01739nas a2200265 4500008004100000020002200041022001400063245011200077210006900189260019400258300001200452490000900464520062700473653002401100653002601124653005201150100002501202700002801227700002201255700002701277700001501304700001201319700001101331856013101342 2010 eng d a978-0-7354-0854-8 a0094-243X00aMathematical modeling and simulation of bubble column reactor for aerial liquid phase cyclohexane oxidation0 aMathematical modeling and simulation of bubble column reactor fo a2 Huntington Quadrangle, STE 1no1, Melville, NY 11747-4501 USAbNatl Inst Technol Durgapur; SERC, Dept Sci & Technol; Caledonian Coll Engn; BRNS, Dept Atom Energy; DRDO, Minist DefencecOCT a151-1590 v12983 a
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.
10aK-A Oil Selectivity10aMathematical modeling10asubstrate conversion and product yield analysis1 aUpkare, Makarand, M.1 aRajurkar, Kalpendra, B.1 aGupta, Pankaj, R.1 aJaganathan, Rengaswamy1 aParuya, S.1 aKar, S.1 aRoy, S uhttp://library.ncl.res.in/content/mathematical-modeling-and-simulation-bubble-column-reactor-aerial-liquid-phase-cyclohexane-0