Upgrading sorelslag for production of synthetic rutile

Claim 2

A process for recovering titanium, as TiO 2 , and other values from Sorelslag the steps comprising: a. admixing Sorelslag with an alkali metal salt or mixtures thereof in a weight ratio of 0.3:1 to 0.6:1 salt to slag and roasting the same at a temperature from 600° to 950° C. for about 1 to 4 hours; b. leaching in a first leaching stage said roasted slag, said leaching liquor being introduced from a subsequent leaching stage and being at a concentration of less than about 15% H 2 SO 4 ; c. leaching in at least one additional stage said slag, with a leaching liquor which is sulphuric acid of 25% to 30% concentration and returning the spent leaching liquor to a preceeding stage for first stage leaching; and d. calcining in a temperature range of 850 to 950° C. said leached slag to obtain a TiO 2 concentrate having at least 94% TiO 2 present.

Claim 3

The process as defined in claim 1, wherein the slag is ground and is admixed with salts of sodium or potassium or a mixture of said salts in an amount from 20 to 40% by weight based on said slag.

Claim 4

The process as defined in claim 1, wherein said slag is roasted with said salts whereby the refractory structure of said slag is destroyed, said roasting being at a temperature from 850° to 900° C.

Claim 5

A process for recovering titanium, as TiO 2 , and other values from Sorelslag the steps comprising: a. admixing Sorelslag with an alkali metal salt or mixtures thereof in a weight ratio of 0.3:1 to 0.6:1 salt to slag and roasting the same at a temperature from 600° to 950° C. for 1 to 4 hours; b. wet milling said slag and filtering the same including removing from filtrate vanadium and chromium values; c. leaching countercurrently in a first stage said slag with sulfuric acid leaching liquor, said leaching liquor being introduced from a subsequent leaching stage said leaching liquor being at a concentration of less than about 15% H 2 SO 4 ; d. separating the spent leaching liquor from said first stage leached slag; e. leaching in at least one additional stage said slag with a leaching liquor which is a sulphuric acid leaching liquor wherein the concentration of sulphuric acid in said leaching liquor is about 25 to 30%; f. filtering said leached slag and returning the spent leaching liquor to a preceeding stage for leaching of said slag in said first stage; and g. calcining said leached slag to obtain a TiO 2 concentrate having at least 94% TiO 2 present.

Claim 6

A process for recovering titanium, as TiO 2 , and other values from Sorelslag the steps comprising: a. admixing Sorelslag with an alkali metal salt or mixtures thereof in a weight ratio of 0.3:1 to 0.6:1 salt to slag and roasting the same at a temperature from 600° to 950° C. for 1 to 4 hours; b. wet milling said slag and filtering the same including removing from filtrate vanadium and chromium values; c. leaching countercurrently in a first stage said slag with sulfuric acid leaching liquor, said leaching liquor being introduced from a subsequent leaching stage said leaching liquor being at a concentration of less than about 15% H 2 SO 4 ; d. separating the spent leaching liquor from said first stage leached slag; e. leaching in at least one additional stage said slag with a leaching liquor which is a sulphuric acid leaching liquor wherein the concentration of sulphuric acid in said leaching liquor is about 25 to 30%; f. filtering said leached slag and returning the spent leaching liquor to a preceeding stage for leaching of said slag in said first stage; and g. calcining said leached slag to obtain a TiO 2 concentrate having at least 94% TiO 2 present.

Claim 7

The process for recovery of titanium values from Sorelslag as defined in claim 11, wherein in step (a) a refractory structure of said slag is destroyed by admixing and roasting said slag with an alkali metal salt or mixtures thereof including carbonates, chlorides, sulphates, nitrates, or oxides or hydroxides whereby said slag is rendered amenable to leaching.

Claim 8

The process as defined in claim 4 wherein said leaching is carried out in the first stage at an atmospheric boiling temperature, under reflux, utilizing spent acid from a subsequent leaching stage, said acid being diluted with washings to contain a maximum concentration of less than about 15% of H 2 SO 4 , and leaching in the second stage, for which a spent acid of a concentration from 25 to 30% of H 2 SO 4 is employed to obtain a leached slag, said leaching being carried out at atmospheric boiling temperature and atmospheric pressure, and recovering the final concentrate of TiO 2 by filtering of said leached slag, washing said leached slag, and calcining said leached slag at a temperature of 850° to 900° C.