The manufacture method of sodium hypochlorite aqueous solution
A technology of sodium hypochlorite and its manufacturing method, which is applied in the direction of hypochlorous acid, hypochlorite, chemical instruments and methods, etc., which can solve the problems of increased decomposition, deterioration of consumed resources, etc., and achieve the effect of high yield
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Embodiment 1
[0084] To those equipped with agitator, coil cooler and external circulation type cooler figure 1 The reaction tank shown, using the figure 2 For the stirring blade shown, the power required for stirring per unit volume is 0.41kW / m 3 And while stirring under the condition that the ratio (Np / Nq) of the required power number Np and the circulation flow number Nq is 2.5, supply 45% by mass of sodium hydroxide aqueous solution as a raw material with 1491kg / hour, this hydroxide The sodium aqueous solution was maintained at 30° C., and chlorine gas was introduced at 560 kg / hour to perform a chlorination reaction so that the average residence time was about 100 minutes. Furthermore, the power P=2.22kW required for stirring, the density ρ=1500kg / m of the reaction solution 3 , rotation speed n=1.30rps, stirring blade diameter d=0.67m, total circulation flow q=0.351m 3 / s, so by Np≡P / (ρn 3 d 5 ) and Nq≡q / (nd 3 ) to calculate Np=5 and Nq=2.
[0085] Then, extract 2051kg / hour reac...
Embodiment 2
[0088] To those equipped with agitator, coil cooler and external circulation type cooler figure 1 The reaction tank shown, using the image 3 For the stirring blade shown, the power required for stirring per unit volume is 0.41kW / m 3 And Np / Nq is 7.1 conditions while stirring, with 1442kg / hour supply 45 mass % sodium hydroxide aqueous solution as raw material, this sodium hydroxide aqueous solution is maintained at 30 ℃, and introduce chlorine gas with 552kg / hour, make the average The chlorination reaction proceeded so that the residence time became about 100 minutes. Furthermore, the power P=2.22kW required for stirring, the density ρ=1500kg / m of the reaction solution 3 , rotation speed n=1.30rps, stirring blade diameter d=0.67m, total circulation flow q=0.27m 3 / s, so by Np≡P / (ρn 3 d 5 ) and Nq≡q / (nd 3 ) to calculate Np=5 and Nq=0.7.
[0089] Next, extract 2018kg / hour reactant slurry from reaction tank, carry out solid-liquid separation with centrifuge, thus obtain...
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