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Reaction Kinetics Study Of Hydrogen Chloride Catalytic Oxidation

Posted on:2020-05-20Degree:MasterType:Thesis
Country:ChinaCandidate:D Q FuFull Text:PDF
GTID:2381330572489542Subject:Chemical processes
Abstract/Summary:PDF Full Text Request
HCl catalytic oxidation is the important process of Cl2 recycling,and it has turned into a current research hotspot of chemical engineering.In order to realize Cl2 efficient recycle and industrial reactor optimization,reaction kinetics of HCl catalytic oxidation over Cu-based composite catalyst was studied.First,reactor reliability was evaluated.In the non-gradient reactor,external diffusion can be eliminated while HCl conversion can reach only 50%.In the fixed-bed reactor external diffusion can’t be eliminated while HCl conversion can reach 90%.Device combined with non-gradient reactor and fixed-bed reactor is suitable for reaction kinetics study.Because external diffusion can be eliminated and HCl conversion can reach 1%~90%,reaction can reach stable in a short time and experimental data has good repeatability.Next,influence of T=360~400℃,nHCl/nO2=1~4,FHCl0/W=0.01~60h-1 on HCl conversion and reaction rate was studied.Before chemical equilibrium,HCl conversion and reaction rate increase with the increase of T,or the decrease of nHCl/nO2;With the decrease of FHCl0/W,HCl conversion increases while HCl reaction rate decreases.After chemical equilibrium,HCl conversion decreases with the increase of T and nHCl/nO2,or the decrease of FHCl0/W.Then,kinetics models were proposed by assuming HCl adsorption,O2 adsorption,surface reaction,and Cl2 desorption as rate-controlling steps,respectively.By NLS method parameters fit and statistical test,the kinetics model assuming O2 adsorption as rate-controlling step can suitably describe the reaction behaviour of HCl catalytic oxidation over Cu-based composite catalyst and the kinetics model is established as follow:Finally,concentration distribution,temperature distribution and thermal stability of tubular fixed-bed reactor were analyzed.At point A,reaction temperature can keep in 369~387℃ when Ts=355~360℃&do=0.025~0.032m.At point B,reaction temperature can keep in 365~410℃ when(Ts)min=341~381℃&△Tmax=24~29℃&(do)max=0.015~0.079m.HCl conversion increases along axial distance and the maximum xHCl=69%.Temperature first increases and then decreases along axial distance and hot spot T=664K appears at Z=1.1m.
Keywords/Search Tags:HCl catalytic oxidation, Cu-based composite catalyst, reaction kinetics, non-gradient reactor, thermal stability
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