1962
DOI: 10.1016/0009-2509(62)85010-6
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The absorption of oxygen into sodium sulphite solution

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1964
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Cited by 42 publications
(16 citation statements)
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“…Equation (11) predicts orders with respect to S0 3 2 " and H + in agreement with those observed in many experimental studies ( Table 1). The halforder dependence on 0 2 has not been observed in any of the studies of the uncatalysed oxidation of sulphite, while a first-order dependence on 0 2 concentration has been noted in some studies at particular experimental conditions (6,18). The [M*]2 dependence has not been specifically reported in any of the kinetic experiments, however the observed variation in the oxidation rate with water quality may be due to the effect of metal ion impurities ( Table 2).…”
Section: Mechanismmentioning
confidence: 79%
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“…Equation (11) predicts orders with respect to S0 3 2 " and H + in agreement with those observed in many experimental studies ( Table 1). The halforder dependence on 0 2 has not been observed in any of the studies of the uncatalysed oxidation of sulphite, while a first-order dependence on 0 2 concentration has been noted in some studies at particular experimental conditions (6,18). The [M*]2 dependence has not been specifically reported in any of the kinetic experiments, however the observed variation in the oxidation rate with water quality may be due to the effect of metal ion impurities ( Table 2).…”
Section: Mechanismmentioning
confidence: 79%
“…However, Yagi and Inoue (6) observed that the rate was first-order in 0 2 concentration at pH 8 to 9, while Larson et al (18) report an oxygen dependence at higher pH (> 9.5). O'Brien and Birkner (17) report an 0 2 dependence for the reaction, however they did not study sulphite oxidation directly but inferred the rate law from experiments into sulphide oxidation.…”
Section: Kineticsmentioning
confidence: 95%
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“…The first set of experiments was carried out to study the reaction rate as a function of HSO 3 Ϫ concentration at the temperature of 45°C and a fixed Co 2ϩ concentration ͑c Co 2ϩ ϭ 1 mol m Ϫ3 ). The second set includes experimental runs carried out at three different temperature levels (25,45, and 55°C) by varying catalyst concentration at fixed SO 2 and Ca(OH) 2 levels in feed solution. The third experimental set was carried out in the simultaneous presence of the two catalysts at the temperature of 45°C.…”
Section: Resultsmentioning
confidence: 99%
“…The kinetics of these reactions (in particular, of oxygen absorption by solutions of calcium bisulfite) in the absence 2,3 and in presence 4 -6 of catalysts has been of great interest during the last 5 decades. The main engineering uses of sulfite (SO 3 2Ϫ ) oxidation are the determination of the interfacial area or the volumetric mass transfer constant in gas-liquid contactors and, recently, the oxidation of calcium sulfite waste products in FGD.…”
Section: Introductionmentioning
confidence: 99%