02769nas a2200301 4500008004100000022001400041245007700055210006900132260007300201300001200274490000800286520177700294653001802071653001302089653001302102653002402115653001502139100002802154700002402182700002402206700001902230700001902249700002302268700002402291700002402315700001802339856011002357 2009 eng d a1381-116900aAcetalization of glycerol using mesoporous MoO3/SiO2 solid acid catalyst0 aAcetalization of glycerol using mesoporous MoO3SiO2 solid acid c aPO BOX 211, 1000 AE AMSTERDAM, NETHERLANDSbELSEVIER SCIENCE BVcSEP a150-1580 v3103 a

Acetalization of glycerol with various aldehydes has been carried out using mesoporous MoO3/SiO2 as a solid acid catalyst. A series of MoO3/SiO2 catalysts with varying MoO3 loadings(1-20 mol%) were prepared by sol-gel technique using ethyl silicate-40 and ammonium heptamolybdate as silica and molybdenum source respectively. The sol-gel derived samples were calcined at 500 degrees C and characterized using various physicochemical characterization techniques. The XRD of the calcined samples showed the formation of amorphous phase up to 10 mol% MoO3 loading and at higher loading of crystalline alpha-MoO3 on amorphous silica support. TEM analyses of the materials showed the uniform distribution of MoO3 nanoparticles on amorphous silica support. Raman spectroscopy showed the formation of silicomolybdic acid at low Mo loading and a mixture of alpha-MoO3 and polymolybdate species at high Mo loadings. Moreover the Raman spectra of intermediate loading samples also suggest the presence of beta-MoO3. Acetalization of glycerol with benzaldehyde was carried out using series of MoO3/SiO2 catalysts with varying MoO3 loadings (1-20 mol%). Among the series, MoO3/SiO2 With 20 mol% MoO3 loadings was found to be the most active catalyst in acetalization under mild conditions. Maximum conversion of benzaldehyde (72%) was obtained in 8 h at 100 degrees C with 60% selectivity for the six-membered acetal using 20% MoO3/SiO2. Interestingly with substituted benzaldehydes under same reaction conditions the conversion of aldehydes decreased with increase in selectivity for six-membered acetals. These results indicate the potential of this catalyst for the acetalization of glycerol for an environmentally benign process. (C) 2009 Elsevier B.V. All rights reserved.

10aAcetalization10aAldehyde10aGlycerol10aSilicomolybdic acid10asolid acid1 aUmbarkar, Shubhangi, B.1 aKotbagi, Trupti, V.1 aBiradar, Ankush, V.1 aPasricha, Renu1 aChanale, Jyoti1 aDongare, Mohan, K.1 aMamede, Anne-Sophie1 aLancelot, Christine1 aPayen, Edmond uhttps://library.ncl.res.in/content/acetalization-glycerol-using-mesoporous-moo3sio2-solid-acid-catalyst-001634nas a2200217 4500008004100000022001400041245007600055210006900131260009900200300001400299490000800313520085400321653002201175653001301197653002401210653001801234100001601252700002001268700002601288856010201314 2009 eng d a0960-852400aMannitol production from glycerol by resting cells of Candida magnoliae0 aMannitol production from glycerol by resting cells of Candida ma aTHE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, OXON, ENGLANDbELSEVIER SCI LTDcOCT a4911-49130 v1003 a

Production of mannitol from glycerol by resting cells of Candida magnoliae under aerobic condition was investigated. The resting cells were Suspended in aqueous Solution of glycerol in Erlenmeyer flasks and incubated on rotary shaker. The samples were analyzed by ion exclusion-HPLC equipped with refractive index and UV detector. The resting cells of C. magnoliae produced mannitol from fructose, Sucrose and glycerol but not from glucose. Addition of yeast extract and/or potassium phosphate to the glycerol solution adversely affected its conversion to mannitol. The conversion of glycerol to mannitol was dependent on oxygen availability. Using testing cells, the yield of mannitol was as high as 45%. This is probably the first report of conversion of glycerol to mannitol by osmophilic yeast. (C) 2009 Elsevier Ltd. All rights reserved.

10aCandida magnoliae10aGlycerol10aMannitol production10aResting cells1 aKhan, Asiya1 aBhide, Amey, J.1 aGadre, Ramchandra, V. uhttps://library.ncl.res.in/content/mannitol-production-glycerol-resting-cells-candida-magnoliae-001646nas a2200277 4500008004100000022001400041245008400055210006900139260005700208300001200265490000800277520071600285653000601001653001801007653002401025653001301049653002901062100002101091700002101112700002501133700002801158700002301186700002101209700002901230856010901259 2010 eng d a1011-372X00aCu:Al Nano catalyst for selective hydrogenolysis of glycerol to 1,2-propanediol0 aCuAl Nano catalyst for selective hydrogenolysis of glycerol to 1 a233 SPRING ST, NEW YORK, NY 10013 USAbSPRINGERcMAR a141-1470 v1353 a

Non-chromium Cu:Al nano catalyst prepared by simultaneous co-precipitation and digestion method without any template or stabilizer, showed three times higher activity than the bulk Cu-Cr catalyst for hydrogenolysis of glycerol in both isopropanol and water solvents, with the selectivity to 1,2-Propanediol (1,2-PDO) as high as 91% at 493 K and H(2) pressure of 7 MPa in 5 h. XRD pattern showed the presence of Cu(+) species in the activated Cu: Al nano catalyst. Although Cu(+) is catalytically inactive in glycerol hydrogenolysis reaction, the presence of Cu(+) helps to stabilize the particle size in a narrow range of 7-11 nm by inhibiting the sintering of copper particles under reaction conditions.

