Method for producing titanium products

By stabilizing chlorination temperatures and controlling impurity levels through specific ratio adjustments and pulp return methods, the method enhances the quality of sponge titanium production by reducing impurities in technical titanium tetrachloride.

WO2026111713A1PCT designated stage Publication Date: 2026-05-28LLC RESEARCH & DESIGN TITANIUM INSTITUTE
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Patent Information

Authority / Receiving Office
WO · WO
Patent Type
Applications
Current Assignee / Owner
LLC RESEARCH & DESIGN TITANIUM INSTITUTE
Filing Date
2025-10-27
Publication Date
2026-05-28
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Abstract

Method for producing titanium products, comprising the preparation of a titanium-containing charge for chlorination, said charge containing titanium slag, a carbon-containing reducing agent, and sodium chloride; chlorination of the charge with gaseous chlorine in a chlorinator in a molten chloride salt medium, while maintaining the molar ratio of impurity-binding metals (Fe, Mg, Al) to the resulting chlorides of iron, magnesium, and aluminum at 2, 1-2,8, and the mass ratio between carbon and titanium dioxide in the molten chloride salts at 0,15-5,0, at a melt temperature of 710 °C to 800 °C, thereby obtaining a vapor-gas mixture which is purified from sublimated by-product chlorides to yield technical-grade titanium tetrachloride and pulp, purification of the technical titanium tetrachloride from impurities in columns, resulting in purified titanium tetrachloride and the separation of impurities in the form of a low-boiling distillate and a column bottoms residue, magnesiothermic reduction of the purified titanium tetrachloride in a reduction reactor using magnesium, to obtain a reaction mass and molten recyclable magnesium chloride, vacuum separation of the reaction mass in a vacuum separation unit, yielding sponge titanium blocks and magnesium condensate, whereby the pulp obtained from the purification of the vapor-gas mixture is returned to the chlorinator in two streams: one stream is supplied to the surface of the melt, and the other is sprayed into the subroof space of the chlorinator, thereby maintaining the temperature of the vapor-gas mixture in the subroof space of the chlorinator between 300 °C and 650 °C, while adjusting the ratio of the total pulp flow rate to the gaseous chlorine flow rate from 2:1 to 4: 1. Technical result: reducing the amount of impurities in technical titanium tetrachloride and improving the quality of the sponge titanium obtained as a result of its subsequent processing.
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