Regeneration method for sulphureous alkali residues
A technology of alkali residue and lye, applied in the preparation/purification of sulfur, the removal of alkali metal hydroxide, solid waste, etc. Dealing with device adverse effects, etc.
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Embodiment 1
[0042] A certain alkali washing liquid hydrocarbon alkali residue wastewater, in which COD is 1.27×10 5 mg / L, the sulfide is 1.08×10 4 mg / L, volatile phenol 1.99×10 4 mg / L. Use the inventive method to process, introduce the SO contained in the Claus plant 2 Gas, that is, the raw material gas in the Claus unit, is introduced at the same time as the exhaust gas from the SCOT unit of the Claus unit’s tail gas treatment unit to acidify the alkali slag wastewater. By adjusting the ratio of the gas introduced, the volume content of hydrogen sulfide in the exhaust gas to 50%, the acidification is carried out until the pH of the alkali slag wastewater drops to 3, and the SO 2 Gas, continue to pass the exhaust gas of the SCOT device for 10 minutes.
[0043] After the acidification, the oil phase (mainly phenol) separated from the water layer was recovered by standing still. After the above acidification treatment, more than 99% of sulfides are removed, more than 80% of phenols are...
Embodiment 2
[0046] A liquid hydrocarbon and gasoline mixed alkali residue wastewater, in which COD is 1.25×10 5 mg / L, sulfide is 1.78×10 4 mg / L, volatile phenol 7.17×10 4 mg / L. Use the inventive method to process, introduce the SO contained in the Claus plant 2 Gas, that is, the raw material gas in the Claus unit, is introduced at the same time as the exhaust gas from the SCOT unit of the Claus unit’s tail gas treatment unit to acidify the alkali slag wastewater. By adjusting the ratio of the gas introduced, the volume content of hydrogen sulfide in the exhaust gas to 65%, the acidification is carried out until the pH of the alkali slag wastewater drops to 4, and the SO 2 Gas, continue to pass the exhaust gas of the SCOT device for 20 minutes.
[0047] After the acidification, the oil phase (mainly phenol) separated from the water layer was recovered by standing still. After the above acidification treatment, more than 98% of sulfides are removed, more than 80% of phenols are removed...
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