10a110a2-Propanediol10aCu:Al nano catalyst10aGlycerol10aSelective hydrogenolysis1 aMane, Rasika, B.1 aHengne, Amol, M.1 aGhalwadkar, Ajay, A.1 aVijayanand, Subramanian1 aMohite, Pravin, H.1 aPotdar, Hari, S.1 aRode, Chandrashekhar, V. uhttps://library.ncl.res.in/content/cual-nano-catalyst-selective-hydrogenolysis-glycerol-12-propanediol-002448nas a2200337 4500008004100000022001400041245010600055210006900161260007600230300001200306490000600318520131100324653001301635653001301648653002801661653001301689653002401702100002101726700001801747700001601765700002201781700002101803700001901824700002201843700002701865700002301892700002101915700002301936700002201959856012901981 2010 eng d a1864-563100aRenewable H-2 from glycerol steam reforming: effect of La2O3 and CeO2 addition to Pt/Al2O3 catalysts.0 aRenewable H2 from glycerol steam reforming effect of La2O3 and C aCOMMERCE PLACE, 350 MAIN ST, MALDEN 02148, MA USAbWILEY-BLACKWELLcMAY a619-6280 v33 a

Glycerol is the main byproduct of biodiesel production and its increased production volume derives from the increasing demand for biofuels. The conversion of glycerol to hydrogen-rich mixtures presents an attractive route towards sustainable biodiesel production. Here we explored the use of Pt/Al2O3-based catalysts for the catalytic steam reforming of glycerol, evidencing the influence of La2O3 and CeO2 doping on the catalyst activity and selectivity. The addition of the latter metal oxides to a Pt/Al2O3 catalyst is found to significantly improve the glycerol steam reforming, with high H-2 and CO2 selectivities. A good catalytic stability is achieved for the Pt/La2O3/Al2O3 system working at 350 degrees C, while the Pt/CeO2/Al2O3 catalyst sharply deactivates after 20 h under similar conditions. Studies carried out on fresh and exhausted catalysts reveal that both systems maintain high surface areas and high Pt dispersions. Therefore, the observed catalyst deactivation can be attributed to coke deposition on the active sites throughout the catalytic process and only marginally to Pt nanoparticle sintering. This work suggests that an appropriate support composition is mandatory for preparing high-performance Pt-based catalysts for the sustainable conversion of glycerol into syngas.

10abiofuels10aGlycerol10aheterogeneous catalysis10aplatinum10asupported catalysts1 aMontini, Tiziano1 aSingh, Rakesh1 aDas, Piyali1 aLorenzut, Barbara1 aBertero, Nicolas1 aRiello, Pietro1 aBenedetti, Alvise1 aGiambastiani, Giuliano1 aBianchini, Claudio1 aZinoviev, Sergey1 aMiertus, Stanislav1 aFornasiero, Paolo uhttps://library.ncl.res.in/content/renewable-h-2-glycerol-steam-reforming-effect-la2o3-and-ceo2-addition-ptal2o3-catalysts-001629nas a2200277 4500008004100000022001400041245010600055210006900161260007300230300001200303490000800315520066700323653000800990653001300998653002301011653002401034100002501058700002101083700002001104700001901124700001601143700001701159700002001176700002501196856013001221 2014 eng d a1381-116900a1,8-Diazabicyclo[5.4.0]undec-7-ene (DBU): a highly efficient catalyst in glycerol carbonate synthesis0 a18Diazabicyclo540undec7ene DBU a highly efficient catalyst in gl aPO BOX 211, 1000 AE AMSTERDAM, NETHERLANDSbELSEVIER SCIENCE BVcSEP a144-1490 v3913 a

Transesterification of dimethyl carbonate (DMC) with glycerol (GLY) was investigated using various amines as catalysts. Amidines like 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU) and 1,5-diazabicyclo[4.3.0]non-5-ene (DBN) were found to be the best catalysts for this reaction. Best results: 98% conversion of GLY with 96% selectivity to GC (TON: 9408), were obtained with DBU as a catalyst. Effect of various reaction conditions on activity and selectivity were investigated using DBU as catalyst. The mechanism of the reaction was investigated with the help of H-1, C-13 and N-15 NMR analysis and OFT calculations. (C) 2014 Elsevier B.V. All rights reserved.

10aDBU10aGlycerol10aGlycerol carbonate10atransesterification1 aMunshi, Mudassir, K.1 aGade, Swapna, M.1 aMane, Manoj, V.1 aMishra, Deepti1 aPal, Sourav1 aVanka, Kumar1 aRane, Vilas, H.1 aKelkar, Ashutosh, A. uhttps://library.ncl.res.in/content/18-diazabicyclo540undec-7-ene-dbu-highly-efficient-catalyst-glycerol-carbonate-synthesis-002623nas a2200409 4500008004100000022001400041245012500055210006900180260000800249490000800257520131500265653002101580653002101601653001401622653001301636653002501649653002801674653002401702653002201726653001901748653001501767653002301782653001801805653002601823653001701849653001301866653002501879653003101904653002201935653002301957100002101980700001402001700002102015700002402036700002902060856012402089 2017 eng d a0926-337300aInfluence of carbon based supports on selectivity behavior of diols and propanol in Ru catalyzed glycerol hydrogenolysis0 aInfluence of carbon based supports on selectivity behavior of di cMAY0 v2043 a

Activated carbon (AC) and three graphite materials were studied as supports for Ru catalyzed glycerol hydrogenolysis to propanediols and 1-propanol. Structural characteristics of AC and graphite materials were found to greatly affect the reducibility and particle size of supported Ru and hence, the activity and product distribution in glycerol hydrogenolysis. XRD of graphite materials showed distinctly (002) plane having highly organized layered structure and the peak intensity decreased in the order of Ru/KS150 > Ru/HSAG100 > Ru/KS6 due to decrease in the graphite sheet thickness. In Raman, the intense D band in HSAG100 compared to that in KS6 and KS150 samples indicated its highly amorphous nature or mixed carbon hybridization. Glycerol conversion for Ru on AC was higher than that on graphite and among different graphites, it showed a descending activity order of Ru/KS6 > Ru/HSAG100 > Ru/KS150. The product distribution for AC and HSAG100 supported Ru was similar, giving 1-propanol (45%) alongwith 1,2-propanediol (1,2-PDO) (37%) and 1,3-propanediol (1,3-PDO) (9–11%). For graphite supports, availability of Ru although bigger in size (4–5 nm), would be higher on the surface than in case of AC which formed deep hydrogenolysis products like 1-, 2- propanol, ethanol etc.

