343results about "Titanium tetrachloride" patented technology

The invention discloses a method for producing titanium tetrachloride by using a low grade titanium material, and belongs to the chemical technical field. The technical problem to be solved is to provide a method for producing titanium tetrachloride by using the low grade titanium material in continuous industrialized production. The method is characterized in that the low grade titanium material containing a certain proportion of titanium carbide is adopted to directly react with chlorine at the temperature of 600 DEG C to 700 DEG C to produce titanium tetrachloride. Long period continuous stable operation can be kept by using the technological parameters of the invention, and chlorination rate of titanium carbide in titanium material reaches above 90 percent, so that the titanium can be better used for producing titanium tetrachloride.

There are provided processes for treating red mud. For example, the processes can comprise leaching red mud with HCl so as to obtain a leachate comprising ions of a first metal (for example aluminum) and a solid, and separating said solid from said leachate. Several other metals can be extracted from the leachate (Fe, Ni, Co, Mg, rare earth elements, rare metals, etc.). Various other components can be extracted from solid such as TiO2, SiO2 etc.

The disclosure is directed to a process for isolating solids from a purification purge stream comprising an impurity present as a solid, wherein the purification purge stream is substantially free of chlorides other than titanium tetrachloride and vanadium chloride, the process comprising the steps of: (a) atomizing the purification purge stream comprising titanium tetrachloride as a liquid and an impurity present as a solid; (b) drying solids in the atomized purification purge stream by contacting the atomized stream with a titanium tetrachloride vapor stream such that the combined streams reach a temperature of at least about 140° C. to vaporize the liquid titanium tetrachloride, wherein the titanium tetrachloride vapor is substantially free of chlorides other than those of titanium and vanadium, and substantially free of non-condensable gases comprising CO, CO2, N2, or mixtures thereof; and (c) separating the impurity present as a solid from the vaporized titanium tetrachloride. The separated vanadium solids may be further processed to recover valuable by products.

A method for separating one or more titanium (halo) alkoxides from a liquid mixture comprising titanium tetrachloride TiCl4 and at least one titanium (halo) alkoxide, said method comprising: agitatingand cooling the liquid mixture until crystallization of at least one titanium (halo) alkoxide occurs in the liquid mixture; separating the crystallized titanium (halo) alkoxide from the mixture; andoptionally, washing the separated, crystallized titanium (halo) alkoxide with a solvent.

The cost-effective hydrogenated, purified titanium powder is manufactured by the semi-continuous process including: (a) magnesium-thermic reduction of titanium chlorides at 830-880° C. in the hydrogen atmosphere characterized by the formation of a hollow porous block of the reaction mass having an open cavity in the center of the block, (b) full thermal-vacuum separation of the hollow block from excessive Mg and MgCl2 at 850-980° C. and residual pressure of 26-266 Pa using a multi-step cycle including: (i) purging hydrogen at 800-950° C. into the reactor at the pressure 10 kPa to 24.5 kPa, (ii) directive squeezing-out of a separated liquid phase containing magnesium and magnesium chloride into an additional vessel, and (iii) application of alternate pressure to small portions of the liquid phase in porous titanium compound from different sides which provides removal of the liquid from small pores of the titanium compound and fast evaporation of said liquid, (c) simultaneous hydrogenation and cooling of the titanium sponge down to 600° C. by purging cold hydrogen using multiple recirculation of hydrogen, (d) holding the hydrogenated porous titanium compound in the hydrogen atmosphere at 450-600° C. for 20-70 minutes, (e) removing the hydrogenated porous titanium compound from the reactor, and (f) crushing and grinding the crushed hydrogenated porous titanium pieces into the powder having a predetermined particle size.

There are provided processes for treating red mud. For example, the processes can comprise leaching red mud with HCl so as to obtain a leachate comprising ions of a first metal (for example aluminum) and a solid, and separating said solid from said leachate. Several other metals can be extracted from the leachate (Fe, Ni, Co, Mg, rare earth elements, rare metals, etc.). Various other components can be extracted from solid such as TiO2, SiO2 etc.