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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[0036] Example 1
[0037] (1) Reductive decomposition of titanium white waste residue and green vitriol and treatment of higher concentration of waste sulfuric acid
[0038] Add titanium dioxide waste residue and green vitriol into a rotary kiln or continuous wok reactor, and dry it at 120℃ for 60 minutes under nitrogen and argon atmosphere to remove the crystal water in the titanium dioxide waste residue, and control the total temperature and time by adjusting the drying temperature and time. Water is divided into 5%, the flue gas is emptied after dust removal and purification, and the dried material enters the next step of reaction;
[0039] Use sulfur in nitrogen and oxygen to reduce and decompose the anhydrous titanium dioxide waste into FeO residue and SO at a temperature of 500℃ 2 gas. Use SO 2 The sulfuric acid produced by the gas is returned to the acid hydrolysis process in the titanium dioxide production process. The decomposed FeO residue directly neutralizes the 10% was...
Example Embodiment
[0044] Example 2
[0045] (1) Reductive decomposition of titanium white waste residue and green vitriol and treatment of higher concentration of waste sulfuric acid
[0046] Add titanium dioxide waste residue and green vitriol into a rotary kiln or continuous wok reactor, and dry it at 400℃ for 5 minutes under nitrogen and argon atmosphere to remove the crystal water in the titanium dioxide waste residue. Control the total drying temperature and time by adjusting the drying temperature and time. Water is divided into 5%, the flue gas is emptied after dust removal and purification, and the dried material enters the next reaction;
[0047] Use high-sulfur coal in carbon dioxide and oxygen to reduce and decompose anhydrous titanium dioxide waste residue into FeO residue and SO at a temperature of 1000℃ 2 gas. Use SO 2 The sulfuric acid produced by the gas is returned to the acid hydrolysis process in the titanium dioxide production process. The decomposed FeO residue directly neutrali...
Example Embodiment
[0052] Example 3
[0053] (1) Reductive decomposition of titanium white waste residue and green vitriol and treatment of higher concentration of waste sulfuric acid
[0054] Put the titanium white waste slag green vitriol into the rotary kiln or continuous wok reactor, and dry it at 300℃ for 30 minutes under nitrogen and argon atmosphere to remove the crystal water in the titanium white waste slag, and control the total drying temperature and time by adjusting the drying temperature and time. The water content is 2.5%, the flue gas is emptied after dust removal and purification, and the dried material enters the next reaction;
[0055] Use sulfur in nitrogen and oxygen to reduce and decompose anhydrous titanium dioxide waste into FeO residue and SO at a temperature of 800°C 2 gas. Use SO 2 The sulfuric acid produced by the gas is returned to the acid hydrolysis process in the titanium dioxide production process. The decomposed FeO residue directly neutralizes the 20% waste H genera...
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