Process for extracting titanium values from titaniferous bearing material

Claim 2

A process of extracting titanium values from titaniferous bearing material, which comprises: (1) preparing a reaction mixture containing a titaniferous bearing material in an amount between about 10% and about 400% above the stoichiometric amount of titaniferous bearing material necessary to react with sulfuric acid to provide titanyl sulfate, and a dilute sulfuric acid solution having a concentration between about 25% and about 60% by weight; (2) maintaining the temperature of the reaction mixture below about 140° C. in the reaction vessel; (3) extracting the titanium values by circulating the reaction mixture in an agitation column located within the reaction vessel in a direction countercurrent to the flow of the reaction mixture in the annular space located between the agitation column and the inner vessel wall, said circulation being done in a manner to maintain the titaniferous bearing material in a continuous turbulent suspension flow in the agitation column; (4) cooling the resulting reaction mixture to a temperature below about 110° C. without precipitating the reaction mixture; and (5) discharging the reaction mixture from the reaction vessel and recovering the extracted titanium values.

Claim 3

The process in claim 1 wherein agitation is conducted by introducing a stream of gas under pressure into the lower part of the agitation column located within the reaction vessel at a sufficient velocity flow to form a continuously rising turbulent suspension of gas bubbles and reaction mixture, discharging from the upper part of the agitation column the reaction mixture which is then returned to the lower part of the agitation column in the annular space between the agitation column and the inner reaction vessel wall.

Claim 4

The process in claim 1 wherein agitation is conducted by an impeller agitator within the agitation column.

Claim 5

The process in claim 1 wherein a suitable reductant is added to the reaction mixture to reduce ferric sulfate values to ferrous sulfate, said reductant being added in at least stoichiometric amounts to the quantity of ferric iron present.

Claim 6

A continuous process of extracting titanium values from titaniferous bearing material, which comprise: (1) continuously reacting a titaniferous bearing material in an amount between about 10% and about 400% above the stoichiometric amount of material necessary to react with sulfuric acid to provide titanyl sulphate, and a dilute sulfuric acid solution having a concentration between about 25% and about 60% by weight; (2) maintaining the reaction mixture at a temperature below about 140° C. in the reaction vessel; (3) extracting the titanium values by circulating the reaction mixture through an agitation column located within the reaction vessel in a direction countercurrent to the flow of the reaction mixture in the annular space located between the agitation column and the inner reaction vessel wall, said circulation being done in a manner to maintain the titaniferous bearing material in a continuous turbulant suspension flow in the agitation column; (4) cooling the resulting reaction mixture to a temperature below about 110° C. without precipitating the reaction mixture, and (5) continuously discharging the reaction mixture from the reaction vessel and recovering extracted titanium values.

Claim 7

A continuous process of extracting titanium values from titaniferous bearing material, which comprise: (1) continuously reacting a titaniferous bearing material in an amount between about 10% and about 400% above the stoichiometric amount of material necessary to react with sulfuric acid to provide titanyl sulphate, and a dilute sulfuric acid solution having a concentration between about 25% and about 60% by weight; (2) maintaining the reaction mixture at a temperature below about 140° C. in the reaction vessel; (3) extracting the titanium values by circulating the reaction mixture through an agitation column located within the reaction vessel in a direction countercurrent to the flow of the reaction mixture in the annular space located between the agitation column and the inner reaction vessel wall, said circulation being done in a manner to maintain the titaniferous bearing material in a continuous turbulant suspension flow in the agitation column; (4) cooling the resulting reaction mixture to a temperature below about 110° C. without precipitating the reaction mixture, and (5) continuously discharging the reaction mixture from the reaction vessel and recovering extracted titanium values.

Claim 8

The process in claim 5 wherein the agitation is conducted by introducing a stream of gas under pressure into the lower part of the agitation column located within the reaction vessel at a sufficient velocity flow to form a rising turbulent suspension of gas bubbles and reaction mixture, discharging from the upper part of the agitation column the reaction mixture which is then returned to the lower part of the agitation column in the annular space between the agitation column and the inner reaction vessel wall.

