<?xml version="1.0" encoding="UTF-8"?><xml><records><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>47</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Upkare, Makarand M.</style></author><author><style face="normal" font="default" size="100%">Rajurkar, Kalpendra B.</style></author><author><style face="normal" font="default" size="100%">Das, Samir K.</style></author><author><style face="normal" font="default" size="100%">Jaganathan, Rengaswamy</style></author></authors><secondary-authors><author><style face="normal" font="default" size="100%">Paruya, S.</style></author><author><style face="normal" font="default" size="100%">Kar, S.</style></author><author><style face="normal" font="default" size="100%">Roy, S.</style></author></secondary-authors></contributors><titles><title><style face="normal" font="default" size="100%">Dynamic modeling of hydro- formylation of 1-decene on Rh/C catalyst in bubble colunm slurry reactor</style></title><secondary-title><style face="normal" font="default" size="100%">International Conference on Modeling, Optimization, and Computing</style></secondary-title><tertiary-title><style face="normal" font="default" size="100%">AIP Conference Proceedings</style></tertiary-title></titles><keywords><keyword><style  face="normal" font="default" size="100%">axial dispersion</style></keyword><keyword><style  face="normal" font="default" size="100%">bubble column slurry reactor</style></keyword><keyword><style  face="normal" font="default" size="100%">Dynamic modeling</style></keyword><keyword><style  face="normal" font="default" size="100%">method of line</style></keyword><keyword><style  face="normal" font="default" size="100%">PDE solutions</style></keyword></keywords><dates><year><style  face="normal" font="default" size="100%">2010</style></year><pub-dates><date><style  face="normal" font="default" size="100%">OCT</style></date></pub-dates></dates><publisher><style face="normal" font="default" size="100%">Natl Inst Technol Durgapur; SERC, Dept Sci &amp; Technol; Caledonian Coll Engn; BRNS, Dept Atom Energy; DRDO, Minist Defence</style></publisher><pub-location><style face="normal" font="default" size="100%">2 Huntington Quadrangle, STE 1NO1, Melville, NY 11747-4501 USA</style></pub-location><volume><style face="normal" font="default" size="100%">1298</style></volume><pages><style face="normal" font="default" size="100%">143-150</style></pages><isbn><style face="normal" font="default" size="100%">978-0-7354-0854-8</style></isbn><language><style face="normal" font="default" size="100%">eng</style></language><abstract><style face="normal" font="default" size="100%">&lt;p&gt;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.&lt;/p&gt;</style></abstract><notes><style face="normal" font="default" size="100%">International Conference on Modeling, Optimization, and Computing, Durgapur, INDIA, OCT 28-30, 2010</style></notes></record><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>47</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Upkare, Makarand M.</style></author><author><style face="normal" font="default" size="100%">Rajurkar, Kalpendra B.</style></author><author><style face="normal" font="default" size="100%">Gupta, Pankaj R.</style></author><author><style face="normal" font="default" size="100%">Jaganathan, Rengaswamy</style></author></authors><secondary-authors><author><style face="normal" font="default" size="100%">Paruya, S.</style></author><author><style face="normal" font="default" size="100%">Kar, S.</style></author><author><style face="normal" font="default" size="100%">Roy, S</style></author></secondary-authors></contributors><titles><title><style face="normal" font="default" size="100%">Mathematical modeling and simulation of bubble column reactor for aerial liquid phase cyclohexane oxidation</style></title><secondary-title><style face="normal" font="default" size="100%">International Conference on Modeling, Optimization, and Computing</style></secondary-title><tertiary-title><style face="normal" font="default" size="100%">AIP Conference Proceedings</style></tertiary-title></titles><keywords><keyword><style  face="normal" font="default" size="100%">K-A Oil Selectivity</style></keyword><keyword><style  face="normal" font="default" size="100%">Mathematical modeling</style></keyword><keyword><style  face="normal" font="default" size="100%">substrate conversion and product yield analysis</style></keyword></keywords><dates><year><style  face="normal" font="default" size="100%">2010</style></year><pub-dates><date><style  face="normal" font="default" size="100%">OCT</style></date></pub-dates></dates><publisher><style face="normal" font="default" size="100%">Natl Inst Technol Durgapur; SERC, Dept Sci &amp; Technol; Caledonian Coll Engn; BRNS, Dept Atom Energy; DRDO, Minist Defence</style></publisher><pub-location><style face="normal" font="default" size="100%">2 Huntington Quadrangle, STE 1no1, Melville, NY 11747-4501 USA</style></pub-location><volume><style face="normal" font="default" size="100%">1298</style></volume><pages><style face="normal" font="default" size="100%">151-159</style></pages><isbn><style face="normal" font="default" size="100%">978-0-7354-0854-8</style></isbn><language><style face="normal" font="default" size="100%">eng</style></language><abstract><style face="normal" font="default" size="100%">&lt;p&gt;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.&lt;/p&gt;</style></abstract><notes><style face="normal" font="default" size="100%">International Conference on Modeling, Optimization, and Computing, Durgapur, INDIA, OCT 28-30, 2010</style></notes></record></records></xml>