The disclosure relates to a method for the beneficiation of an ore in a froth flotation process. The method comprises contacting an ore in a liquid medium to a collector composition comprising a plant-derived liquid decarboxylated rosin acid (DCR) collector. The DCR comprises 40 to 100 wt. % of tricyclic compounds having 18-20 carbon atoms, one or more CC groups, and m/z (mass/charge) value of 220-280. The DCR has an oxygen content of <5%, a density of 0.9 to 1.0 g/cm.sup.3 at 20 C., and an acid value of <50 mg KOH/g.

The disclosure relates to a method for the beneficiation of an ore in a froth flotation process. The method comprises contacting an ore in a liquid medium to a collector composition comprising a plant-derived liquid decarboxylated rosin acid (DCR) collector. The DCR comprises 40 to 100 wt. % of tricyclic compounds having 18-20 carbon atoms, one or more CC groups, and m/z (mass/charge) value of 220-280. The DCR has an oxygen content of <5%, a density of 0.9 to 1.0 g/cm.sup.3 at 20 C., and an acid value of <50 mg KOH/g.

Disclosed is an application of a class of selenium-containing organic compounds in copper sulfide flotation collectors, including organic compound with selenium atoms as functional groups and containing single selenium atom or multiple selenium atoms, where the organic compound with selenium atoms as functional groups and containing single selenium atom or multiple selenium atoms includes but not limited to selenophene, phenylselenol and diselenide as copper collectors; and a class of organic compound containing selenium atoms combined with nitrogen, oxygen, phosphorus, sulfur and carbon, where the class of organic compound containing selenium atoms combined with nitrogen, oxygen, phosphorus, sulfur and carbon includes but not limited to selenomethyl ester, carbonyl selenomethyl ester, oxycarbonyl selenomethyl ester, selenourea, selenium nitrogen, selenoxanthonic acid, selenoxanthate, selenophosphoric acid, selenium phosphate ester, triphenylphosphine selenide, all kinds of benzoselenediazole molecules as copper collectors.

Disclosed is an application of a class of selenium-containing organic compounds in copper sulfide flotation collectors, including organic compound with selenium atoms as functional groups and containing single selenium atom or multiple selenium atoms, where the organic compound with selenium atoms as functional groups and containing single selenium atom or multiple selenium atoms includes but not limited to selenophene, phenylselenol and diselenide as copper collectors; and a class of organic compound containing selenium atoms combined with nitrogen, oxygen, phosphorus, sulfur and carbon, where the class of organic compound containing selenium atoms combined with nitrogen, oxygen, phosphorus, sulfur and carbon includes but not limited to selenomethyl ester, carbonyl selenomethyl ester, oxycarbonyl selenomethyl ester, selenourea, selenium nitrogen, selenoxanthonic acid, selenoxanthate, selenophosphoric acid, selenium phosphate ester, triphenylphosphine selenide, all kinds of benzoselenediazole molecules as copper collectors.

Provided herein are processes for treating a metal ore containing a flotable mineral involving subjecting an ore to flotation and separating a fraction enriched in the flotable mineral from a fraction containing waste ore components. Also provided herein are flotation collector compositions useful in the above processes, and additive compositions and kits for producing the flotation collector compositions.

Provided herein are processes for treating a metal ore containing a flotable mineral involving subjecting an ore to flotation and separating a fraction enriched in the flotable mineral from a fraction containing waste ore components. Also provided herein are flotation collector compositions useful in the above processes, and additive compositions and kits for producing the flotation collector compositions.

Disclosed herein are methods, devices, and systems for effectively separating carbonate gangue from bastnaesite without sacrificing significant REO grade or recovery. In some embodiments, centrifugal concentrators may beneficiate Ultra-Fine (UF) bastnaesite and calcite bearing flotation concentrates. The disclosed methods, devices, and systems can achieve initial gravity REO recoveries exceeding 90% while rejecting on the order of 25% to 35% of the total calcium from an assortment of rougher and cleaner flotation concentrates. Addition of stages of cleaner UF Falcon gravity separation may be operated in an open circuit configuration, from an original fine feed of 35 microns containing 50.5% REO and 5.5% Ca, to upgrade up to approximately 59% REO and 2.0% calcium. The disclosed methods, devices, and systems may comprise UF gravity concentration that may provide for recovery of rare earth oxides at levels of greater than 70%, 80% and 90%, while also rejecting more than 15%, 20%, 25%, 30, or 35% of the total calcium. Also described are benefication of fine feed of 35 microns containing 50.5% REO and 5.5% Ca, to approximately 59% REO and 2.0% calcium. In some embodiments, the disclosed methods, compounds, and systems may be used to complement existing or modified flotation systems.

Disclosed herein are methods, devices, and systems for effectively separating carbonate gangue from bastnaesite without sacrificing significant REO grade or recovery. In some embodiments, centrifugal concentrators may beneficiate Ultra-Fine (UF) bastnaesite and calcite bearing flotation concentrates. The disclosed methods, devices, and systems can achieve initial gravity REO recoveries exceeding 90% while rejecting on the order of 25% to 35% of the total calcium from an assortment of rougher and cleaner flotation concentrates. Addition of stages of cleaner UF Falcon gravity separation may be operated in an open circuit configuration, from an original fine feed of 35 microns containing 50.5% REO and 5.5% Ca, to upgrade up to approximately 59% REO and 2.0% calcium. The disclosed methods, devices, and systems may comprise UF gravity concentration that may provide for recovery of rare earth oxides at levels of greater than 70%, 80% and 90%, while also rejecting more than 15%, 20%, 25%, 30, or 35% of the total calcium. Also described are benefication of fine feed of 35 microns containing 50.5% REO and 5.5% Ca, to approximately 59% REO and 2.0% calcium. In some embodiments, the disclosed methods, compounds, and systems may be used to complement existing or modified flotation systems.

Compositions and methods for the separation and recovery of one or more minerals from a mineral ore bulk material are provided. The compositions and methods include selectively depressing minerals utilizing an ammoniated polycarbamide as a separation aid. The ammoniated polycarbamide reduces, or eliminates, the conventional use of depressants such as sodium hydrosulfide (NaSH) in mining flotation processes, including copper-molybdenum (CuMo) separations.

Compositions and methods for the separation and recovery of one or more minerals from a mineral ore bulk material are provided. The compositions and methods include selectively depressing minerals utilizing an ammoniated polycarbamide as a separation aid. The ammoniated polycarbamide reduces, or eliminates, the conventional use of depressants such as sodium hydrosulfide (NaSH) in mining flotation processes, including copper-molybdenum (CuMo) separations.