@article { ISI:000257694300013, title = {Rapid extraction and separation of indium(III) with a high molecular weight amine}, journal = {Indian Journal of Chemical Technology}, volume = {15}, number = {3}, year = {2008}, month = {MAY}, pages = {291-297}, publisher = {NATL INST SCIENCE COMMUNICATION}, address = {DR K S KRISHNAN MARG, NEW DELHI 110 012, INDIA}, abstract = {

The liquid-liquid extraction of indium(III) from sodium succinate media using n-octylaniline in toluene as an extractant was studied. Quantitative extraction of indium(III) was observed in the range of 0.004-0.0075 M sodium succinate at pH 3.8-6.0 with 4\% n-octylaniline in toluene. Indium(III) was completely stripped from the metal loaded organic phase of the extractant with water and determined complexometrically. The stoichiometry of the extracted species was determined on the basis of;slope analysis. The extraction was found to proceed by a ion-pair mechanism with the extracted species being [RNH3+In(succinate)(2)(-)](org). Separation of indium(III) was carried out from some associated metals like Tl(I), Mg(II), Ni(II), Cu(II), Zn(II),. Cd(II), Hg(II), Pb(II), GC(IV), Sb(III), Bi(III). The selectivity of the extraction of indium(III) can also be achieved by use of a suitable masking agent for estimation and determination from the synthetic mixture corresponding to alloy to show the practical utility of the extractant.

}, keywords = {Indium(III), n-octylaniline, Separation, solvent extraction, succinate}, issn = {0971-457X}, author = {Shilmkar, T. N. and Kolekar, S. S. and Wadgaonkar, P. P. and Anuse, Mansing A.} } @article { ISI:000314145100008, title = {Behavior of the transport and separation of lanthanum, yttrium and lutetium metal ions through a celluose fiber supported solid membrane}, journal = {Macedonian Journal of Chemistry and Chemical Engineering}, volume = {31}, number = {2}, year = {2012}, month = {Jan}, pages = {255-269}, publisher = {SOC CHEMISTS TECHNOLOGISTS MADECONIA}, type = {Article}, address = {STS CYRIL \& METHODIUS UNIV, FAC TECHNOL \& METALLURGY, PO BOX 560, RUGER BOSKOVIC 16, SKOPJE, MK-1001, MACEDONIA}, abstract = {

A newly designed membrane cell was used to study the behavior of the transport and separation of lanthanum, yttrium and lutetium metal ions using a cellulose fiber supported solid membrane. The cellulose fiber membrane was prepared by the chemical modification of cellulose fiber using an esterification reaction with citric acid. Different experimental variables were investigated, such as time, membrane size, stirring of the source and receiving phases and the pH of the source phase. The use of different stripping agents in the receiving phase was explored, including nitric acid, hydrochloric acid, sodium nitrate, ammonium thiocyanate, D(2)EHPA, TBP, Aliquat-336, tartaric acid, EDTA and organic solvents. Pre-concentration of lanthanum, yttrium and lutetium metal ions from dilute solutions was carried out.

}, keywords = {binary mixture, cellulose fiber membrane, Citric acid, complexing reagent, Lanthanum, lutetium, metal ions, Separation, transport studies, yttrium}, issn = {1857-5552}, author = {Gaikwad, Abaji G.} } @article { ISI:000325204200090, title = {Cinnamic acid derivatives via heck reaction in an aqueous-biphasic catalytic system with easy catalyst-product separation}, journal = {Asian Journal of Chemistry}, volume = {25}, number = {15, A}, year = {2013}, month = {NOV}, pages = {8633-8637}, publisher = {ASIAN JOURNAL OF CHEMISTRY}, address = {11/100 RAJENDRA NAGAR, SECTOR 3,, SAHIBABAD 201 005, GHAZIABAD, INDIA}, abstract = {

A true biphasic [aqueous-organic] system for the coupling of water soluble sodium acrylate with different aryl halides for the synthesis of cinnamic acid derivatives has been developed, employing palladium catalysts that is soluble in organic phase. Amongst them, palladacycle was found to be stable in presence of water and could be recycled for four times with no loss in the activity. Such a system facilitates easy recycle of catalyst and also the removal of the salts from the catalyst phase, ensuring high activity with respect to cumulative turn over number (TON) and turn over frequency (TOF). The reaction was facilitated by organic as well as inorganic bases. The efficiency of the catalyst, role of organic/inorganic bases on the activity is reported.

