Process for controlling the flow of titanium bearing material into the fluidized bed reactor in the manufacture of titanium tetrachloride

1. A process for controlling chlorination reactions in manufacturing titanium tetrachloride in a fluidized bed reactor, optionally followed by processing to form a titanium product comprising an amount of silica, the process comprising:

(a) feeding carbonaceous material, titanium bearing material comprising an amount of silica, and chlorine to the fluidized bed reactor to form a gaseous stream, and condensing the gaseous stream to form titanium tetrachloride, a non-condensed gas stream and a condensable product stream, wherein at least one of the titanium tetrachloride and the non-condensed gas stream comprise silicon tetrachloride;

(b) analyzing the non-condensed gas stream, the titanium tetrachloride or both, to determine the analyzed concentration of silicon tetrachloride;

(c) identifying a set point concentration of silicon tetrachloride based on the desired amount of silica in the titanium product;

(d) calculating the difference between the analyzed concentration of silicon tetrachloride and the set point concentration of silicon tetrachloride; and

(e) generating a signal which corresponds to the difference calculated in step (d) which provides a feedback response that controls the flow of the titanium bearing material into the fluidized bed reactor.

2. The process of claim 1 wherein the analyzed concentration of silicon tetrachloride is greater than the set point concentration of silicon tetrachloride.

3. The process of claim 1 wherein the analyzed concentration of silicon tetrachloride is less than the set point concentration of silicon tetrachloride.

4. The process of claim 2 wherein the analyzed concentration of silicon tetrachloride is greater than the set point concentration of silicon tetrachloride and the feedback response comprises increasing the amount of titanium bearing material being introduced into the fluidized bed reactor.

5. The process of claim 3 wherein the analyzed concentration of silicon tetrachloride is less than the set point concentration of silicon tetrachloride and the feedback response comprises decreasing the amount of titanium bearing material being introduced into the fluidized bed reactor.

6. The process of claim 1 wherein the analyzed concentration of silicon tetrachloride is determined by analyzing the non-condensed gas stream.

7. The process of claim 1 wherein the analyzed concentration of silicon tetrachloride is determined by analyzing the titanium tetrachloride.

8. The process of claim 1 wherein analyzing the non-condensed gas stream is achieved by spectroscopy, spectrometry or chromatography.

9. The process of claim 8 wherein analyzing the non-condensed gas stream is by infrared spectroscopy.

10. The process of claim 1 wherein the silicon tetrachloride is present in the non-condensed gas stream in the amount of about 0 to about 0.3 mole %, based on the total weight of the analyzed stream.

11. The process of claim 10 wherein the silicon tetrachloride is present in the non-condensed gas stream in the amount of about 0.01 to about 0.1 mole %, based on the total weight of the analyzed stream.

12. The process of claim 11 wherein the silicon tetrachloride is present in the non-condensed gas stream in the amount of about 0.01 to about 0.05 mole %, based on the total weight of the analyzed stream.

13. The process of claim 1 wherein the set point of silicon tetrachloride is about 0.01 to about 0.25 mole %.

14. The process of claim 1 wherein the signal is electrical, pneumatic, digital or manual.

15. The process of claim 1 wherein the feedback response is provided by a feedback controller selected from the group consisting of a proportional, a proportional integral action controller, a proportional integral derivative action controller; or suitable computer software or algorithm that provides a feedback response to a control device.