10aactivated carbon10aAmorphous carbon10acatalysis10aGlycerol10aGlycerol conversions10aGlycerol hydrogenolysis10agraphite composites10aGraphite supports10aHydrogenolysis10aHydrolysis10alayered structures10aParticle size10aProduct distributions10aPropanediols10aPropanol10aSelectivity behavior10aStructural characteristics10aStructural effect10aStructural effects1 aMane, Rasika, B.1 aPatil, S.1 aShirai, Masayuki1 aRayalu, Sadhana, S.1 aRode, Chandrashekhar, V. uhttps://library.ncl.res.in/content/influence-carbon-based-supports-selectivity-behavior-diols-and-propanol-ru-catalyzed03203nas a2200265 4500008004100000022001400041245017200055210006900227260000800296300001400304490000700318520224200325653002802567653001302595653001902608653002002627653002302647100001902670700002302689700001802712700002102730700002902751700002602780856013102806 2020 eng d a2155-543500aControlling and stabilization of Ru nanoparticles by tuning the nitrogen content of the support for enhanced H-2 production through aqueous-phase reforming of glycerol0 aControlling and stabilization of Ru nanoparticles by tuning the  cFEB a2489-25070 v103 a

The stable activity of catalysts is an important issue in catalysis, particularly aqueous-phase reforming (APR) of renewable oxygenates, of biomass origin, to get H-2. Sintering of metal nanoparticles on supports affects catalyst stability. To alleviate this problem, a series of highly stable Ru-supported catalysts with controlled metal nanoparticle sizes have been prepared via the easy incipient wetness impregnation method. These catalysts were used for APR of glycerol to produce H-2. Nitrogen-doped mesoporous carbons (NMCs) were utlized as supports and found to have a strong influence on the catalytic performance of the catalysts. Incorporation of nitrogen in the carbon framework significantly enhanced the catalytic activity compared to Ru catalysts on nitrogen-free supports. Notably, the catalyst (5 wt % Ru-NMC-3) with optimal N content (10.9 wt %) demonstrated improved stability and H-2 selectivity, which are better than those of many state-of-the-art catalysts. Nitrogen in the carbon framework has a dual relationship with the activity of the catalyst: (i) it creates basic environment over the catalysts support and (ii) it acts as an anchoring site for metal nanoparticles. Anchoring of metal nanoparticles has helped to curb their sintering, thus leading to better stability of the catalysts under APR reaction conditions. Various characterization techniques were employed to understand the nature of active catalytic sites responsible for higher H-2 production while minimizing CO formation. In situ CO-FTIR studies showed that the higher catalytic activity of 5 wt % Ru-NMC-3 catalyst was attributed to the enhanced WGS activity over this catalyst. Density functional theory calculations were performed to understand the stabilization of metal nanoparticles by different types of N present on the support and provide insights into the prefered sites of glycerol adsorption on the NMC support. Since S wt % Ru-NMC-3 was the relatively best catalyst, it was selected for the preparation of bimetallic catalysts. Accordingly, addition of Pt to this system helped to increase the stability of the catalyst. This bimetallic catalyst may, therefore, find application for wide use in APR of biomass oxygenates.

10aaqueous-phase reforming10aGlycerol10aH-2 production10aRu/NMC catalyst10asynergistic effect1 aGogoi, Pranjal1 aKanna, Narsimharao1 aBegum, Pakiza1 aDeka, Ramesh, C.1 aSatyanarayana, C., V. V.1 aRaja, Thirumalaiswamy uhttps://library.ncl.res.in/content/controlling-and-stabilization-ru-nanoparticles-tuning-nitrogen-content-support-enhanced-h-201923nas a2200241 4500008004100000022001400041245015200055210006900207260000900276300001400285490000700299520108500306653001301391653002501404653001301429653002401442653001401466100001901480700002801499700002301527700000501550856012601555 2020 eng d a2470-155600aSynthesis and characterization of supported heteropoly acid: efficient solid acid catalyst for glycerol esterification to produce biofuel additives0 aSynthesis and characterization of supported heteropoly acid effi cNOV  a1157-11650 v503 a

Esterification of glycerol with acetic acid has been studied with different solid acid catalysts, prepared by impregnating phospotungustic, silicotungstic, and phosphomolybdic acids on polymeric material polyvinylpyrrolidone. These results were compared with commercially available montmorillonite KSFO catalyst showed that PVP-DTP gave higher selectivity to di- and triacetins. This study was mainly focused on increasing the selectivity toward triacetin which is an excellent alternative to fossil fuel based fuel additives. The detail characterization was done for the PVP-DTP catalyst which gave complete conversion of glycerol and maximum selectivity of 34% toward triacetin. Complete conversion of glycerol was achieved at 110 degrees C within 6 h of reaction time. The characterization of the catalyst was performed by SEM/EDX, X-ray diffraction, thermogravimetic techniques, and FT-IR analysis.TPD-NH3 characterization showed that DTP supported on PVP increases the catalyst acidity of PVP. The highest acidity of PVP-DTP is also confirmed using NH3-TPD analysis.