}, keywords = {Biphasic catalysis, Heck reaction, Palladacycle, Separation}, issn = {0970-7077}, author = {Jagtap, Sangeeta Vijay and Deshpande, R. M.} } @article { ISI:000324153700020, title = {Medium pressure hydrate based gas separation (HBGS) process for pre-combustion capture of carbon dioxide employing a novel fixed bed reactor}, journal = {International Journal of Greenhouse Gas Control}, volume = {17}, year = {2013}, month = {SEP}, pages = {206-214}, publisher = {ELSEVIER SCI LTD}, address = {THE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, OXON, ENGLAND}, abstract = {

This work presents an effective medium pressure hydrate based gas separation (HBGS) process for pre-combustion carbon dioxide capture in a novel fixed bed column. 2.5 mol\% propane was added to the fuel gas mixture as an additive to decrease the operating pressure of the HBGS process. Hydrate formation kinetics was investigated at three different pressures (4.5, 5.5 and 6.0 MPa respectively) and at 274.15 K. The performance of silica sand and silica gel as a medium was evaluated. In silica sand bed, multiple nucleation events were observed. In silica gel bed, the gas uptake and water conversion to hydrates was significantly low at any given driving force than that obtained in silica sand bed. Experiments at different water saturation levels (50, 75 and 100\%) in silica sand bed were investigated at 6.0 MPa and 274.15 K. It was found that at 50\% water saturation, gas consumed for hydrate formation and water conversion to hydrates was almost three times that at 100\% saturation. Water to hydrate conversions of up to 64.3\% was achieved after 4 h of hydrate formation for the 50\% water saturated silica sand bed. Our study presents an opportunity to scale up the HBGS process for CO2 capture with enhanced kinetics by employing a fixed bed reactor configuration. Decomposition experiments at a driving force of Delta T of 10 K and 23K were carried out to recover the gas consumed for hydrate formation and it was found that Delta T of 23 K was sufficient to recover the hydrated gas. (C) 2013 Elsevier Ltd. All rights reserved.

}, keywords = {Carbon dioxide capture, Gas hydrates, Global warming, Pre-combustion, Separation}, issn = {1750-5836}, doi = {10.1016/j.ijggc.2013.05.010}, author = {Babu, Ponnivalavan and Kumar, Rajnish and Linga, Praveen} } @article {46381, title = {Covalent organic framework thin-films for molecular separation}, journal = {Acta Crystallographica A-Foundation and Advances}, volume = {70}, year = {2014}, month = {MAY}, pages = {C547}, type = {Meeting Abstract}, keywords = {Covalent organic framework, Separation, Thin-films}, issn = {2053-2733}, author = {Dey, Kaushik and Banerjee, Rahul} } @article { ISI:000355093500003, title = {Direct glycosylation of unprotected and unactivated sugars using bismuth nitrate pentahydrate}, journal = {Journal of Carbohydrate Chemistry}, volume = {34}, number = {4}, year = {2015}, month = {MAY}, pages = {196-205}, publisher = {TAYLOR \& FRANCIS INC}, address = {530 WALNUT STREET, STE 850, PHILADELPHIA, PA 19106 USA}, abstract = {

Bi(NO3)(3), a low-cost, mild, and environmentally green catalyst, has been successfully utilized for Fischer glycosylation for the synthesis of alkyl/aryl glycopyranosides by reacting unprotected sugars, namely, D-glucose, L-rhamnose, D-galactose, D-arabinose, and N-acetyl-D-glucosamine with various alcohols in good to excellent yields. The glycosides were formed with high alpha-selectivity. Further, an expedient separation of alpha- and beta-glycosides using silver nitrate-impregnated silica gel flash liquid chromatography has been developed.

}, keywords = {Bismuth nitrate, carbohydrates, Fischer glycosylation, Flash chromatography, Separation}, issn = {0732-8303}, doi = {10.1080/07328303.2015.1028585}, author = {Polanki, Innaiah K. and Kurma, Siva H. and Bhattacharya, Asish K.} } @article {43908, title = {Modular assembly of porous organic cage crystals: isoreticular quasiracemates and ternary co-crystal}, journal = {CrystEngComm}, volume = {19}, year = {2017}, month = {SEP}, chapter = {4933-4941}, abstract = {

Small changes in molecular structure and crystallisation conditions can have a profound effect on the crystal packing of molecules. Increasing the system complexity-for example, by introducing multiple components-greatly increases the number of potential outcomes. Hence, the rational design of porous cocrystals with multiple components is challenging. Here, we report a family of isoreticular quasiracemate crystalline phases for porous organic cages, FT-RCC3-R center dot CCX-S (where X = 1, 2, or 4), that were prepared in a modular and predictable fashion. By using directional intermolecular interactions between cages, we were able to prepare a rare ternary co-crystal, (CC3-S(0.5)CC4-S-0.5)center dot(CC13-S(0.5)CC3-S(0.25)CC4-S-0.25).

