Kerr-mcgee Chemical, LLC

John C Magyar

William A Yuill

Alan J Morris

R Gerald McDill

Eugene R Adams

Glenn D Wootten

A process for reacting titanium tetrachloride vapors with oxygen to produce titanium dioxide wherein the oxygen is introduced into the reactor in at least two points. The process has the ability to control properties, such as particle size, of the raw pigment produced. The temperature of the oxygen introduced to the reactor at the further inlet point is above, below, or at the same temperature of the oxygen introduced at the first inlet point. The further inlet point can be located before or after the all the titanium tetrachloride has been introduced into the reactor. The titanium tetrachloride is introduced at a relatively low temperature, below about 427&#xb0; C., and the reaction temperature in the reactor is at least about 700&#xb0; C. The process includes the use of an auxiliary fuel such as carbon monoxide, methane, propane, butane, pentane, hexane, benzene, xylene, toluene, or combinations thereof for increasing the temperature in the reactor. Still further, the process for producing titanium dioxide provides for the addition of aluminum chloride to the reactor. Advantageously, the process allows the pressure in the reactor to be above atmospheric pressure and range between about 0.15 MPa and 4.0 MPa above atmospheric pressure during the production of titanium dioxide. A reactor is also provided with an aluminum chloride generator for heating the titanium tetrachloride and delivering aluminum chloride to the reactor.

Method and apparatus for producing titanium dioxide

A process for reacting titanium tetrachloride vapors with oxygen to produce titanium dioxide wherein the oxygen is introduced into the reactor in at least two points. The process has the ability to control properties, such as particle size, of the raw pigment produced. The temperature of the oxygen introduced to the reactor at the further inlet point is above, below, or at the same temperature of the oxygen introduced at the first inlet point. The further inlet point can be located before or after the all the titanium tetrachloride has been introduced into the reactor. The titanium tetrachloride is introduced at a relatively low temperature, below about 427&deg; C., and the reaction temperature in the reactor is at least about 700&deg; C. The process includes the use of an auxilary fuel such as carbon monoxide, methane, propane, butane, pentane, hexane, benzene, xylene, toluene, or combinations thereof for increasing the temperature in the reactor. Still further, the process for producing titanium dioxide provides for the addition of aluminum chloride to the reactor. Advantageously, the process allows the pressure in the reactor to be above atmospheric pressure and range between about 0.15 MPa and 4.0 MPa above atmospheric pressure during the production of titanium dioxide. A reactor is also provided with an aluminum chloride generator for heating the titanium tetrachloride and delivering aluminum chloride to the reactor.

An improved method for preparing a rutile titanium dioxide pigment of uniform particle size wherein the pigment is formed by reaction of a mixture of an oxidizing gas and a titanium halide in the vapor phase at elevated temperatures in the presence of a metal ion containing compound. The improvement comprises introducing the metal ion containing compound into a vapor phase oxidation reactor containing the reacting mixture in at least two separate and discrete increments. The first increment is introduced into the reactor at a point prior to reaction of said mixture having occurred while the second increment is introduced into the reactor at a point wherein at least 20 weight percent of the total titanium halide reactant has been converted to the desired titanium dioxide pigment.

Process for preparing titanium dioxide

A system for protecting glass structures in a combustion zone wherein heat refractory material is applied to the glass structure. The applied heat refractory material substantially is opaque and non-reflective to visible light and also is resistant to degradation at temperatures of up to about 2500 degrees farenheit. The heat refractory material acting to absorb radiant energy and to inhibit the devitrification of glass structures maintained at temperatures elevated to about 1000 degrees centigrade for extended periods of time.

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Ackerman, MS, United States of America

John C Magyar