10aGlycerol10aphospostugustic acid10apovidone10asolid acid catalyst10atriacetin1 aMagar, Subhash1 aMohanraj, Govindraj, T.1 aJana, Sumit, Kumar1 a uhttps://library.ncl.res.in/content/synthesis-and-characterization-supported-heteropoly-acid-efficient-solid-acid-catalyst02316nas a2200229 4500008004100000022001400041245006900055210006700124260000800191300001400199490000600213520159900219653001301818653001901831653003201850653001701882653001601899100001901915700002901934700002601963856009701989 2021 eng d a2365-654900aActive K-OMS-2 supported catalyst for hydrogenolysis of glycerol0 aActive KOMS2 supported catalyst for hydrogenolysis of glycerol cSEP a8700-87080 v63 aPropanediols are very important chemical intermediates, which need to be prepared through commercially viable routes. Cryptomelane type octahedral molecular sieve-2 (K-OMS-2), a cheap and environmentally benign microporous oxide was employed to support Ru and used as a catalyst to get 1,2-propanediol (1,2-PDO) selectively through hydrogenolysis of glycerol. Three catalysts with different Ru content were prepared and evaluated for glycerol hydrogenolysis. Among these, 1 wt.% Ru-K-OMS-2 showed reasonably good activity towards 1,2-PDO formation under moderate reaction conditions even at lower Ru loading (0.9 wt.%). When other metals such as Cu and Ni were supported on K-OMS-2, their performance was inferior compared to Ru-supported catalysts. All the catalysts were characterized using various physicochemical techniques like XRD, N-2-sorption, TPD, H-2-TPR, TGA, ICP-OES, FE-SEM and TEM. The enhanced catalytic activity with the 1 wt.%Ru-K-OMS-2 catalyst was attributed to the better Ru metal dispersion, higher active metal surface area, basic strength, and porosity of the support. The catalyst was found to be recyclable. Analysis of spent catalyst by TEM showed disintegration of Ru nanoparticles to smaller ones, under high H-2 pressure at the reaction temperature. Smaller Ru particles are expected to promote C-C bond cleavage thus suppressing 1,2-PDO formation. Furthermore, a relationship between the TOF value, Ru nanoparticles size, and the basic strength of the catalysts was established, which provides dipper insight into the different catalytic behavior of the catalysts.10aGlycerol10aHydrogenolysis10aoctahedral molecular sieves10aPropanediols10aselectivity1 aGogoi, Pranjal1 aChilukuri, Satyanarayana1 aThirumalaiswamy, Raja uhttps://library.ncl.res.in/content/active-k-oms-2-supported-catalyst-hydrogenolysis-glycerol02081nas a2200205 4500008004100000022001400041245009200055210006900147260000800216520137100224653000601595653001801601653004401619653002501663653001301688653001901701100002101720700002101741856011301762 2021 eng d a0161-494000aAdvances in solid catalysts for selective hydrogenolysis of glycerol to 1,3-propanediol0 aAdvances in solid catalysts for selective hydrogenolysis of glyc cJAN3 a

Glycerol is one of the top 12 platform chemicals obtained from biomass. Its surplus availability as a by-product of biodiesel, fat-splitting and soap manufacturing industries and affordable price lends significant opportunity for its valorization, using solid catalysts, into propanediols (PDOs), particularly to 1,3-propanediol (1,3-PDO), by selective hydrogenolysis. 1,3-PDO is an important chemical with wide applications including that as a precursor in polymers manufacturing. However, the synthesis of 1,3-PDO by selective cleavage of the secondary C-O bond of glycerol in the presence of hydrogen (instead of the primary C-O bond yielding 1,2-PDO) is highly challenging. Of late, supported Pt and Ir catalysts in combination with a reducible oxide (WO(x)or ReOx) were found selective for 1,3-PDO formation. Support, metals composition and additives (co-added metals) affect the performance of these catalysts. Detailed investigations revealed that metal dispersion, electronic connectivity between metal and metal oxide/support, hydrogen activation/spillover and Bronsted acidity are some parameters that influence the activity and selectivity of these bi-functional, metal-metal oxide catalysts. This review summarizes the latest advances in these solid catalysts for selective hydrogenolysis of glycerol to 1,3-PDO, a monomer for advanced polymers.

10a110a3-Propanediol10abifunctional metal-metal oxide catalyst10abiomass valorization10aGlycerol10aHydrogenolysis1 aBhowmik, Susmita1 aDarbha, Srinivas uhttps://library.ncl.res.in/content/advances-solid-catalysts-selective-hydrogenolysis-glycerol-13-propanediol02064nas a2200265 4500008004100000022001400041245011200055210006900167260000800236300001400244490000700258520120900265653000601474653001701480653001701497653002101514653001301535653001301548653002701561100001801588700002001606700001901626700002501645856012801670 2021 eng d a0268-257500aBioglycerol (C3) upgrading to 2,3-butanediol (C4) by cell-free extracts of Enterobacter aerogenes NCIM 26950 aBioglycerol C3 upgrading to 23butanediol C4 by cellfree extracts cMAY a1316-13250 v963 a

BACKGROUND Production of biobased chemicals from renewable resources is a green starring approach that serves as a substitute to petroleum derivatives. Bioglycerol, with its growing production as a co-product of biodiesel, is an attractive low-cost feedstock for the synthesis of platform chemicals by microbial fermentation. 2,3-butanediol (2,3-BDO) is amongst the top biorefinery platform chemicals that can be produced by glycerol fermentation. RESULTS The `Circular Economy' concept is demonstrated by converting the by-product bioglycerol using a cell-free extract of Enterobacter aerogenes NCIM 2695 (National Collection of Industrial Microorganisms, NCIM), yielding 22 g L-1 2,3-BDO, in 96 h, 98% atom economy and 0.4 g/g E factor. The cell-free bioglycerol conversion to 2,3-BDO was proved using a modified procedure for determining glycerol dehydrogenase enzyme assay by protein analysis and it was also shown to be cell-bounded. CONCLUSION Our study offers an effective utilization of the leftover material (i.e. cell-free extract) that biocatalysed C3 to C4 diol, which adds value to the overall economics of the process using only crude glycerol (C3) itself as a fermentative medium.

