@article {46755, title = {Maximization of furanic compounds formation by dehydration and hydrogenation of xylose in one step over SO3-H functionalized H-beta catalyst in alcohol media}, journal = {Biomass \& Bioenergy}, volume = {139}, year = {2020}, month = {AUG}, pages = {105646}, type = {Article}, abstract = {

Furanic compounds such as furfural (FUR); furfuryl alcohol (F. Alc) are important renewable platform chemicals can be used as such or further convert for preparation of other value added products such as Levulinic acid (LA), Alkyl Levulinates, 2-Methyltetrahydrofuran (MTHF), and Tetrahydrofuran (THF) etc. Sulfonated H-beta zeolite was successfully prepared and used for the synthesis of furanic compounds especially FUR and F. Alc from c-xylose in one step using isopropanol as alcohol media. Prepared catalyst was well characterized by powder X-ray diffraction (XRD), scanning electron microscopy (SEM), BET, NH3-Temperature programmed desorption (TPD) and carbon-hydrogen-nitrogen-sulfur analysis (CHNS). It was found the total acid amount was increased with increase in sulfur loading which confirmed the sulfonic acid group (SO3-H) was successfully grafted onto zeolite structure. 3 wt\% H-beta-SO3-H catalyst with optimized reaction parameters of 150 degrees C, 7 h, 25 wt\% catalyst loading was tuned to get the highest furanic compound yield of 88.5\% (FUR 76.8\% + F.Alc 11.7\%).The reusability study confirmed that there was a marginal drop of similar to 25\% after 3 recycle runs.

}, keywords = {furfural, Furfuryl alcohol, H-beta, isopropanol, sulfonated zeolite, Xylose}, issn = {0961-9534}, doi = {10.1016/j.biombioe.2020.105646}, author = {Gupta, Anshita and Nandanwar, Sachin U. and Niphadkar, Prashant and Simakova, Irina and Bokade, Vijay} } @article {46763, title = {Review of porous adsorbents for the separation of nitrogen from natural gas}, journal = {Industrial \& Engineering Chemistry Research}, volume = {59}, year = {2020}, month = {JUL}, pages = {13355-13369}, type = {Review}, abstract = {

Natural gas is one of the critical fossil fuel sources in the world to fulfill current energy demand in the global market. Methane is the primary component in natural gas and its concentration is dependent on the source; a variety of impurities, such as nitrogen, carbon dioxide, oxygen, helium, hydrogen sulfide, water, and heavier hydrocarbons can be present, which reduces the overall fuel quality. Purification of natural gas is important in order to meet the U.S. pipeline and minimum heating value specifications. The separation of nitrogen from methane is challenging because of their similar molecular size (i.e., the two gases differ in kinetic diameter by only 0.16 angstrom). This Review discusses different methods for separating nitrogen from methane. Of these methods, pressure swing adsorption is one of the most effective techniques for separating nitrogen from natural gas using porous adsorbents, and encouraging results have been demonstrated in the past few decades. Many types of porous adsorbents are discussed here, including carbon molecular sieves, activated carbons, zeolites, titanosilicates, and metal-organic frameworks. Future trends and materials are discussed to put into perspective the new opportunities in this research area.

}, issn = {0888-5885}, doi = {10.1021/acs.iecr.0c02730}, author = {Nandanwar, Sachin U. and Corbin, David R. and Shiflett, Mark B.} } @article {47585, title = {Active nickel hollow nanosphere supported over SiO2 catalyst for reduction of nitro compound}, journal = {Particulate Science and Technology}, volume = {40}, year = {2021}, month = {APR}, pages = {325-335}, type = {Article}, abstract = {

