@article { ISI:000230435900058, title = {Kinetic modeling of reductive alkylation of aniline with acetone using Pd/Al2O3 catalyst in a batch slurry reactor}, journal = {Industrial \& Engineering Chemistry Research}, volume = {44}, number = {14}, year = {2005}, month = {JUL}, pages = {5388-5396}, publisher = {AMER CHEMICAL SOC}, type = {Article}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

The kinetics of reductive alkylation of aniline with acetone was studied in a slurry reactor under isothermal conditions in a temperature range of 378-408 K using 3\% Pd/Al2O3 catalyst. Experimental data on concentration-time as well as hydrogen consumption-time profiles were obtained to study the effect of concentration of aniline, catalyst loading, and partial pressure of hydrogen. Separate controlled experiments were performed to understand the nature of the condensation reaction between aniline and acetone, which forms the Shiff{\textquoteright}s base intermediate. From the concentration-time profiles and the effect of reaction conditions, it was found that the noncatalytic equilibrium formation of the Shiff base intermediate was the slowest step in the multistep reaction sequence. Several rate equations were considered to fit the batch slurry reactor data, and rate models based on competitive dissociative adsorption of hydrogen and the reactive substrates in the rate-limiting catalytic steps were found to represent the experimental data. The kinetic parameters were evaluated by fitting the integral batch reactor data at different temperatures. The activation energies, heat of adsorption, and entropy of adsorption of all the reactant species were also evaluated.

}, issn = {0888-5885}, doi = {10.1021/ie049093+}, author = {Roy, D. and Jaganathan, Rengaswamy and Chaudhari, Raghunath V.} } @article { ISI:000251763600036, title = {Modeling of bubble column slurry reactor for reductive alkylation of p-phenylenediamine}, journal = {Chemical Engineering Science}, volume = {62}, number = {24, SI}, year = {2007}, note = {8th International Conference on Gas-Liquid and Gas-Liquid-Solid Reactor Engineering, Indian Inst Technol Delhi, New Delhi, INDIA, DEC 16-19, 2007}, month = {DEC}, pages = {7290-7304}, publisher = {PERGAMON-ELSEVIER SCIENCE LTD}, type = {Article}, address = {THE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, ENGLAND}, abstract = {

A bubble column slurry reactor (BCSR) model has been developed for the reductive alkylation of p-phenylenediamine (PPDA) with methyl ethyl ketone (MEK) to N, N{\textquoteright}-di-secondary-alkyl-p-phenylenediamine (Di-amine). This particular reaction system is commercially relevant and involves a combination of parallel and consecutive reactions comprising equilibrium non-catalytic (homogeneous) and catalytic (heterogeneous) steps. The proposed model is based on the {\textquoteleft}mixing cell approach{\textquoteright}. In this work the mixing cell approach has been extended by including a liquid backflow stream from all but the bottommost mixing cell. The model incorporates the contributions of gas-liquid and liquid-solid mass transfer, heat effects, and complex multistep reaction kinetics. CFD model is used to estimate the extent of backflow among mixing cells and its dependence on operating parameters. The effect of gas and liquid velocities, catalyst loading, inlet PPDA concentration, and temperature on the conversion, selectivity, global rate of hydrogenation, and temperature rise is discussed. The comparison of the current approach with the traditional mixing cell model is discussed. The BCSR model presented here will be useful to provide guidelines for designing and improving overall performance of bubble column reactors. (C) 2007 Elsevier Ltd. All rights reserved.

}, keywords = {bubble columns, CFD, kinetics, Mathematical modeling, Reductive alkylation}, issn = {0009-2509}, doi = {10.1016/j.ces.2007.08.065}, author = {Chaudhari, Amit S. and Rampure, Mohan R. and Ranade, Vivek V. and Jaganathan, Rengaswamy and Chaudhari, Raghunath V.} } @conference { ISI:000287122200023, title = {Dynamic modeling of hydro- formylation of 1-decene on Rh/C catalyst in bubble colunm slurry reactor}, booktitle = {International Conference on Modeling, Optimization, and Computing}, series = {AIP Conference Proceedings}, volume = {1298}, year = {2010}, note = {International Conference on Modeling, Optimization, and Computing, Durgapur, INDIA, OCT 28-30, 2010}, month = {OCT}, pages = {143-150}, publisher = {Natl Inst Technol Durgapur; SERC, Dept Sci \& Technol; Caledonian Coll Engn; BRNS, Dept Atom Energy; DRDO, Minist Defence}, organization = {Natl Inst Technol Durgapur; SERC, Dept Sci \& Technol; Caledonian Coll Engn; BRNS, Dept Atom Energy; DRDO, Minist Defence}, address = {2 Huntington Quadrangle, STE 1NO1, Melville, NY 11747-4501 USA}, abstract = {