10a210a3-Butanediol10aatom economy10acircular economy10aE factor10aGlycerol10aglycerol dehydrogenase1 aParate, Roopa1 aBorgave, Mrunal1 aDharne, Mahesh1 aRode, Chandrashekhar uhttps://library.ncl.res.in/content/bioglycerol-c3-upgrading-23-butanediol-c4-cell-free-extracts-enterobacter-aerogenes-ncim01395nas a2200265 4500008004100000022001400041245009200055210006900147260000800216300001400224490000600238520057700244653001600821653000800837653001300845653001600858653001300874100002000887700002100907700001700928700002500945700002200970700001800992856011901010 2021 eng d a2365-654900aGlycerol-triazole conjugated rhodamine as colorimetric and fluorimetric sensor for Cu2+0 aGlyceroltriazole conjugated rhodamine as colorimetric and fluori cSEP a9288-92920 v63 a{A glycerol-triazole tethered rhodamine based colorimetric and fluorimetric sensor 3 `,6 `-bis(diethylamino)-2-(((1-(1,3-dihydroxypropan-2-yl)-1H-1,2,3-triazol-4 -yl)methylene)aminospiro [isoindoline-1,9 `-xanthen]-3-one (L1) is designed and synthesized for the selective recognition of Cu2+ ion. The sensor L1 allows naked eye detection of Cu2+ ion with a fast response (<1 min). Among the various metal ions tested, the sensor L1 shows selective binding with Cu2+ through turn-on fluorescence mechanism. The sensor shows 1 : 2 binding stoichiometry with binding constant10aCu2+ Sensor10aDFT10aGlycerol10aRhodamine B10aTriazole1 aVerma, Abhishek1 aGahlyan, Parveen1 aBawa, Rashim1 aDash, Soumya, Ranjan1 aPrasad, Ashok, K.1 aKumar, Rakesh uhttps://library.ncl.res.in/content/glycerol-triazole-conjugated-rhodamine-colorimetric-and-fluorimetric-sensor-cu202135nas a2200253 4500008004100000022001400041245011400055210006900169260000800238300001100246490000700257520127700264653002601541653001301567653002301580653002101603100002301624700001801647700002101665700001601686700002401702700002501726856013001751 2021 eng d a0019-452200aRole of preparation parameters of Cu-Zn mixed oxide catalyst in solvent free glycerol carbonylation with urea0 aRole of preparation parameters of CuZn mixed oxide catalyst in s cJUL a1000900 v983 aSolvent-free carbonylation of glycerol with urea to glycerol carbonate (GC) was achieved over heterogeneous Cu-Zn mixed oxide catalyst. Cu-Zn catalysts with different ratios of Cu:Zn were prepared using co-precipitation (CP) and oxalate gel (OG) methods. As compared to CuO-ZnO(2:1) catalyst prepared by oxalate gel (OG) method, much higher conversion of glycerol and highest selectivity towards glycerol carbonate (GC) was achieved with CuO-ZnO_CP(2:1) catalyst. Physicochemical properties of prepared catalysts were investigated by using XRD, FT-IR, BET, TPD of CO2 and NH3 and TEM techniques. The effect of stoichiometric ratio of Cu/Zn, calcination temperature of CuO-ZnO catalysts and effect of reaction parameters such as molar ratio of substrates, time and temperature on glycerol conversion to GC were critically studied. Cu/Zn of 2:1 ratio, glycerol-urea 1:1 molar ratio, 145 degrees C reaction temperatures were found to be optimized reaction conditions to achieve highest glycerol conversion of 86% and complete selectivity towards GC. The continuous expel of NH 3 from reaction the mixture avoided formation of ammonia complex with CuO-ZnO catalyst. As a result of this, CuO-ZnO catalyst could be recycled up to three times without losing its initial activity.10aCo-precipitation (CP)10aGlycerol10aGlycerol carbonate10aOxalate gel (OG)1 aCharate, Shrinivas1 aShinde, Suhas1 aKondawar, Sharda1 aDesai, Uday1 aWadgaonkar, Prakash1 aRode, Chandrashekhar uhttps://library.ncl.res.in/content/role-preparation-parameters-cu-zn-mixed-oxide-catalyst-solvent-free-glycerol-carbonylation01669nas a2200253 4500008004100000245009700041210006900138260000800207300000900215490000700224520088900231653000901120653001501129653001301144653002301157653000701180653001101187653000601198100002101204700002501225700002001250700002101270856012401291 2022 eng d00aC-O hydrogenolysis of C3-C4 polyols selectively to terminal diols over Pt/W/SBA-15 catalysts0 aCO hydrogenolysis of C3C4 polyols selectively to terminal diols  cSEP a10700 v123 a

Pt/W/SBA-15 catalysts (with Pt-loading = 0.5-4 wt% and W-loading = 1 wt%) prepared by the sequential impregnation method were evaluated for selective C-O cleavage of erythritol and glycerol in an aqueous medium. The Pt and W particles dispersed on SBA-15 approached close proximity at higher Pt loadings and afforded synergistic enhancement in C-O hydrogenolysis activity/selectivity. 1,4-Butanediol yields of 30.9% (at 190 degrees C, 50 bar H-2 and 24 h) and 1,3-propanediol yields of 34.4% (at 190 degrees C, 50 bar H-2 and 12 h of reaction) were obtained over these catalysts. Pt nanoparticles (facilitating dissociative H-2 adsorption and spillover) and W (present as acidic oligomeric WOx species; activating and coordinating the polyol via 1 degrees-OH group) worked in tandem for the selective hydrogenolysis of polyols yielding terminal diols of industrial demand.

10adiol10aErythritol10aGlycerol10aHydrodeoxygenation10aPt10aSBA-1510aW1 aBhowmik, Susmita1 aEnjamuri, Nagasuresh1 aMarimuthu, Banu1 aDarbha, Srinivas uhttps://library.ncl.res.in/content/c-o-hydrogenolysis-c3-c4-polyols-selectively-terminal-diols-over-ptwsba-15-catalysts01770nas a2200241 4500008004100000022001400041245010500055210006900160260000800229300001500237490000700252520097900259653000801238653003001246653001301276653001701289653002601306653001101332100001801343700001701361700002501378856012501403 2022 eng d a2193-580700aInfluence of catalyst reduction temperature on autogenous glycerol hydrogenolysis over NiAl catalyst0 aInfluence of catalyst reduction temperature on autogenous glycer cFEB ae2021007040 v113 a

Autogenous glycerol hydrogenolysis to 1,2-propanediol by aqueous phase reforming (APR) was investigated over supported nickel catalysts. Effect of reduction temperature on physico-chemical properties of catalysts played a significant role in tuning conversion and product selectivities. The formation of nickel aluminate (NiAl2O4) spinel phase during catalyst reduction led to rearrangement of Ni species to obtain small and stable Ni particles. The catalyst activation temperature alters the extent of reduction of multivalent Ni species (Ni-0, Ni+2/+3) which facilitated glycerol dehydration and hydrogenation while suppressing C-C cleavage and thus avoiding undesirable side products. Additionally, presence of moderate Bronsted/Lewis acid ratio of the catalyst promoted higher 1,2-PDO selectivity. In-situ glycerol hydrogenolysis involves glycerol dehydration to acetol with simultaneous reforming to H-2 and CO2 and this hydrogen converts acetol to 1,2-PDO.

