<?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%">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>