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The Reduction Of SO2and No In Flue Gas By V2O5/AC Catalyst

Posted on:2014-09-16Degree:MasterType:Thesis
Country:ChinaCandidate:Y J WangFull Text:PDF
GTID:2251330425956817Subject:Chemical processes
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This paper took columnar activated coke as the carrier, prepared two types of catalyst:V2O5/AC catalyst prepared by solution and nano-V2O5/AC catalyst, and studied the difference ofNO reduction, then, had a research of simultaneous desulfurization and denitrificationperformance on nano-V2O5/AC catalyst.The V2O5/AC catalyst prepared with impregnation method by ammonium metavanadatesolution had a NO conversion of34.87%at a loading of3wt%V2O5,200℃,5%O2and10000L/(Kg·h) space velocity. The most suitable conditions were a loading of13wt%, atemperature of200℃, and O2concentration of5%. The NO reduction of V2O5/AC catalystincreased with the decrease of space velocity. NO reduction reached61.89%when the spacevelocity was2500L/(Kg·h).And the presence of water vapor restrained NO reduction.The nano-V2O5/AC catalyst prepared by hydrothermal synthesis method had a better NOreduction. The nano-V2O5in the surface of activated coke showed nanobelts, which was at alength of several micrometers, a width of100300nm and a thickness around100nm. The NOreduction reached45.36%at a loading of1wt%,200℃and2500L/(Kg·h) space velocity.However the NO reduction reached49.72%by adding1wt%Fe2O3. The catalyst prepared bythis method had a stable catalytic performance.O2and H2O had important influence on desulfurization over the catalyst, and the adding ofNO and NH3promoted the SO2reduction. Using the two-step method for desulfurization anddenitration, when the first step reactor temperature was120℃, the second step reactortemperature was200℃, the SO2removal rate reached94.98%, and the NO removal rate was48.76%after10minters.
Keywords/Search Tags:Activated coke, Nano vanadium pentoxide, Desulfurization, Denitration
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