}, keywords = {cocrystals, Frameworks, Gas-chromatography, Halogen Bonds, Hydrogen-bonds, Molecular Cage, Nanoparticles, Pores, porosity, Separation}, issn = {1466-8033}, doi = {10.1039/c7ce00783c}, author = {Tothadi, Srinu and Little, Marc A and Hasell, Tom and Briggs, Michael E. and Chong, Samantha Y. and Liu, Ming and Cooper, Andrew I.} } @article {46422, title = {Separation of nitroaromatics from wastewater by using supported ionic liquid membranes}, journal = {Journal of Water Process Engineering}, volume = {32}, year = {2019}, month = {DEC}, pages = {100925}, type = {Article}, abstract = {

Nitroaromatics have been released into wastewater during its production and application, thus, contaminating the ecosystem. The stringent discharge limits of industrial effluents have led to the development of sustainable technologies for removal of nitroaromatics from wastewater. In the present investigation, separation of nitroaromatic compounds such as TNT, TNP and Tetryl from model wastewater was investigated by using supported ionic liquid membrane (SILM) process. Various aliquat 336 based ionic liquids (ILs) were synthesised and characterized, and immobilized in PTFE and PVDF supports for the preparation of SILMs. The key parameters such as type of IL and striping phase, feed phase pH, selectivity for SILM, extraction kinetics and reuse of SILM were studied, in detail. The size of IL-anion plays an important role in removal process. The SILM was found to be selective for TNP over other nitroaromatics. Maximum separation of TNP (\< 95\%) was achieved with IL, [A336][SCN] within 12 h. Selectivity and reuse of the membrane indicate the potential of SILM technology as a sustainable chemical process for the treatment of nitroaromatics contaminated wastewater.

}, keywords = {Ionic liquid, Membrane, Nitroaromatics, Separation, wastewater}, issn = {2214-7144}, doi = {10.1016/j.jwpe.2019.100925}, author = {Bhosale, Vikas K. and Chana, Harpreet K. and Kamble, Sanjay P. and Kulkarni, Prashant S.} } @article {48915, title = {Development of multipurpose biomass-derived adsorbents using Coccinia grandis for removal of contaminants}, journal = {Clean Technologies and Environmental Policies }, volume = {25}, year = {2023}, month = {DEC}, pages = {3393-3405}, type = {Article}, abstract = {

The present study is an attempt to develop newer multipurpose biomass-derived adsorbents for water and wastewater treatment; biomass that are easily available, renewable and most importantly, sustainable. A model adsorbent was developed using Coccinia grandis (CG, Ivy gourd) and further modified by impregnating copper nanoparticles (CG-Cu). The adsorbent characterization was done for evaluating surface morphology, surface area and metal modification. The utility of the newer adsorbents was established for the removal of different contaminants such as dyes (cationic Malachite Green, anionic Congo Red and fluorescent cationic Rhodamine B), Active Pharmaceutical Ingredient pollutant (Ciprofloxacin) and also for the removal of pathogenic bacteria, Gram-negative Escherichia coli. Both CG and CG-Cu bio-nanocomposite were highly effective in removal of different contaminants, 99\% dye removal for Malachite Green, with a high adsorption capacity of 49 mg/g, higher than that for commercial activated charcoal whereas for all other dyes, the performance of CG-Cu was similar. The isotherm studies indicated multilayer adsorption, in general. A good adsorption capacity of 10.8 mg/g was also observed for the removal of ciprofloxacin. The combined effect of the bio-nanocomposite, CG-Cu was impressive and 100\% disinfection was achieved within 10 min, due to the antimicrobial activity of Cu and oxidation effect of reactive oxygen species enhancing the disinfection.Graphical abstractMultipurpose biomass derived adsorbents using Coccinia grandis for removal of contaminants