10aAPR10aautogenous hydrogenolysis10aGlycerol10aPropanediols10areduction temperature10aspinel1 aPandya, Rajan1 aMane, Rasika1 aRode, Chandrashekhar uhttps://library.ncl.res.in/content/influence-catalyst-reduction-temperature-autogenous-glycerol-hydrogenolysis-over-nial02074nas a2200277 4500008004100000022001400041245013100055210006900186260000800255300001100263490000800274520114500282653001801427653001701445653001301462653002301475653001901498653002201517100002101539700002501560700001901585700002101604700002001625700002101645856013001666 2022 eng d a2468-823100aInsights into active tungsten species on Pt/W/SBA-15 catalysts for selective hydrodeoxygenation of glycerol to 1,3-propanediol0 aInsights into active tungsten species on PtWSBA15 catalysts for  cOCT a1127040 v5313 a

Diols are important class of industrial chemicals. Their synthesis from bio-resources (instead from fossil feed-stocks) is sustainable. In this study, we probed active tungsten species on Pt/W/SBA-15 catalysts for selective synthesis of 1,3-propanediol (1,3-PDO) from aqueous glycerol through a liquid-phase hydrodeoxygenation re-action. A synergistic enhancement in glycerol conversion and 1,3-PDO selectivity was observed when both Pt and W were present on the catalyst. A volcano-shape variation followed with a gradual increase in glycerol conversion and 1,3-PDO yield with W-loading (0.25-15 wt%) was observed. Pt dispersion and acidity of the catalyst dis-played similar variations with the W-loading confirming their critical role in the reaction. Structure-function relationships inferred that oligomeric WOx with moderate Bro center dot nsted acidity (predominant at 1 wt% W-loading) in contact with dispersed Pt are the active species for 1,3-PDO formation and crystalline WO3 with strong Bro center dot nsted acidity (prevalent above 4 wt% W-loading) in association with Pt nanoparticles lead to 1-propanol formation.

10a3-Propanediol10aActive sites10aGlycerol10aHydrodeoxygenation10aHydrogenolysis10aSupported Pt-WO x1 aBhowmik, Susmita1 aEnjamuri, Nagasuresh1 aSethia, Govind1 aAkula, Venugopal1 aMarimuthu, Banu1 aDarbha, Srinivas uhttps://library.ncl.res.in/content/insights-active-tungsten-species-ptwsba-15-catalysts-selective-hydrodeoxygenation-glycerol01633nas a2200253 4500008004100000022001400041245008300055210006900138260000800207300001100215490000800226520083900234653001401073653001301087653001401100653001301114653002301127653002001150653002401170100002101194700002401215700002901239856011101268 2022 eng d a1566-736700aPerception of glycerol carbonate as green chemical: synthesis and applications0 aPerception of glycerol carbonate as green chemical synthesis and cDEC a1065420 v1723 a

Glycerol carbonate (GC) is a prominent component in industrial practice and has a remarkable potential for the sophisticated applications. While GC has come into prominence due to the perceived overflow of glycerol (GLY) as a coproduct of biodiesel industry, its contemporary and future downstream applications are driving tremendous interest in recent years. This review comprises strategies for glycerol carbonate synthesis, properties and its applications. The conversion of GLY to GC via transesterification has appeared in consensus to be the most promising route. A detailed explanation of the effect of the catalysts and operating conditions on the GC yield to provide an updated understanding of the process are summarized. Future directions for GC production through catalytic transesterification are also discussed.

10aBiodiesel10abiofuels10acatalysis10aGlycerol10aGlycerol carbonate10agreen chemistry10atransesterification1 aGade, Swapna, M.1 aSaptal, Vitthal, B.1 aBhanage, Bhalchandra, M. uhttps://library.ncl.res.in/content/perception-glycerol-carbonate-green-chemical-synthesis-and-applications01866nas a2200241 4500008004100000022001400041245011300055210006900168260000800237300001400245490000800259520106200267653001801329653002101347653001301368653001301381653002201394100002501416700002201441700002601463700000501489856013001494 2023 eng d a0008-403400aActivity performance and kinetics for glycerol carbonylation with urea over Zn-Co mixed metal oxide catalyst0 aActivity performance and kinetics for glycerol carbonylation wit cAPR a2075-20930 v1013 a

Efficient carbonylation of glycerol using urea with Zn-Co mixed metal oxide (MMO) catalyst has been achieved. Various methods of catalyst preparation were explored for glycerol carbonate (GC) synthesis. The optimized method of catalyst preparation was found to be co-precipitation (CP) with a Zn:Co ratio of 70:30, achieving 81% glycerol conversion with 97% GC selectivity. X-ray diffraction (XRD) studies revealed the formation of ZnO, Co-3 O-4, and spinel ZnCo2O4 phases. Thermal treatment given to the catalyst allows insertion of Zn cations into Co3O4 lattice forming ZnCo2O4 phase which was also evidenced in X-ray photoelectron spectroscopy (XPS) and Raman spectroscopy. Herein, for the first time, reaction kinetics was studied to propose the rate equation, based on which a plausible reaction pathway is proposed involving two-site adsorption of glycerol (basic site) and urea (acidic site), which undergo carbonylation followed by cyclization into GC. A recycle study and hot filtration test have proven the reusability of the catalyst.

