02423nas a2200229   4500008004100000022001400041245012500055210006900180260007700249300001200326490000600338520156500344653001301909653001401922653001901936653001901955653001301974100002901987700002302016700002202039856013202061       2014                        eng d  a2194-428800aGlycerol etherification using n-butanol to produce oxygenated additives for biodiesel fuel over H-beta zeolite catalysts0 aGlycerol etherification using nbutanol to produce oxygenated add  aBOSCHSTRASSE 12, D-69469 WEINHEIM, GERMANYbWILEY-V C H VERLAG GMBHcMAY  a446-4520 v23 a<p>The catalytic etherification of glycerol has been systematically studied in batch process by using n-butanol to produce oxygenated additives for biodiesel fuels over various solid-acid catalysts, such as H-beta zeolite, ZSM-5, K10, etc.. The present work includes a detailed study of the optimization of the etherification process parameters, such as catalyst loading (7-20 wt% of glycerol), molar ratio of glycerol/n-butanol (1: 6 to 1: 15), speed of agitation (100-400 rpm), reaction temperature (413-453 K), and reaction time (0.5-4 h) in view of maximizing the glycerol conversion and selectivity towards mono-butyl-glycerol ether (ME). The catalyst reusability was studied using the optimized process parameters. Amongst the studied catalysts, the H-beta zeolite was found to be the most promising for the etherification of glycerol with glycerol conversion of 55% and a 98% selectivity towards ME formation. The H-beta zeolite was found to be an active and stable catalyst for up to 4 cycles. The use of n-butanol as alkylating agent is presented for first time, to the authors knowledge. The reaction was performed at milder operating conditions (0.5 MPa) than previously reported (2 MPa). A kinetic model was developed for the etherification reaction and the data obtained at optimized process parameters was used to calculate the kinetic parameters. The reaction rate constants at different reaction temperatures, activation energies, and pre-exponential factors were obtained for the etherification reaction with an accuracy of R-2 &gt; 0.989.</p>10abiofuels10acatalysis10aetherification10afuel additives10azeolites1 aNandiwale, Kakasaheb, Y.1 aPatil, Shivraj, E.1 aBokade, Vijay, V.  uhttps://library.ncl.res.in/content/glycerol-etherification-using-n-butanol-produce-oxygenated-additives-biodiesel-fuel-over-h-001312nas a2200205   4500008004100000022001400041245016600055210006900221260000900290300001400299490000700313520054600320653001600866653001900882653001900901653001300920100002200933700002500955856012600980       2016                        eng d  a0040-403900aApplication of glucose derived magnetic solid acid for etherification of 5-HMF to 5-EMF, dehydration of sorbitol to isosorbide, and esterification of fatty acids0 aApplication of glucose derived magnetic solid acid for etherific  cSEP   a4398-44000 v573 a<p>In this study, the catalytic activity of Glu-Fe3O4-SO3H was evaluated for three acid catalyzed reactions: etherification of 5-hydroxymethylfurfural (5-HMF) to 5-ethoxymethylfurfural (5-EMF) in ethanol, dehydration of sorbitol to isosorbide, and esterification of fatty acids with good yields and selectivity. Moreover, the catalyst can be easily separated from the reaction with an external magnetic force and reused at least five times without a significant decrease in catalytic activity. (C) 2016 Elsevier Ltd. All rights reserved.</p>10adehydration10aEsterification10aetherification10aMagnetic1 aThombal, Raju, S.1 aJadhav, Vrushali, H.  uhttps://library.ncl.res.in/content/application-glucose-derived-magnetic-solid-acid-etherification-5-hmf-5-emf-dehydration01325nas a2200253   4500008004100000022001400041245015900055210006900214260000800283300001400291490000700305520042200312653000600734653001900740653002500759653002100784653001900805653003400824653001300858100002200871700002800893700002200921856012800943       2020                        eng d  a0922-616800aSynthesis of ethyl furfuryl ether (potential biofuel) by etherification of furfuryl alcohol with ethanol over heterogenized reusable H1Cs2PW12O40 catalyst0 aSynthesis of ethyl furfuryl ether potential biofuel by etherific  cAPR  a2309-23250 v463 a<p>{Ethyl furfuryl ether (EFE) considered as potential biofuel can replace petroleum diesel up to 100%. EFE also has efficient blending properties with biodiesel to improve its cold flow properties. Herein we demonstrate efficient synthesis of EFE by etherification of renewable furfuryl alcohol (FAlc) with ethanol over heterogenized heteropoly acids. Cs-exchanged heterogenized heteropoly acid (H3-xCsxPW12O40</p>
