Please use this identifier to cite or link to this item: http://nopr.niscair.res.in/handle/123456789/9057
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dc.contributor.authorMehta, A S-
dc.date.accessioned2010-05-26T05:46:46Z-
dc.date.available2010-05-26T05:46:46Z-
dc.date.issued2010-05-
dc.identifier.issn0975-0991 (Online); 0971-457X (Print)-
dc.identifier.urihttp://hdl.handle.net/123456789/9057-
dc.description204-214en_US
dc.description.abstractModel proposed by Wagner et al. for distillation data considering gas phase resistance as the controlling resistance is modified in the present study wherein instead of gas phase resistance liquid phase resistance is considered as the controlling resistance for mass-transfer. This has been successfully applied to the experimental data collected during process development for recovery of bromine from brine employing air-blowing method. Experimental data collected are evaluated based on the modified model of Onda et al. and Wagner et al. Calculated values of mass transfer coefficients tally well with the observed values of mass transfer coefficient. Packed column performance is also compared with the results of Castillo et al. for removal of volatile organic compounds by steam stripping from water, wherein values of volumetric liquid phase mass transfer coefficient ranged from 0.001-0.008 (1/s) whereas in the present study it ranges from 0.0006-0.0164 (1/s).en_US
dc.language.isoen_USen_US
dc.publisherCSIRen_US
dc.sourceIJCT Vol.17(3) [May 2010]en_US
dc.subjectBromineen_US
dc.subjectSodium bromide-bromate solutionen_US
dc.subjectAir blowing processen_US
dc.subjectLiquid phase mass transfer coefficienten_US
dc.subjectInterfacial areaen_US
dc.subjectRandomly packed columnen_US
dc.subjectVolatile organic compoundsen_US
dc.titleStudies on debromination of sea water and aqueous sodium bromide bromate solutionen_US
dc.typeArticleen_US
Appears in Collections:IJCT Vol.17(3) [May 2010]

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