Method for recovering and utilizing three wastes during titanium white production through sulfuric acid process
A technology of titanium dioxide and sulfuric acid method, which is applied in the direction of sulfur trioxide/sulfuric acid, calcium/strontium/barium sulfate, ferrous oxide, etc., which can solve the problems of polluting groundwater resources and surface vegetation, secondary pollution of the ecological environment, violations, etc. , to reduce the reduction and decomposition temperature, eliminate environmental pollution, and shorten the production cycle
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Embodiment 1
[0037] (1) Reduction decomposition of titanium dioxide waste slag green vitriol and treatment of higher concentration waste sulfuric acid
[0038]Add the green vitriol of the titanium dioxide waste slag into the rotary kiln or continuous frying pan reactor, and dry it at a temperature of 120°C for 60 minutes under the atmosphere of nitrogen and argon to remove the crystal water in the titanium dioxide waste slag, and control the total drying time by adjusting the drying temperature and time. The water content is 5%, the flue gas is emptied after dust removal and purification, and the dry material enters the next step of reaction;
[0039] Use sulfur in nitrogen and oxygen to decompose anhydrous titanium dioxide residue into FeO residue and SO at a temperature of 500°C 2 gas. use SO 2 The sulfuric acid produced from the gas is returned to the acid hydrolysis process in the titanium dioxide production process. The decomposed FeO residue directly neutralizes 10% of waste H gen...
Embodiment 2
[0045] (1) Reduction and decomposition of titanium dioxide waste slag green vitriol and treatment of higher concentration waste sulfuric acid
[0046] Put the waste titanium dioxide slag green vitriol into the rotary kiln or continuous frying pan reactor, and dry it at 400°C for 5 minutes under the atmosphere of nitrogen and argon to remove the crystal water in the waste titanium dioxide, and control the total drying time by adjusting the drying temperature and time. The water content is 5%, the flue gas is emptied after dust removal and purification, and the dry material enters the next step of reaction;
[0047] Use high-sulfur coal to reduce and decompose anhydrous titanium dioxide residue into FeO residue and SO at a temperature of 1000°C in carbon dioxide and oxygen 2 gas. use SO 2 The sulfuric acid produced from the gas is returned to the acid hydrolysis process in the titanium dioxide production process. The decomposed FeO residue directly neutralizes 25% of the wast...
Embodiment 3
[0053] (1) Reduction and decomposition of titanium dioxide waste slag green vitriol and treatment of higher concentration waste sulfuric acid
[0054] Add the green vitriol of the titanium dioxide waste slag into a rotary kiln or a continuous frying pan reactor, and dry it at a temperature of 300°C for 30 minutes in an atmosphere of nitrogen and argon to remove the crystal water in the titanium dioxide waste slag, and control the total drying time by adjusting the drying temperature and time. The moisture content is 2.5%, the flue gas is emptied after dust removal and purification, and the dry material enters the next step of reaction;
[0055] Use sulfur in nitrogen and oxygen to decompose anhydrous titanium dioxide residue into FeO residue and SO at a temperature of 800°C 2 gas. use SO 2 The sulfuric acid produced from the gas is returned to the acid hydrolysis process in the titanium dioxide production process. The decomposed FeO residue directly neutralizes 20% of the w...
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