowprocessfortheacetalizationofcrudeglycerolwithacetoneon zeolite catalysts. Chem. Eng. J. 2020, 401, 126143. [CrossRef] 112. Huang,X.;Zhang,G.;Zhang,L.;Zhang,Q.ContinuousflowsynthesisofaZSM-5filmincapillarymicrochannelforefficient production of solketal. ACS Omega 2020, 5, 20784–20791. [CrossRef] 113. Zhang,G.;Zhang,L.;Wang,X.;Chen,A.;Zhang,Q.MicrofluidicprocessingofHZSM-5filmsinacapillarymicroreactorforthe continuous acetalisation reaction of glycerol with acetone. React. Chem. Eng. 2020, 5, 539–546. [CrossRef] 114. Stankiewicz,A.;Moulijn,J.A.Processintensification:Transformingchemicalengineering.Chem.Eng.Prog.2000,96,22–33. 115. Stankiewicz, A.; Moulijn, J.A. Chapter 2—Process intensification—An overview. In Process Intensification, 2nd ed.; Reay, D., Ramshaw, C., Harvey, A., Eds.; Butterworth-Heinemann: Oxford, UK, 2008; pp. 21–45. ISBN 978-0-7506-8941-0. 116. Priya,S.S.;Selvakannan,P.R.;Chary,K.V.R.;Kantam,M.L.;Bhargava,S.K.Solvent-freemicrowave-assistedsynthesisofsolketal from glycerol using transition metal ions promoted mordenite solid acid catalysts. Mol. Catal. 2017, 434, 184–193. [CrossRef] 117. Eze,V.C.;Harvey,A.P.Continuousreactivecouplingofglycerolandacetone—Astrategyfortriglyceridetransesterificationand in-situ valorisation of glycerol by-product. Chem. Eng. J. 2018, 347, 41–51. [CrossRef] 118. Al-Saadi,L.S.;Eze,V.C.;Harvey,A.P.Areactivecouplingprocessforco-productionofsolketalandbiodiesel.GreenProcess.Synth. 2019, 8, 516–524. [CrossRef] 119. Qing, W.; Chen, J.; Shi, X.; Wu, J.; Hu, J.; Zhang, W. Conversion enhancement for acetalization using a catalytically active membrane in a pervaporation membrane reactor. Chem. Eng. J. 2017, 313, 1396–1405. [CrossRef] 120. Zaharia,E.;Bildea,C.;Muntean,O.Design,economicevaluationandplantwidecontrolofglycerolketalizationplant.UPBSci. Bull. Ser. B Chem. Mater. Sci. 2015, 77, 41–52. 121. Dmitriev,G.S.;Terekhov,A.V.;Zanaveskin,L.N.;Khadzhiev,S.N.;Zanaveskin,K.L.;Maksimov,A.L.Choiceofacatalystand technological scheme for synthesis of solketal. Russ. J. Appl. Chem. 2017, 89, 1619–1624. [CrossRef] 122. DaSilva,M.J.;deÁvilaRodrigues,F.;Júlio,A.A.SnF2-catalyzedglycerolketalization:Afriendlyenvironmentallyprocessto synthesize solketal at room temperature over on solid and reusable Lewis acid. Chem. Eng. J. 2017, 307, 828–835. [CrossRef] 123. Al-Saadi, L.S.; Eze, V.C.; Harvey, A.P. Techno-economic analysis of processes for biodiesel production with integrated co- production of higher added value products from glycerol. Biofuels 2020, 1–8. [CrossRef] 124. Chol, C.G.; Dhabhai, R.; Dalai, A.K.; Reaney, M. Purification of crude glycerol derived from biodiesel production process: Experimental studies and techno-economic analyses. Fuel Process. Technol. 2018, 178, 78–87. [CrossRef] 125. Clarke,N.S.Thebasicsofpatentsearching.WorldPat.Inf.2018,54,S4–S10.[CrossRef]

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