Nickel hollow nanospheres (Ni HNSs) was prepared by solvothermal method using mixture of ethylenediamine (EN) and ethanol (ET), sodium borohydride as reducing agent and nickel chloride hexahydrate as precursor. The particle size of the Ni HNSs were tuned by varying several parameters including precursor concentrations, reaction temperatures (130-190 degrees C), and ET to EN volume ratios. The particle size and morphology of Ni HNSs were confirmed by dynamic light scattering and transmission electron microscope, respectively. Spherical shape of Ni nanoparticles of 300 nm size having similar to 200 nm hollow space and 50 nm thickness was achieved at optimize condition of 4:6 volume ratio of ET/EN, 150 degrees C temperature, 0.1 M NaBH4 concentration, and 7 h. Ni HNSs supported over SiO2 (Ni HNSs/SiO2) with different loading of Ni HNSs (1-10 wt.\%) were prepared by impregnation method. The catalyst was characterized by X-ray diffraction, and inductively coupled plasma - optical emission spectroscopy. The catalytic performance of Ni HNSs/SiO2 was carried out in the reduction of 4-Nitrophenol (4-NP) to 4 - Aminophenol (4-AP). 5 wt.\% Ni HNSs/SiO2 exhibited 87\% reduction of 4-NP in 25 min and stable up to 6 catalyst cycles due to higher surface area of the catalyst.

}, keywords = {4-Aminophenol, 4-nitrophenol, Catalyst, hollow nanospheres, Nanoparticles, Nickel}, issn = {0272-6351}, doi = {10.1080/02726351.2021.1947424}, author = {Pawar, Priyanka S. and Lokhande, Aboli A. and Nandanwar, Sachin U. and Niphadkar, Prashant S. and Bokade, Vijay V.} } @article {46681, title = {Milder operating parameters for one-step conversion of fructose to levulinic acid over sulfonated H-beta zeolite in aqueous media}, journal = {Environmental Progress \& Sustainable Energy}, volume = {40}, year = {2021}, month = {JAN}, pages = {e13530}, type = {Article}, abstract = {

The sulfonated H-beta zeolite was successfully prepared and used for the synthesis of levulinic acid (LA) fromD-fructose. The catalyst was characterized by powder X-ray diffraction, Fourier transform infrared spectroscopy, scanning electron microscope, N-2 physisorption, NH3-temperature programmed desorption and carbon-hydrogen-nitrogen-sulfur analysis. The total acid amount is increased with increase in sulfur loading, confirmed that the sulfonic acid group (SO3-H) is successfully grafted onto zeolite structure. The various parameters such as different amount of sulfur loading, reaction temperature, time, catalyst loading was studied for selective production of LA. The catalytic activity of sulfonated H-beta (S-beta) zeolite was found to be efficient for synthesis of LA from D-fructose in aqueous media. Maximum LA yield of 43.5 mol\%, low HMF yield (\<1\%) with 98.15\% fructose conversion was obtained with 3\% S-beta catalyst at 160 degrees C for 7 hr. The catalyst was reusable for minimum three times by H2O2 regeneration. This study provides the new zeolitic catalyst for the efficient production of LA at shorter reaction time (7 hr) and low catalyst to substrate ratio (0.7:1).

}, keywords = {conversion, D-fructose, H-beta, HMF, levulinic acid, sulfonated zeolite, yield}, issn = {1944-7442}, doi = {10.1002/ep.13530, Early Access Date = OCT 2020}, author = {Bisen, Swapneel K. and Niphadkar, Prashant S. and Nandanwar, Sachin U. and Simakova, Irina and Bokade, Vijay V.} } @article {47811, title = {Milder operating parameters for one-step conversion of fructose to levulinic acid over sulfonated H-β zeolite in aqueous media}, journal = {Environmental Progress \& Sustainable Energy}, volume = {40}, year = {2021}, month = {FEB}, pages = {e13530}, type = {Article}, abstract = {Abstract The sulfonated H-β zeolite was successfully prepared and used for the synthesis of levulinic acid (LA) from D-fructose. The catalyst was characterized by powder X-ray diffraction, Fourier transform infrared spectroscopy, scanning electron microscope, N2 physisorption, NH3-temperature programmed desorption and carbon{\textendash}hydrogen{\textendash}nitrogen{\textendash}sulfur analysis. The total acid amount is increased with increase in sulfur loading, confirmed that the sulfonic acid group (SO3-H) is successfully grafted onto zeolite structure. The various parameters such as different amount of sulfur loading, reaction temperature, time, catalyst loading was studied for selective production of LA. The catalytic activity of sulfonated H-β (S-β) zeolite was found to be efficient for synthesis of LA from D-fructose in aqueous media. Maximum LA yield of 43.5 mol\%, low HMF yield (<1\%) with 98.15\% fructose conversion was obtained with 3\% S-β catalyst at 160{\textdegree}C for 7 hr. The catalyst was reusable for minimum three times by H2O2 regeneration. This study provides the new zeolitic catalyst for the efficient production of LA at shorter reaction time (7 hr) and low catalyst to substrate ratio (0.7:1).}, keywords = {conversion, D-fructose, H-β, HMF, levulinic acid, sulfonated zeolite, yield}, doi = {10.1002/ep.13530}, url = {https://aiche.onlinelibrary.wiley.com/doi/abs/10.1002/ep.13530}, author = {Bisen, Swapneel K. and Niphadkar, Prashant S. and Nandanwar, Sachin U. and Simakova, Irina and Bokade, Vijay V.} } @article {47129, title = {Review on selective production of acetophenone from oxidation of ethylbenzene over heterogeneous catalysts in a decade}, journal = {Catalysis Letters}, year = {2021}, month = {JAN}, type = {Article; Early Access 2021}, abstract = {

