01631nas a2200229   4500008004100000022001400041245010700055210006900162260007300231300001200304490000800316520077600324653002701100653002101127653002301148653001301171653001201184100002601196700002201222700002901244856012801273       2005                        eng d  a1381-116900aHydroformylation of 1-hexene using Rh/TPPTS complex exchanged on anion exchange resin: kinetic studies0 aHydroformylation of 1hexene using RhTPPTS complex exchanged on a  aPO BOX 211, 1000 AE AMSTERDAM, NETHERLANDSbELSEVIER SCIENCE BVcMAY  a179-1860 v2323 a<p>The exchange of the Rh/Triphenylphosphine trisulfonate sodium [TPPTS] complex on to an anion exchange resin results in a stable heterogenized catalyst for the hydroformylation of alkenes. The kinetics of hydroformylation of 1-hexene using Rh/TPPTS complex exchanged on anion exchange resin to Amberlite IRA-93 has been investigated for the first time. The rate of the reaction was found to be dependent on the partial pressure of hydrogen and 1-hexene concentrations with a first order. A maximum in the rate with increasing partial pressure of carbon monoxide was observed. A rate model has been proposed which predicts the observed rate data within reasonable error. The activation energy was found to be 84.37 kJ/mol. (c) 2005 Elsevier B.V. All rights reserved.</p>10aheterogenized catalyst10aHydroformylation10aion-exchange resin10akinetics10aRhodium1 aDiwakar, Makarand, M.1 aDeshpande, R., M.1 aChaudhari, Raghunath, V.  uhttps://library.ncl.res.in/content/hydroformylation-1-hexene-using-rhtppts-complex-exchanged-anion-exchange-resin-kinetic-102138nas a2200265   4500008004100000022001400041245012100055210006900176260010600245300001400351490000700365520112700372653002301499653003801522653001301560653002901573653002501602653001501627100002201642700002501664700001501689700002401704700001801728856012601746       2011                        eng d  a0009-250900aKinetics of hydroformylation of 1-octene in ionic liquid-organic biphasic media using rhodium sulfoxantphos catalyst0 aKinetics of hydroformylation of 1octene in ionic liquidorganic b  aTHE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, ENGLANDbPERGAMON-ELSEVIER SCIENCE LTDcAPR  a1631-16390 v663 a<p>Biphasic hydroformylation of 1-octene was performed using rhodium sulfoxantphos catalyst dissolved in [BuPy][BF(4)] ionic liquid. Preliminary experiments proved this system to retain the catalytic complex within the ionic liquid phase and to maintain a high selectivity towards the linear aldehyde (n:iso ratio of 30) over several cycles. Process parameter investigation showed a first order dependence of the initial rate with respect to the catalyst and 1-octene concentrations, but a more complex behavior with respect to hydrogen (fractional order) and carbon monoxide partial pressures (inhibition at high pressures). Different mathematical models were selected based on the trends observed and evaluated for data fitting. Also, rate models were derived from a proposed mechanism, using Christiansen matrix approach. To calculate concentrations of substrates in the catalytic phase as required by this kinetic modeling, solubility measurements were preformed for the gases (pressure drop technique), as well as for 1-octene and n-nonanal (thermogravimetry analysis). (C) 2011 Elsevier Ltd. All rights reserved.</p>10aBiphasic catalysis10aButylpyridinium tetrafluoroborate10akinetics10aParameter identification10aReaction engineering10asolubility1 aDeshpande, R., M.1 aKelkar, Ashutosh, A.1 aSharma, A.1 aJulcour-Lebigue, C.1 aDelmas, Henri  uhttps://library.ncl.res.in/content/kinetics-hydroformylation-1-octene-ionic-liquid-organic-biphasic-media-using-rhodium-001506nas a2200205   4500008004100000022001400041245009700055210006900152260010700221300001400328490000700342520070200349653001801051653001301069653003101082653002401113100001901137700002201156856012201178       2012                        eng d  a0970-707700aKinetics of hydrogenation of lauric acid in a batch slurry reactor using Ru-Sn/TiO2 catalyst0 aKinetics of hydrogenation of lauric acid in a batch slurry react  a11/100 RAJENDRA NAGAR, SECTOR 3,, SAHIBABAD 201 005, GHAZIABAD, INDIAbASIAN JOURNAL OF CHEMISTRYcJUN  a2767-27710 v243 a<p>Ru-Sn catalyst was prepared in-house by impregnation method. This catalyst was found to be stable for four recycles. The rate of hydrogenation of lauric acid (LAC) using Ru-Sn/TiO2 catalyst was found to be linearly dependent on catalyst loading, lauric acid concentration old hydrogen partial pressure. The rate data obtained from kinetic study were fitted to simple rate equation based on Langmuir-Hinshelwood (L-H) type model. Based on kinetic data the hydrogenation of lauric acid over Ru-Sn/TiO2 catalyst is proposed to occur by I dual site mechanism the activation energy for hydrogenation of lauric acid to lauryl alcohol (LAOH) using Rii-Sn/TiO2 catalyst was found to be 77.2 kJ/mol.</p>10aHydrogenation10akinetics10aLangmuir-Hinshelwood model10aRu-Sn/TiO2 catalyst1 aShinde, S., B.1 aDeshpande, R., M.  uhttps://library.ncl.res.in/content/kinetics-hydrogenation-lauric-acid-batch-slurry-reactor-using-ru-sntio2-catalyst-0