The oxidation of aqueous sodium sulphite solutions
β Scribed by T. Reith; W.J. Beek
- Publisher
- Elsevier Science
- Year
- 1973
- Tongue
- English
- Weight
- 747 KB
- Volume
- 28
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
In this paper new experimental work on the kinetics of the absorption of oxygen in an aqueous solution of sodium sulphite with cobaltous sulphate as a catalyst, has been presented and compared with already published data. It is shown that the reaction of oxygen with sodium sulphite is zero order in sulphite, lirst order in cobalt and second order in oxygen for 2 X lo4 N/m* < p o,< 10" N/m*, 15Β°C < T < fXl"C, 3 X lo+ kmol/m3 < cCo++ < 3 x 10e3 kmol/m 750 < pH < 8.50 and 0.4 kmol/m3 < csos__ < O-8 kmol/m3.
The reaction rate constant can be varied by more than two decades by changing the cobalt concentration, pH and temperature.
The specific interfacial areas, a, and mass transfer coefficients, k,,, measured by DeWaal and Beek 114,151 using an incorrect kinetic model of this reaction, are reinterpreted with the results of the present kinetic investigation. It is shown that their values of a and k,, are a factor 2.2 too low and too high, respectively, but that their values of k,a are correct.
π SIMILAR VOLUMES
PI 131 [41 LEHRER I. H., Gas holdup in sparged vessels, Ind. Engng. Chem. Research Results Service MS69-469. GEHAN K. and LEHRER I. H., On heat and mass transfer to deformable particles at high Reynolds numbers, Ind. Engng. Chem. Research Results Services MS69-628. Interfacial area in sparged vessel
The rate of reaction of dissolved oxygen and sulphite ions in diluted aqueous solutions, which has industrial importance in abatement of air pollution by sulphur dioxide, was investigated in homogeneous and in heterogeneous systems. Cobaltous sulphate was used as a catalyst. The rate of sulphite ox
## DE WAAL et al.[l] have measured the absorption rate of oxygen into sodium sulphite solutions in a packed column (I ft i.d., IOft high, I in Raschig rings), and have determined the interfacial areas and the mass transfer coefficient in the liquid in terms of the surface renewal rate. However, th