Preparation of iron compounds by hydrothermal conversion
View Patent ↗An apparatus and continuous process for the conversion of one solid iron compound to another solid iron compound in a heterogeneous suspension wherein the suspension is formed by dispersing a solid starting iron compound in a liquid that is continuously fed through one or more agitated conversion vessels under hydrothermal conditions and converted to a solid product iron compound having different physical, chemical, or structural properties from the solid starting iron compound.
1. A continuous process comprising the steps of:
forming a suspension by dispersing a solid starting iron compound in a liquid;
continuously feeding the suspension through two or more agitated conversion vessels under hydrothermal conditions wherein the operating conditions in at least one of the conversion vessels is different from the other conversion vessels;
converting the solid starting iron compound into a solid product iron compound, having different physical, chemical, or structural properties from the solid starting iron compound, in the two or more agitated conversion vessels; and
continuously removing the solid product iron compound from the last of the two or more conversion vessels.
2. The process of claim 1 , wherein the solid starting iron compound is selected from the group consisting of iron oxides, iron hydroxide, iron oxyhydroxides, and mixtures thereof.
3. The process of claim 2 , wherein the solid starting iron compound is an iron ore, a synthetic iron product, or a precipitated iron salt.
4. The process of claim 3 , wherein the solid starting iron compound is an iron ore selected from the group consisting of goethite, akaganeite, bernalite, feroxyhyte, ferrihydrite, lepidocrocite, limonite, maghemite, magnetite, hematite, and wustite.
5. The process of claim 1 wherein an additive-containing solid starting iron compound is used.
6. The process of claim 1 , wherein the suspension flows substantially upward through the one or more conversion vessels.
7. The process of claim 1 , wherein from two to five conversion vessels are employed.
8. The process of claim 1 , wherein the pH in at least one of the conversion vessels is different from the other conversion vessels.
9. The process of claim 1 , wherein an additive is added to at least one of the conversion vessels.
10. The process of claim 1 , wherein seeds are added to at least one of the conversion vessels.
11. The process of claim 1 further comprising a feed preparation vessel wherein the suspension is prepared.
12. The process of claim 11 , wherein the liquid is water.
13. The process of claim 11 , wherein the liquid is an alcohol.
14. The process of claim 11 , wherein the liquid is a hydrocarbon.
15. The process of claim 11 , wherein at least one additive is added to the suspension.
16. The process of claim 15 , wherein the additive includes a rare earth metal, a transition metal, a noble metal, and alkali metal, or an alkaline earth metal.
17. The process of claim 16 , wherein the additive is an oxide, hydroxide, carbonate, or hydroxycarbonate.
18. The process of claim 11 , wherein the temperature in the one or more conversion vessels ranges from 150 to 375° C.
19. The process of claim 1 wherein the solids to liquid ratio of the suspension entering the one or more conversion vessels ranges from 0.05:1 to 0.25:1.
20. The process of claim 19 , wherein the solids to liquid ratio of the suspension exiting the last of the two or more conversion vessels ranges from 0.03:1 to 0.22:1.
21. The process of claim 1 , wherein the solids content of the suspension entering the two or more conversion vessels deviates from the solids content of the suspension exiting the last of the two or more conversion vessels by less than 40 wt%.
22. The process of claim 21 , wherein the solids content of the suspension entering the two or more conversion vessels deviates from the solids content of the suspension exiting the last of the two or more conversion vessels by less than 25 wt%.
23. The process of claim 22 , wherein the solids content of the suspension entering the one or more conversion vessels deviates from the solids, content of the suspension exiting the last of the two or more conversion vessels by less than 10 wt%.