Claim 9

The process in claim 5 wherein the agitation is conducted by an impeller agitator within the agitation column.

Claim 10

The process in claim 5 where a suitable reductant is added to the reaction mixture to reduce ferric sulfate values to ferrous sulfate, and to reduce minor amounts of titanyl sulfate to titanous sulfate, said reductant being added in at least stoichiometric amounts to the quantity of ferric iron present.

Claim 11

A continuous process of extracting titanium values from titaniferous bearing material, which comprises: (1) reacting titaniferous bearing material in an amount from about 10% to about 400% in excess of the stoichiometric amount of titaniferous bearing material necessary to react with sulfuric acid to provide titanyl sulfate, and dilute sulfuric acid solution having a concentration between about 25% and about 60% by weight, based upon the total weight of said solution, in the presence of a reducing agent which effects the reduction of ferric iron to ferrous iron in a first reaction vessel at a temperature below about 140° C.; (2) maintaining the reaction until the reaction mixture has a ratio of active acid to titanium dioxide of about 3.0; (3) extracting the titanium values by agitating the reaction mixture in an agitation column located within the reaction vessel in a direction countercurrent to the flow of the reaction mixture in the annular space located between the agitation column and the inner reaction vessel wall by introducing a stream of gas under pressure into the lower part of the agitation column at a sufficient rate to form a continuously rising turbulent suspension of gas bubbles and reaction mixture through the agitation column, discharging from the upper part of the agitation column the reaction mixture which is then returned to the lower part of the agitation column; (4) removing the reaction solution from said first reaction vessel and passing it to a second reaction vessel; (5) continuing the reaction of titaniferous bearing material and dilute sulfuric acid in said second reaction vessel at a temperature below about 110° C. to provide a reaction mixture having a ratio of active acid to titanium dioxide of about 2.0; (6) separating unreacted titaniferous bearing material from the reaction mixture to provide a solution of iron sulphate and titanyl sulphate; (7) removing iron sulfate from said solution of iron sulfate and titanyl sulfate to provide a solution of titanyl sulfate; (8) and recovering the extracted titanium values.

Claim 12

A continuous process of extracting titanium values from titaniferous bearing material, which comprises: (1) reacting titaniferous bearing material in an amount from about 10% to about 400% in excess of the stoichiometric amount of titaniferous bearing material necessary to react with sulfuric acid to provide titanyl sulfate, and dilute sulfuric acid solution having a concentration between about 25% and about 60% by weight, based upon the total weight of said solution, in the presence of a reducing agent which effects the reduction of ferric iron to ferrous iron in a first reaction vessel at a temperature below about 140° C.; (2) maintaining the reaction until the reaction mixture has a ratio of active acid to titanium dioxide of about 3.0; (3) extracting the titanium values by agitating the reaction mixture in an agitation column located within the reaction vessel in a direction countercurrent to the flow of the reaction mixture in the annular space located between the agitation column and the inner reaction vessel wall by introducing a stream of gas under pressure into the lower part of the agitation column at a sufficient rate to form a continuously rising turbulent suspension of gas bubbles and reaction mixture through the agitation column, discharging from the upper part of the agitation column the reaction mixture which is then returned to the lower part of the agitation column; (4) removing the reaction solution from said first reaction vessel and passing it to a second reaction vessel; (5) continuing the reaction of titaniferous bearing material and dilute sulfuric acid in said second reaction vessel at a temperature below about 110° C. to provide a reaction mixture having a ratio of active acid to titanium dioxide of about 2.0; (6) separating unreacted titaniferous bearing material from the reaction mixture to provide a solution of iron sulphate and titanyl sulphate; (7) removing iron sulfate from said solution of iron sulfate and titanyl sulfate to provide a solution of titanyl sulfate; (8) and recovering the extracted titanium values.