Titanium bearing material flow control in the manufacture of titanium tetrachloride with silica content monitoring of the titanium product
View Patent ↗This disclosure relates to a process for controlling chlorination reactions in manufacturing titanium tetrachloride in a fluidized bed reactor, 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; (b) processing the titanium tetrachloride to form a titanium product comprising an amount of silica; (c) analyzing the titanium product comprising an amount of silica to determine the analyzed concentration of silica; (d) identifying a set point concentration of silica; (e) calculating the difference between the analyzed concentration of silica and the set point concentration of silica; and (f) generating a signal which corresponds to the difference calculated in step (e) which provides a feedback response that controls the flow of the titanium bearing material into the fluidized bed reactor.
1. A process for controlling chlorination reactions in manufacturing titanium tetrachloride in a fluidized bed reactor, 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;
(b) processing the titanium tetrachloride to form a titanium product comprising an amount of silica;
(c) analyzing the titanium product comprising an amount of silica to determine the analyzed concentration of silica;
(d) identifying a set point concentration of silica;
(e) calculating the difference between the analyzed concentration of silica and the set point concentration of silica; and
(f) generating a signal which corresponds to the difference calculated in step (e) 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 silica is greater than the set point concentration of silica.
3. The process of claim 1 wherein the analyzed concentration of silica is less than the set point concentration of silica.
4. The process of claim 2 wherein the analyzed concentration of silica is greater than the set point concentration of silica 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 silica is less than the set point concentration of silica 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 silica is determined by analyzing the titanium product.
7. The process of claim 1 wherein analyzing the titanium product is achieved by spectroscopy, spectrometry or chromatography.
8. The process of claim 7 wherein analyzing the titanium product is by XRF spectroscopy.
9. The process of claim 1 wherein the silica is present in the titanium product in the amount of about 0 to about 0.3 weight %, based on the total weight of the titanium product.
10. The process of claim 1 wherein the silica is present in the titanium product in the amount of about 0.0 to about 0.1 weight %, based on the total weight of the titanium product.
11. The process of claim 1 wherein the silica is present in the titanium product in the amount of about 0.01 to about 0.06 weight %, based on the total weight of the titanium product.
12. The process of claim 1 wherein the desired concentration of silica is about 0.01 to about 0.3 mole %.
13. The process of claim 1 wherein the signal is electrical, pneumatic, digital or manual.
14. The process of claim 1 wherein the feedback response is provided by a feedback controller selected from the group consisting of a proportional action controller, 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.