}, keywords = {Adsorption, Biomass, Disinfection, dye removal, nanomaterial, Separation}, issn = {1618-954X}, doi = {10.1007/s10098-023-02598-w}, author = {Raj, Surabhi S. and Mane, Maya B. and Thanekar, Pooja and Balapure, Kshama and Bhandari, Vinay M.} } @article {48291, title = {Short review on recent advances in porous adsorbents for separation of oxygen from atmospheric air}, journal = {Asia-Pacific Journal of Chemical Engineering}, volume = {18}, year = {2023}, month = {MAR}, type = {Review}, abstract = {

Pure oxygen demand is continuously increasing worldwide due to wide applications including medical and industrial. Pressure swing adsorption (PSA) is one of the promising techniques to separate O-2 from atmospheric air. The porous solid adsorbent is a key element in the PSA to trap nitrogen (N-2) and release O-2. Several adsorbents including low silica X (LSX), zeolite 5A, ion-exchanged LSX (Li-LSX, AgLi-LSX, Ca-LSX), Engelhard titanosilicate (Na-ETS-10, Ag-ETS-10), and SSZ-13 have been investigated for adsorption of N-2 from the air. This review article is a summarization of recent research work published on O-2 separation using different porous adsorbents via PSA. This review also emphasizes on the best porous sorbent for purification of O-2 by sorption of N-2 and Ar. The adsorption capacities with experimental conditions are also rigorously discussed. The review also proposed future trends and prospects for O-2 separation. This review will be helpful to choose remarkable adsorbent for the generation pure O-2.

}, keywords = {13X zeolite, adsorbent, ETS-10, oxygen, Separation}, issn = {1932-2135}, doi = {10.1002/apj.2896}, author = {Shrotri, Aadesh R. R. and Niphadkar, Prashant S. S. and Bokade, Vijay V. V. and Utgikar, Vivek P. P. and Nandanwar, Sachin U. U.} } @article {49240, title = {Exploring defect-engineered metal-organic frameworks with 1,2,4-triazolyl isophthalate and benzoate linkers}, journal = {INORGANIC CHEMISTRY}, volume = {63}, year = {2024}, month = {MAY }, pages = {10843-10853}, type = {Journal Article}, keywords = {Separation, spectroscopy, TRIAZOLYL}, issn = {0020-1669}, doi = {10.1021/acs.inorgchem.4c01589}, author = {Chetry, Sibo and Lukman, Muhammad Fernadi and Bon, Volodymyr and Warias, Rico and Fuhrmann, Daniel and Moellmer, Jens and Belder, Detlev and Gopinath, Chinnakonda S. and Kaskel, Stefan and Poeppl, Andreas and Krautscheid, Harald} } @article {49022, title = {Performance of Li exchange hierarchical X zeolite for CO2 adsorption and H2 separation}, journal = {Journal of Industrial and Engineering Chemistry }, volume = {133}, year = {2024}, month = {MAY }, pages = {505-514}, type = {Article}, abstract = {

Li exchange hierarchical X zeolite (Li-H-X) was prepared by decationization of X zeolite by NH4Cl solution followed by Li exchange and subsequent calcination. NH4-X and Li-X were prepared to compare the results of LiH-X. XRD, FE-SEM, EDS, N2 adsorption-desorption, and micro-/mesoporous volume were performed. The higher mesoporosity was confirmed in Li-H-X due to the framework dealumination during decationization. Static and dynamic sorption capacity of sorbents was evaluated to identify the performance of sorbent. The CO2 and H2 equilibrium adsorption capacity of Li-H-X was found to be 9.6 mmol g-1 and 0.78 mmol g-1, respectively, at 298 K and 20 bar, which was 25 \% (CO2) and 30 \% (H2) higher than Li-X. Static experimental data were validated using the Langmuir, Freundlich, and Sips models. The CO2 \& H2 dynamic sorption capacity of Li-H-X sorbent for binary gas (CO2/H2, 25/75 \%) was 4.145 mmol g-1 and 0.258 mmol g-1 at 303 K and 10 bar. The higher sorption capacity of Li-H-X was obtained due to large micro-/mesoporous volume of sorbent, which may allow to access unoccupied sites at higher pressure. This result reveals that micro-/mesoporous structure of zeolite adsorbs significantly higher CO2 from binary gas stream, which can use to separate pure H2 from gas stream.

}, keywords = {Adsorption, Carbon dioxide, Hydrogen, Microporous-mesoporous, Separation}, issn = {1226-086X}, doi = {10.1016/j.jiec.2023.12.027}, author = {Shrotri, Aadesh R. and Birje, Amit R. and Niphadkar, Prashant S. and V. Bokade, Vijay and Mali, Nilesh A. and Nandanwar, Sachin U.} }