10aCarbonylation10acyclic carbonate10aGlycerol10akinetics10amixed metal oxide1 aKondawar, Sharda, E.1 aKasar, Gaytri, B.1 aKhatua, Angshuman, S.1 a uhttps://library.ncl.res.in/content/activity-performance-and-kinetics-glycerol-carbonylation-urea-over-zn-co-mixed-metal-oxide02539nas a2200289 4500008004100000022001400041245014400055210006900199260000900268300001600277490000700293520157100300653002101871653001301892653001901905653001301924653001401937653000801951100002301959700002101982700001802003700002302021700001902044700002802063700003002091856012802121 2024 eng d a1944-824400aElectrocatalytic glycerol conversion: a low-voltage pathway to efficient carbon-negative green hydrogen and value-added chemical production0 aElectrocatalytic glycerol conversion a lowvoltage pathway to eff cMAY  a26130-261410 v163 a

Electrochemical glycerol oxidation reaction (GLYOR) could be a promising way to use the abundantly available glycerol for production of value-added chemicals and fuels. Completely avoiding the oxygen evolution reaction (OER) with GLYOR is an evolving strategy to reduce the overall cell potential and generate value-added chemicals and fuels on both the anode and cathode. We demonstrate the morphology-controlled palladium nanocrystals, afforded by colloidal chemistry, and their established morphology-dependent GLYOR performance. Although it is known that controlling the morphology of an electrocatalyst can modulate the activity and selectivity of the products, still it is a relatively underexplored area for many reactions, including GLYOR. Among nanocube (Pd-NC), truncated octahedron (Pd-TO), spherical and polycrystalline (Pd-PC) morphologies, the Pd-NC electrocatalyst deposited on a Ni foam exhibits the highest glycerol conversion (85%) along with 42% glyceric acid selectivity at a low applied potential of 0.6 V (vs reversible hydrogen electrode (RHE)) in 0.1 M glycerol and 1 M KOH at ambient temperature. Owing to the much favorable thermodynamics of GLYOR on the Pd-NC surface, the assembled electrolyzer requires an electricity input of only similar to 3.7 kWh/m(3) of H-2 at a current density of 100 mA/cm(2), in contrast to the requirement of >= 5 kWh/m(3) of H-2 with an alkaline/PEM electrolyzer. Sustainability has been successfully demonstrated at 10 and 50 mA/cm(2) and up to 120 h with GLYOR in water and simulated seawater.

10aelectrocatalysis10aGlycerol10agreen hydrogen10ananocube10aPalladium10aSDG1 aChauhan, Inderjeet1 aBajpai, Himanshu1 aRay, Bishakha1 aKolekar, Sadhu, K.1 aDatar, Suwarna1 aPatra, Kshirodra, Kumar1 aGopinath, Chinnakonda, S. uhttps://library.ncl.res.in/content/electrocatalytic-glycerol-conversion-low-voltage-pathway-efficient-carbon-negative-green02551nas a2200253 4500008004100000022001400041245017900055210006900234260000800303300001100311490000800322520161300330653001801943653001301961653001901974653002201993653002802015100002102043700002902064700001502093700002802108700003002136856013102166 2024 eng d a0021-951700aOxidative and selective C-C cleavage of glycerol to glycolaldehyde with atom-like Cu on Cu-TiO2: photocatalytic water reduction with concurrent glycerol oxidation in sunlight0 aOxidative and selective CC cleavage of glycerol to glycolaldehyd cSEP a1156440 v4373 a

Concurrent consumption of electrons and holes for the conversion of a biomass component to value added products represents a highly efficient and sustainable approach towards utilizing renewable energy, but difficult to achieve. The integration of hydrogen production with glycerol oxidation presents a novel and sustainable approach towards achieving a circular economy. In the current study, integration of atom-like Cu-clusters onto TiO2 substrate has been achieved using a facile photo-deposition technique (TC-PDO). Also, novel synthetic approaches have been employed to augment the surface coverage of Cu on TiO2 with atom-like clusters of Cu, either by borohydride treatment on TiO2 followed by Cu-deposition (TC-200) or oxygen-vacancy creation by UV illumination followed by Cu-deposition (TC-PDO). Increased dispersion and enhanced electronic integration of Cu with TiO2 lead to a corresponding increase in the efficiency of photocatalytic hydrogen evolution (13.8 mmol/h.g for TC-PDO at pH 9). Several atom-like Cu integrated with each TiO2 particle acts as photocatalytic reactor, and the same enhances electron-hole separation as well as activity. Sustainable aspect was also studied for TC-PDO up to 25 h at pH 9. Concurrently, glycerol oxidation displays the highest selectivity to C2 product (glycolaldehyde with 70 %) with a C-C cleavage. The investigation of this process holds significant potential for the extensive and simultaneous exploitation of electrons and holes in order to achieve water splitting and glycerol oxidation towards selective value-added products formation.

10aC -C Cleavage10aGlycerol10ananotechnology10aPhoto -deposition10asolar energy conversion1 aBajpai, Himanshu1 aNivedhitha, Thazhath, R.1 aDais, Elsa1 aKanungo, Subhashree, S.1 aGopinath, Chinnakonda, S. uhttps://library.ncl.res.in/content/oxidative-and-selective-c-c-cleavage-glycerol-glycolaldehyde-atom-cu-cu-tio2-photocatalytic01921nas a2200205 4500008004100000022001400041245015100055210006900206260000800275490000800283520112400291653001801415653002701433653001301460653002801473653003301501100002801534700002301562856013001585 2024 eng d a0926-669000aReview on microbial 1, 3-propanediol production: Emerging strategies, key hurdles and attainable solutions to re-establish its commercial interest0 aReview on microbial 1 3propanediol production Emerging strategie cMAR0 v2093 a

1,3-propanediol (1,3-PDO) is a vital value-added bi-functional compound that has numerous uses in the industrial sector including the polymer, pharmaceutical, food, and cosmetics industries. 1,3-PDO biosynthesis from renewable resources through green methods has received considerable attention. However, technical difficulties such as low product titer, by-product accumulation, and incomplete substrate consumption impede its sustainable production at the industrial scale. Hence, understanding the overall 1,3-PDO process development with integrated knowledge of techno-economics would help to build more production facilities across the world. In this view, the biotechnological production of 1,3-PDO is systematically reviewed briefing the synthesis routes, microbial strains, metabolic pathways, and fermentation modes along with several purification strategies. The present review also summarizes key hurdles in 1,3-PDO production and discusses the attainable solutions to achieve higher product titer. Finally, the economic viability of 1,3-PDO biosynthesis is described based on the existing research.

