Claims
- 1. A method for upgrading the content of TiO.sub.2 in a titaniferous slag, the titaniferous slag containing FeO, Ti.sub.2 O.sub.3 and at least 1.0 weight percent MgO, and the molecular ratio of Ti.sub.2 O.sub.3 to FeO being at least about 1, the method comprising:
- contacting the titaniferous slag with chlorine gas at a temperature of at least about 800.degree. C. such that the slag is chlorine-treated and FeCl.sub.2 is formed; and
- contacting the chlorine-treated slag with hydrochloric acid such that MgCl.sub.2 is formed and the slag is hydrochloric acid-treated.
- 2. The method of claim 1 wherein the chlorine-treated slag is contacted with hydrochloric acid at a temperature of at least about 140.degree. C.
- 3. The method of claim 2 where the chlorine-treated slag is contacted with hydrochloric acid at a temperature of about 190.degree. C.
- 4. The method of claim 1 where the titaniferous slag before contacting with the chlorine gas contains at least 1.2 weight percent of magnesium oxide.
- 5. The method of claim 1 where the molecular ratio of Ti.sub.2 O.sub.3 to FeO plus MgO in the titaniferous slag before contacting with the chlorine gas is no more than about 1.
- 6. The method of claim I where the titaniferous slag before contacting with the chlorine gas is sized to a dimension suitable for fluidization.
- 7. The method of claim 1 where the titaniferous slag before contacting with the chlorine gas is preheated in an inert atmosphere before being contacted with chlorine.
- 8. The method of claim 1 where the chlorine gas is diluted with nitrogen.
- 9. The method of claim 8, wherein the molar ratio of nitrogen and chlorine is between about 5:1 to 1:2.
- 10. The method of claim 1 where the hydrochloric acid is present in at least about a 20% stoichiometric excess over that needed to form MgCl.sub.2.
- 11. The method of claim 1 where the hydrochloric acid is at least about 5 molar.
- 12. The method of claim 11, where the hydrochloric acid is about 10 molar.
- 13. The method of claim 1 where the chlorine-treated slag is contacted by hydrochloric acid at a pressure in excess of atmospheric pressure.
- 14. The method of claim 13, wherein the pressure in excess of atmospheric pressure is within the range of about 250- 500 psi.
- 15. The method of claim 1, further comprising the steps of:
- washing the hydrochloric acid-treated slag with water;
- drying the washed slag; and
- calcining the dried slag.
- 16. The method of claim 1, further comprising the step of leaching the slag with a caustic material after completing the step of contacting the chlorine-treated slag with hydrochloric acid.
- 17. The method of claim 16, wherein the caustic material is sodium hydroxide such that the slag is sodium hydroxide-treated.
- 18. The method of claim 17, wherein the sodium hydroxide is present in a 1 normal concentration.
- 19. The method of claim 18, further comprising the step of washing the sodium hydroxide-treated slag with acidified water.
- 20. A method for upgrading the content of TiO.sub.2 in a titaniferous slag, the titaniferous slag containing FeO, Ti.sub.2 O.sub.3 and at least 1.0 weight percent MgO, and the molecular ratio of Ti.sub.2 O.sub.3 to FeO being at least about 1, the method comprising:
- heating the slag in an inert atmosphere to a temperature of at least about 800.degree. C.;
- contacting the heated slag with chlorine gas at a temperature of at least about 800.degree. C. such that ironchlorides are formed and the titaniferous slag is chlorine-treated;
- continuing to contact the heated slag with chlorine gas for a predetermined time interval;
- cooling the chlorine-treated slag to approximately room temperature;
- contacting the chlorine-treated slag with hydrochloric acid at a temperature of at least about 140.degree. C. such that the slag is hydrochloric acid-treated;
- cooling the hydrochloric acid-treated slag;
- washing the slag;
- drying the slag; and
- calcining the slag such that a calcined slag is formed.
- 21. The method of claim 20, further comprising the step of leaching the calcined slag with sodium hydroxide such that the slag is sodium hydroxide leached.
- 22. The method of claim 21, further comprising the step of washing the sodium hydroxide-leached slag with acidified water.
- 23. The method of claim 20, wherein the chlorine gas is diluted with nitrogen, the molar ratio of nitrogen and chlorine being between about 5:1 to 1:2.
- 24. The method of claim 20, wherein the hydrochloric acid is about 10 molar and is present in at least about a 20% stoichiometric excess over that needed to form MgCl.sub.2.
- 25. The method of claim 20, wherein the chlorine-treated slag is contacted by hydrochloric acid at a pressure in excess of atmospheric pressure.
- 26. The method of claim 25, wherein the pressure in excess of atmospheric pressure is within the range of about 250- 500 psi.
Parent Case Info
This application is a continuation-in-part of application Ser. No. 07/130,580, filed Dec 9, 1987, by Michel Gueguin, entitled "METHOD OF PREPARING A SYNTHETIC RUTILE FROM A TITANIFEROUS SLAG CONTAINING ALKALINE EARTH METALS."
US Referenced Citations (27)
Non-Patent Literature Citations (1)
Entry |
Kirk-Othmer's Encyclopedia of Chemical Technology 3rd Ed., vol. 23, pp. 143-148. |