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U.S. Department of Energy
Office of Scientific and Technical Information

Purification of coke oven gas with production of sulfuric acid and ammonium sulfate. [11 claims]

Patent ·
OSTI ID:7329408
A continuous process is provided which has the primary purpose of removing NH/sub 3/, H/sub 2/S, HCN, and (CN)/sub 2/ from the subject gas mixtures and the secondary purpose of producing (NH/sub 4/)/sub 2/SO/sub 4/ and iron oxide for industrial uses. The gas mixture which contains tar and other condensible vapors, NH/sub 3/, H/sub 2/S, HCN, and (CN)/sub 2/ together with small volumes of gas from the ammonia still of the system, and gas from a system H/sub 2/SO/sub 4/ plant, is contacted in a single three-stage reaction chamber in the presence, if need be, of a tar solvent, additional NH/sub 3/, and the reagent Fe(OH)/sub 2/, which itself is a product of a concurrent reaction between NH/sub 3/ and FeSO/sub 4/. The unpurified gas mixture's condensible vapors are largely prevented from condensing by maintaining a steady, elevated temperature, while the mixture is essentially freed of HCN, (CN)/sub 2/, NH/sub 3/, and H/sub 2/S in the reactor before the gas mixture passes through a primary gas cooler. The gas then passes through a benzene, toluene, and xylene absorber before being pressurized and distributed. The spent reaction chamber reagent is separated to produce tar and solvent; (NH/sub 4/)/sub 2/SO/sub 4/, solution, and iron precipitates. Sulfur dioxide released by the iron oxide production process is used to produce H/sub 2/SO/sub 4/, which in turn is either reacted with scrap iron, or used in a metal pickling operation to produce FeSO/sub 4/ for use in preparation of thereaction chamber reagent. 11 claims, 1 figure.
Assignee:
TIC; EDB-77-059025; ERA-02-028259
Patent Number(s):
US 3993730
OSTI ID:
7329408
Country of Publication:
United States
Language:
English