Methods for Pollucite Flotation, Plagioclase Flotation, and Quartz Purification
US-2024359190-A1 · Oct 31, 2024 · US
US9561512B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9561512-B2 |
| Application number | US-201214110646-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 10, 2012 |
| Priority date | Apr 13, 2011 |
| Publication date | Feb 7, 2017 |
| Grant date | Feb 7, 2017 |
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Compounds of the formulae: RO—X—NH 2 (Ia); RO—X—NH 3 + Y − (Ib); RO—X—NH—Z—NH 2 (IIa); and RO—X—NH—Z—NH 3 + Y − (IIb), in which X is an aliphatic alkylene group containing 2 to 6 carbon atoms; Z is an aliphatic alkylene group containing 2 to 6 carbon atoms; Y − is an anion; and R is an aliphatic iso C 13 H 27 -group with average branching degree ranging from 1.5 to 3.5. The compounds are particularly suitable as flotation collectors for enriching an iron mineral from a silicate-containing iron ore.
Opening claim text (preview).
The invention claimed is: 1. A process for enriching an iron mineral from a silicate-containing iron ore, the process comprising: performing inverse flotation with a collector or collector formulation comprising at least one compound of any of formulae (Ia), (Ib), (IIa) and (IIb), to at least partially separate a silicate-containing mineral from the silicate-containing iron ore and provide an iron-enriched mineral: RO—X—NH 2 (Ia); RO—X—NH 3 + Y − (Ib); RO—X—NH—Z—NH 2 (IIa); and RO—X—NH—Z—NH 3 + Y − (IIb), wherein X is an aliphatic alkylene group containing 2 to 6 carbon atoms; Z is an aliphatic alkylene group containing 2 to 6 carbon atoms; Y − is an anion; and R is an aliphatic iso C 13 H 27 -group with an average branching degree ranging from 2.0 to 2.5. 2. The process according to claim 1 , wherein at least one of X and Z is a linear or branched alkylene group. 3. The process according to claim 2 , wherein at least one of X and Z is a —CH 2 CH 2 CH 2 — moiety. 4. The process according to claim 1 , wherein Y − of the compounds of formulae: RO—X—NH 3 + Y − (Ib); and RO—X—NH—Z—NH 3 + Y − (IIb), is CH 3 CO 2 − . 5. The process according to claim 1 , wherein the collector or collector formulation comprises at least one compound selected from the group consisting of compounds of formulae (Ia) and (Ib) in combination with at least one compound selected from the group consisting of compounds of formulae (IIa) and (IIb). 6. The process according to claim 1 , further comprising performing froth flotation. 7. The process according to claim 1 , further comprising employing an additional frother. 8. The process according to claim 7 , wherein the additional frother is either a branched aliphatic alcohol with 10 or less carbon atoms; and/or an alkyl ethoxylate. 9. The process according to claim 1 , wherein the iron ore is haematite. 10. The process according to claim 1 , further comprising adding a depressant. 11. The process according to claim 10 , wherein the depressant is a starch. 12. The process according to claim 1 , wherein R has an average degree of branching from 2.0 to 2.4. 13. The process according to claim 1 , wherein the inverse flotation is carried out at a pH of from 9.8 to 10.7. 14. The process according to claim 1 , wherein the collector or collector formulation further comprises 20-50% by weight of acetic acid. 15. The process according to claim 1 , wherein the inverse flotation comprises five froth steps.
containing nitrogen · CPC title
Collectors · CPC title
Macromolecular compounds · CPC title
Frothers · CPC title
Depressants · CPC title
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