Sodium Chlorate → Sodium;chloric acid;chlorate

참여 물질

반응 단계

Table 10 shows the net average overall throughput rates and concentrations of products obtained in this experiment. Slightly diluted purified sulfuric acid from the GAP system of Example 1 (173 g/L H2SO4 and 22 g/L Na2SO4) was fed to the DCU component (sodium form) of the DPU at a feed rate of 2.5 L/h thereby converting the DCU to the hydrogen form and producing a sodium sulfate-rich regeneration product (64 g/L Na2SO4 and 8 g/L H2SO4 with 8 g/L residual NaClO3) at 2.7 L/h. In a subsequent step, a concentrated sodium chlorate solution (669 g/L NaClO3) was fed to the DCU component (hydrogen form) of the DPU at 1.2 L/h thereby producing a sodium chlorate/chloric acid mixture (260 g/L NaClO3 and 140 g/L HClO3) at a rate of 1.7 L/h. The IT obtained was 1.21.

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