The consumption of acetophenone (AP) is increasing worldwide because of its applications in products such as alcohol, aldehydes, resins, esters, fragrances, and pharmaceuticals. AP is manufactured via several methods like decomposition of cumene hydroperoxide, Hock process, and Friedel-Crafts acylation reaction using homogeneous catalysts with solvent and oxidant. However, it causes several environmental problems that deteriorate the production of AP with these methods. Oxidation of ethylbenzene (EB) is one of the promising methods to synthesize AP in liquid and vapor phases reaction using heterogeneous catalysts, which plays a vital role for selective production of AP. In this review, numerous heterogeneous catalysts are discussed including transition metal nanoparticles, transition metal complexes, and metal free catalysts (carbon nanotubes) used in last 10 years for oxidation of EB. Additionally, catalyst activity along with reaction parameters and its effect, mechanisms, and kinetics study are summarized in this article. The future scope of this reaction is also highlighted. Moreover, this work identifies best catalysts for bulk production of AP with high yield to satisfy global requirement.

}, keywords = {acetophenone, ethylbenzene, Heterogeneous catalysts, Oxidation reaction, reaction mechanisms}, issn = {1011-372X}, doi = {10.1007/s10562-020-03474-8, Early Access Date = JAN 2021}, author = {Nandanwar, Sachin U. and Rathod, Simmy and Bansal, Videsha and Bokade, Vijay V.} } @article {47895, title = {Catalytic activity of CuFe2O4 spinel oxide for liquid-phase oxidation of cinnamyl alcohol}, journal = {ChemistrySelect}, volume = {7}, year = {2022}, month = {FEB}, pages = {e202104441}, type = {Article}, abstract = {

CuFe2O4 spinel oxide catalyst was synthesized by sol-gel and co-precipitation methods for liquid phase oxidation of Cinnamyl alcohol (CnOH) to Cinnamaldehydes (CnHO) using tert-Butyl hydroperoxide (TBHP) as oxidising agent. Spinel oxide catalyst was characterized by different techniques such as X-ray diffraction (XRD), N-2 adsorption-desorption, BET surface area, and X-ray photoelectron spectroscopy (XPS) to understand the structural, physical properties and oxidation state of the catalyst. The result shows that catalyst prepared by sol-gel method was found higher surface area and smaller crystalline size than co-precipitation method. XPS data confirm the formation of Cu2+ in the spinel which helps to improve the catalytic activity of oxidation. This reaction follows radical mechanism, and exhibited 76.7 \% of CnOH conversion and 68.4 \% of CnHO, and 24.8 \% benzaldehyde (benzald) selectivity using TBHP at 60 degrees C. Kinetic data reveal that 41.2 kJ/mol of activation energy for the reaction. The higher activity of spinel oxide catalyst could be due synergetic effect of spinel (88 \%) and oxides (12 \%) formed in the catalyst, which helps to provide the oxygen during reaction. The contribution of Cu2+ is higher in sol-gel than co-precipitation, which may provide the better reactivity of catalyst. This work helps to select the effective and cost-effective catalyst for the oxidation of CnOH.