10aB10aetherification10aEthyl furfuryl ether10aFurfuryl alcohol10aH3-xCsxPW12O4010aHeterogenized heteropoly acid10aL ration1 aMulik, Nagesh, L.1 aNiphadkar, Prashant, S.1 aBokade, Vijay, V.  uhttps://library.ncl.res.in/content/synthesis-ethyl-furfuryl-ether-potential-biofuel-etherification-furfuryl-alcohol-ethanol01968nas a2200217   4500008004100000022001400041245013000055210006900185260000800254300001100262490000800273520120800281653001601489653001901505653001901524653002501543653001901568100001801587700001801605856012701623       2022                        eng d  a2468-823100aImmobilization of HPW on UiO-66-NH2 MOF as efficient catalyst for synthesis of furfuryl ether and alkyl levulinate as biofuel0 aImmobilization of HPW on UiO66NH2 MOF as efficient catalyst for   cOCT  a1126890 v5313 a<p>
	Phosphotungustic Acid (HPW) is an inorganic super acid, that is highly soluble in polar solvents limiting its applicability as acid catalysis. To overcome these limitations immobilization of HPW was carried out at room temperature by protonation of-NH2 group of UiO-66-NH2 MOF to UiO-66-NH2-HPW. ATR-FTIR spectroscopy and XPS results confirmed the protonation and chemical interaction between HPW and UiO-66-NH2. STEM-EDS mapping showed homogeneous distribution of HPW on UiO-66-NH2. BET and NH3-TPD confirmed the reduction in specific surface area, total pore volume, and increase in total acidity for UiO-66-NH2-HPW. Further, powder XRD, SEM, and HR-TEM prevailed that there is no change in phase and morphology after post-synthetic modification of UiO-66-NH2. The prepared catalyst is found to be effective for etherification and alcoholysis of furfuryl alcohol (FALc) to Furfuryl ether (FE) and Alkyl levulinate (AL). UiO-66-NH2-HPW has shown 97 mol % FALc conversions in ethanolic media and 31 mol% Ethyl furfuryl ether (EFE) yield and 29 mol% Ethyl lev-ulinate (EL) yield. UiO-66-NH2-HPW is also found to be efficient for the multistep conversion of Furfural (FFR) to FALc, FE, and AL.</p>
10aAlcoholysis10aetherification10aImmobilization10aPhosphotungstic acid10aUiO-66-NH2-HPW1 aMulik, Nagesh1 aBokade, Vijay  uhttps://library.ncl.res.in/content/immobilization-hpw-uio-66-nh2-mof-efficient-catalyst-synthesis-furfuryl-ether-and-alkyl02339nas a2200277   4500008004100000022001400041245017000055210006900225260000800294300001600302490000700318520139900325653001401724653001901738653001901757653001501776653001701791653001301808653001301821100002301834700001901857700002301876700002201899700002901921856011101950       2023                        eng d  a2190-681500aEtherification of biomass-derived glycerol to oxygenated fuel additives using dodecatungstophosphoric-silica-supported catalyst: characterization and kinetic studies0 aEtherification of biomassderived glycerol to oxygenated fuel add  cNOV  a16285-162950 v133 a<p>
	Commercial biodiesel production is becoming popular due to its sustainability and reduced greenhouse gas emissions in comparison to fossil fuels. Biodiesel production involves the co-generation of crude glycerol that is not directly viable. Valorization of glycerol is essential from techno-economic perspective to achieve goals of circular economy. In this study, the glycerol etherification was carried out using tert-butyl alcohol in presence of dodecatungstophosphoric/silica (DTP/SiO2) catalyst for production of tert-butyl glycerol ethers that can be used as fuel additives. A series of DTP/SiO2 catalysts were prepared with various compositions by impregnating heteropoly acids (HPA, H3PW12O40). The product analysis was performed to monitor mono-, di-, and tri-tert-butyl glycerol ethers. The kinetic studies were conducted based on Langmuir-Hinshelwood model. The rate constants were determined from experimental data by regression analysis. The catalysts were characterized by X-ray diffraction, SEM/EDX, and thermogravimetric analysis. Varying DTP loadings resulted in different catalytic activities. Activation energy (38.23 kJ/mol), activation enthalpy (25.94 kJ/mol), activation entropy (-163.8 J/mol/K), and Gibbs free energy of activation (88.67 kJ/mol) were attained for DTP/SiO2 (20%) catalyst that exhibited the best selectivity for di-tert-butyl glycerol ethers.</p>
10aCatalytic10aetherification10afuel additives10aHinselwood10aImpregnation10akinetics10aLangmuir1 aMagar, Subhash, B.1 aKapoor, Ashish1 aJana, Sumit, Kumar1 aPal, Dan, Bahadur1 aRode, Chandrashekhar, V.  uhttps://library.ncl.res.in/content/etherification-biomass-derived-glycerol-oxygenated-fuel-additives-using