A dynamic model has been developed for the bubble column slurry reactor operating under non-isothermal conditions. The model consists of mass and heat balance equations for the gas and liquid phases and the catalyst particle. The model equations consisted of partial differential equations (PDE) which were converted to ordinary differential equations (ODE) by using finite difference relationships for the spatial derivatives and the ordinary differential equations for the time derivatives (Numerical Method of Lines-NMoL). The model was applied to describe the dynamic behaviour of bubble column slurry reactor during the hydroformylation of 1-decene on Rh/C catalyst. Model simulations were performed to obtain a meaningful path to steady state and to reproduce the other characteristics of the dynamic behaviour of the reactor. Under given conditions, the reaction required approximately 3750 seconds to reach the steady state concentrations at various reactor positions. It was observed with increase in the fluid velocities, the dynamics of the system was altered to 2500 seconds to reach the steady state condition. The effect of axial dispersion on the substrate concentration and the temperature rise along the reactor was further studied and discussed.

}, keywords = {axial dispersion, bubble column slurry reactor, Dynamic modeling, method of line, PDE solutions}, isbn = {978-0-7354-0854-8}, issn = {0094-243X}, doi = {10.1063/1.3516292}, author = {Upkare, Makarand M. and Rajurkar, Kalpendra B. and Das, Samir K. and Jaganathan, Rengaswamy}, editor = {Paruya, S. and Kar, S. and Roy, S.} } @article { ISI:000208189304130, title = {Glycerine to renewable amino alcohol: reaction mechanism and kinetics of the catalytic reductive amination of hydroxyacetone}, journal = {Abstracts of Papers of the American Chemical Society}, volume = {239}, year = {2010}, month = {MAR}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, issn = {0065-7727}, author = {Arredondo, Victor M. and Gibson, Michael S. and Fairweather, Neil T. and Daniels, Angella C. and Kreuzer, David P. and Jaganathan, Rengaswamy} } @conference { ISI:000287122200024, title = {Mathematical modeling and simulation of bubble column reactor for aerial liquid phase cyclohexane oxidation}, booktitle = {International Conference on Modeling, Optimization, and Computing}, series = {AIP Conference Proceedings}, volume = {1298}, year = {2010}, note = {International Conference on Modeling, Optimization, and Computing, Durgapur, INDIA, OCT 28-30, 2010}, month = {OCT}, pages = {151-159}, publisher = {Natl Inst Technol Durgapur; SERC, Dept Sci \& Technol; Caledonian Coll Engn; BRNS, Dept Atom Energy; DRDO, Minist Defence}, organization = {Natl Inst Technol Durgapur; SERC, Dept Sci \& Technol; Caledonian Coll Engn; BRNS, Dept Atom Energy; DRDO, Minist Defence}, address = {2 Huntington Quadrangle, STE 1no1, Melville, NY 11747-4501 USA}, abstract = {

Cyclohexane oxidation is an important but complex commercial reaction, wherein the desired product, K-A oil appears as an intermediates of the reaction sequence. A mathematical model has been developed for the bubble column reactor operating under isothermal conditions. The mass and energy model equations consisted of stiff ODEs. The model was applied to describe the behavior of bubble column reactor for aerial liquid phase cyclohexane oxidation. Effect of initial substrate concentration, catalyst loading and temperature was studied and discussed in detail. Conclusions were presented at the end of the study.

}, keywords = {K-A Oil Selectivity, Mathematical modeling, substrate conversion and product yield analysis}, isbn = {978-0-7354-0854-8}, issn = {0094-243X}, doi = {10.1063/1.3516293}, author = {Upkare, Makarand M. and Rajurkar, Kalpendra B. and Gupta, Pankaj R. and Jaganathan, Rengaswamy}, editor = {Paruya, S. and Kar, S. and Roy, S} }