Method for removing free chlorine in dilute sulfuric acid
A technology of dilute sulfuric acid and free chlorine, which is applied in the chemical industry and can solve the problems of high equipment material requirements, strong corrosion, and inability to meet the requirements of chlorine gas drying.
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Embodiment 1
[0022] A method for removing free chlorine in dilute sulfuric acid, comprising the following steps:
[0023] (1), 8m of dilute sulfuric acid from the chlor-alkali-chlor-hydrogen drying section 3 / h, pumped into the upper part of the dechlorination circulation tower for spraying or pumped into the dilute sulfuric acid storage tank and then injected into the upper part of the dechlorination circulation tower for spraying, 2m from the compressed air entering the lower part of the dechlorination circulation tower 3 / h Reverse contact to remove chlorine gas, the removed chlorine gas enters the absorption tower, and is absorbed by caustic soda to generate sodium hypochlorite;
[0024] (2), dilute sulfuric acid 11m after dechlorination in step (1) 3 , wherein the content of free chlorine is about 20Kg, pumped into the filter circulation tank, and the dechlorination agent Na is added in the filter circulation tank 2 SO 3 28Kg, and continuously circulate dilute sulfuric acid for 10 ...
Embodiment 2
[0026] A method for removing free chlorine in dilute sulfuric acid, comprising the following steps:
[0027] (1), 8m of dilute sulfuric acid from the chlor-alkali-chlor-hydrogen drying section 3 / h, pump into the upper part of the dechlorination circulation tower for spraying or pump into the dilute sulfuric acid storage tank and then pour into the upper part of the dechlorination circulation tower for spraying, and enter the dry nitrogen 2m from the lower part of the dechlorination circulation tower 3 / h Reverse contact to remove chlorine gas, the removed chlorine gas enters the absorption tower, and is absorbed by caustic soda to generate sodium hypochlorite;
[0028] (2), dilute sulfuric acid 11m after dechlorination in step (1) 3 , wherein the content of free chlorine is about 20Kg, pumped into the filter circulation tank, and the dechlorination agent Na is added in the filter circulation tank 2 SO 3 35Kg, and continuously circulate dilute sulfuric acid for 10 to 20 cyc...
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