}, keywords = {Catalysts, Cinnamaldehyde, Cinnamyl Alcohol, Cupper, iron, oxide, spinel}, issn = {2365-6549}, doi = {10.1002/slct.202104441}, author = {Dange, Rutvija M. and Niphadkar, Prashant S. and Bokade, Vijay V. and Nandanwar, Sachin U.} } @article {47984, title = {Methanol-to-light olefins reaction using Zn-Ag modified SSZ-13 catalyst}, journal = {ChemistrySelect}, volume = {7}, year = {2022}, month = {SEP}, pages = {e202201476}, type = {Article}, abstract = {

The 2 wt.\% of Zn and Ag (Zn1-x-Ag-x; x=0.2, 0.4, 0.6 \%) modified SSZ-13 (SZ-13) zeolite was prepared by wet-impregnation method, and its catalytic activity was demonstrated for methanol-to-olefin (MTO). The Zn-0.6-Ag-0.4/SZ-13 catalyst exhibited high catalytic activity due to change in properties of catalyst. The Zn particles were highly dispersed inside the SZ-13; while Ag particles were dispersed on the surface of SZ-13, confirmed by HRTEM and surface area. The small \% of Ag over SZ-13 promotes ethylene production via aromatization of reaction, and highly dispersed Zn on SZ-13 help to produce stable ethylene and propylene. The Zn-0.6-Ag-0.4/SZ-13 catalyst showed (similar to 10 \%) higher light olefin (87 \%) selectivity than parent SZ-13 as well as mono metal incorporated SZ-13. The higher catalytic activity was attributed due to effect of both metals (Zn and Ag), where Ag promotes partial aromatization on the surface, and Zn increases the Lewis acidity in the zeolite pore. This catalyst can help to improve the selectivity of light olefin using MTO reaction.

}, keywords = {Ethylene, Methanol-to-Olef, Propyl, Silver, SSZ, zinc}, issn = {2365-6549}, doi = {10.1002/slct.202201476}, author = {Dange, Rutvija M. and Gawali, Chirag B. and Niphadkar, Prashant S. and Bokade, Vijay V. and Nandanwar, Sachin U.} } @article {48702, title = {Equilibrium adsorption of nitrogen, oxygen, and argon on silver-exchanged hierarchical ETS-10}, journal = {Journal of Chemical and Engineering Data}, volume = {68}, year = {2023}, month = {JUL}, pages = {2159-2172}, type = {Article}, abstract = {

Silver-exchanged hierarchical ETS-10(Ag-H-ETS-10) was synthesizedusing Ag+ exchange with hierarchical Engelhard titanosilicate(H-ETS-10) using silver nitrate solution. The physical propertiesof the adsorbent were analyzed using X-ray diffraction (XRD), BETsurface area, nitrogen adsorption-desorption, pore volume,energy dispersive spectroscopy (EDS), and high resolution-transmissionelectron microscopy (HR-TEM). N-2 physisorption data confirmedthat a micro-mesoporous (bimodal) structure was created in the Ag-H-ETS-10.The equilibrium adsorbent data of pure gases N-2, O-2, and Ar were investigated in the temperature range from 288to 318 K up to 10 bar. The equilibrium adsorption capacity of Ag-H-ETS-10was found to be 1.12 mmol g(-1) for N-2,0.87 mmol g(-1) for O-2, and 1.09 mmol g(-1) for Ar at 298 K and \& SIM;10 bar. \& SIM;20\% higheradsorption capacity was found for N-2 and Ar in Ag-H-ETS-10compared to Ag-ETS-10. The higher sorption capacity was attributedto the formation of a bimodal structure and \& pi;-complexation interactionby the Ag cation, which allows a multilayer of N-2 and Armolecules. The Sips isotherm model was well fitted for the Ag-H-ETS-10experimental data among Langmuir, Freundlich, Toth, and Temkin models.The measured equilibrium adsorption data for Ag-H-ETS-10 can be usefulfor the O-2 purification process.

}, issn = {0021-9568}, doi = {10.1021/acs.jced.3c00124}, author = {Shrotri, Aadesh R. and Niphadkar, Prashant S. and Bokade, Vijay V. and Nandanwar, Sachin U.} }