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Sour water stripping project, Committee on Refinery Environmental Control, American Petroleum Inst

Book ·
OSTI ID:7301406
(Purpose in stripping refinery sour waters is to keep sulfides and NH/sub 3/ out of the wastewater.) Synthetic sour water containing only H/sub 2/S and NH/sub 3/ can be readily stripped if precautions are taken to prevent oxidation of sulfide. Addition of phenols and cyanide did not interfere with NH/sub 3/ or H/sub 2/S removal. Real sour waters behave differently from the synthetic solutions, owing to acidic impurities which hold some NH/sub 3/ as ammonium ions. A full-scale stripper with 10 valve trays removed NH/sub 3/ to the same extent as a small-scale stripper with 5 trays. Van Krevelen (VK) equilibrium data gave estimated tray efficiencies of 65 percent and 90-100 percent for these two strippers. NH/sub 3/ and H/sub 2/S contents in the reflux condensate calculated using VK data were 2 to 4 times greater than measurements. The VK equilibrium data can be used to design sour water strippers with no caustic addition if the amount of ''fixed'' NH/sub 3/ is subtracted from the feed and added to the bottoms. Disposal of the overhead gas is discussed. A number of useful ideas based on experience with sour water systems in refineries are identified. (DLC)
OSTI ID:
7301406
Country of Publication:
United States
Language:
English