10a3-Propanediol10aFermentation processes10aGlycerol10aPurification strategies10aTechno-economical assessment1 aNimbalkar, Pranhita, R.1 aDharne, Mahesh, S. uhttps://library.ncl.res.in/content/review-microbial-1-3-propanediol-production-emerging-strategies-key-hurdles-and-attainable01445nas a2200265 4500008004100000022001400041245011800055210006900173260000900242300001100251490000800262520055100270653001900821653002100840653001300861653000800874653002100882100002000903700002900923700002400952700002000976700003000996700002101026856013201047 2025 eng d a1383-586600aEuropium oxide on carbon nitride for electrocatalytic glycerol oxidation coupled with hydrogen evolution reaction0 aEuropium oxide on carbon nitride for electrocatalytic glycerol o cNOV  a1334420 v3723 a

{The integration of the electrochemical glycerol oxidation reaction (GOR) with the hydrogen evolution reaction (HER) has emerged as a promising alternative to the sluggish oxygen evolution reaction (OER) in water splitting toward the development of renewable and clean energy sources. However, suitable electrodes that facilitate redox kinetics while increasing the selectivity of the desired product(s) are still required. Herein, a series of europium oxide (Eu2O3) anchored on graphitic carbon nitride (g-CN) nanoaggregates (g-CNEux

10acarbon support10aelectrocatalysis10aGlycerol10aHER10aRare earth metal1 aJana, Jayasmita1 aSharma, Tata, Sanjay Kan1 aGhanem, Mohamed, A.1 aChoi, Won, Mook1 aGopinath, Chinnakonda, S.1 aHur, Seung, Hyun uhttps://library.ncl.res.in/content/europium-oxide-carbon-nitride-electrocatalytic-glycerol-oxidation-coupled-hydrogen-evolution02493nas a2200325 4500008004100000022001400041245010800055210006900163260000900232300000800241490000800249520144900257653001301706653002001719653002001739653002901759100001701788700001701805700001901822700002001841700001801861700002601879700002101905700002101926700001801947700002401965700002601989700002302015856012902038 2025 eng d a0974-362600aFacile and eco-friendly synthesis of Mn2O3 nanoparticles via microwave-assisted glycerol-thermal method0 aFacile and ecofriendly synthesis of Mn2O3 nanoparticles via micr cNOV  a1020 v1373 a

Microwave-assisted efficient synthesis of nanosized manganese oxide (Mn2O3) is reported using glycerol and manganese acetate. Glycerol in this reported methodology acts as an efficient solvent for this nanomaterial synthesis under microwave radiation. This reported method enables the synthesis of nanosized Mn2O3 without further use of additives, stabilizers, and bases other than glycerol and manganese precursor. Glycerol is a renewable biomaterial derived nonvolatile and nontoxic, safe solvent. It has a high boiling point and dielectric constant, which makes it an ideal solvent for microwave synthesis. The synthesized nanosized Mn2O3 was analyzed by X-ray diffraction (XRD), high-resolution transmission electron microscopy (HRTEM), X-ray photoelectron spectroscopy (XPS), and Raman spectroscopy. We examined the catalytic properties of as-synthesized Mn2O3 for cinnamyl alcohol oxidation to cinnamaldehyde. In this oxidation activity experiment, nanosized Mn2O3 exhibits good conversion and selectivity towards the desired product. We also made an attempt to understand the probable mechanism of nanomaterial formation and found some conclusive evidence to support it. This research methodology is facile, energy efficient, and involves minimum chemicals for synthesis. It makes this reported methodology not only economically attractive but also environmentally friendly, which aligns well with green chemistry principles.

10aGlycerol10agreen chemistry10aNanosized Mn2O310ananostructured catalysis1 aYadav, Akash1 aJha, Ratnesh1 aBhatkar, Akash1 aGehlot, Bhavika1 aKamble, Aditi1 aManikandan, Marimuthu1 aBhosale, Hritvik1 aVaishnav, Vishal1 aRathod, Rutik1 aUmbarkar, Shubhangi1 aRaja, Thirumalaiswamy1 aBhatte, Kushal, D. uhttps://library.ncl.res.in/content/facile-and-eco-friendly-synthesis-mn2o3-nanoparticles-microwave-assisted-glycerol-thermal02648nas a2200241 4500008004100000022001400041245014700055210006900202260000800271300001100279490000800290520179100298653002302089653001302112653001802125653003302143100002402176700001802200700002102218700002502239700001902264856012302283 2026 eng d a0957-582000aSolvent-assisted chemical recycling of polycarbonate using glycerol as a renewable chemical: mechanistic insights and statistical optimization0 aSolventassisted chemical recycling of polycarbonate using glycer cMAR a1085920 v2093 a

The rapid accumulation of polycarbonate (PC) waste has driven the development of efficient recycling methods. This study presents a comprehensive investigation of solvent-assisted chemical recycling of PC using glycerol, a renewable chemical derived from industrial waste streams. Solvent screening highlighted the critical influence of solvent properties such as dielectric constant, dipole moment and hydrogen-bond accepting ability on depolymerization efficiency. A systematic approach combining Design of Experiments (DoE) and Response Surface Methodology (RSM) was employed to optimize the depolymerization process. Using a Box-Behnken design (BBD), the effects of key process parameters, including temperature, reaction time and the glycerol (GLY:PC) and dimethylformamide (DMF:PC) weight ratios, were evaluated in terms of PC conversion and bisphenol A (BPA) yield. The optimization model predicted that a reaction temperature of 171 degrees C, a reaction time of 1 h and a PC: GLY:DMF ratio of 1:5.05:7.22 would yield 100 % PC conversion and 85 % BPA yield. Experimental validation under these conditions achieved 100 % PC conversion and 83 % BPA yield, confirming the reliability of the model. Product characterization using NMR, LC-HRMS and FTIR confirmed the purity of BPA and provided insights into the reaction mechanism. The solvent recyclability across successive reaction cycles demonstrated the environmental and economic viability of the process. Overall, the energy demand calculation based on the environmental energy impact factor (xi) highlights the industrial relevance of this work and demonstrate an efficient and environmentally friendly catalyst-free route for depolymerization of polycarbonate with strong potential for industrial implementation.

10aChemical Recycling10aGlycerol10aPolycarbonate10aResponse surface methodology1 aMarkandeya, Nishant1 aJadhav, Mayur1 aGopale, Prafulla1 aRamalingam, Karthick1 aKamble, Sanjay uhttps://library.ncl.res.in/content/solvent-assisted-chemical-recycling-polycarbonate-using-glycerol-renewable-chemical