Abstract A method is disclosed for processing a natural calcitic ore to yield a finely divided calcium carbonate particulate of very high brightness characteristics. The natural calcitic ore is initially coarse-milled to produce a product wherein no more than 5% by weight of the particulate is +325 mesh, and no more than 35% by weight of the particles are of less than 2 microns E.S.D. This coarse-milled product is then subjected as an aqueous slurry including less than 40% solids, to a froth flotation, which separates with the froth the relatively coarse colorbodies liberated in the initial grinding. The purified underflow is then dewatered to at least 60% solids by weight, and is wet-milled, as for example in a sand mill, to yield an output product wherein at least 80% by weight of the resultant particulate has an E.S.D. of less than 2 microns, the product being further characterized by a brightness of at least 94 on the G.E. scale.
A method for processing a natural calcitic ore to yield a finely divided calcium carbonate particulate of relatively very high brightness characteristics, comprising in sequence the steps of: coarse-milling said natural calcitic ores to produce a coarse-milled product; subjecting said coarse-milled product as an aqueous slurry including less than 40% solids to a froth flotation, and separating with the froth discoloring contaminants; dewatering the underflow product from said froth flotation to at least 60% solids by weight; and wet-milling the dewatered product to yield an output product wherein at least 80% by weight of the resultant particulate has an E.S.D. of less than 2 microns, said output product being further characterized by a brightness of at least 94 on the G.E. scale.
Claim 2
Independent Claim
122 words
A method for processing a natural calcitic ore to yield a finely divided calcium carbonate particulate of relatively very high brightness characteristics, comprising in sequence the steps of: coarse-milling said natural calcitic ores to produce a coarse-milled product; subjecting said coarse-milled product as an aqueous slurry including less than 40% solids to a froth flotation, and separating with the froth discoloring contaminants; dewatering the underflow product from said froth flotation to at least 60% solids by weight; and wet-milling the dewatered product to yield an output product wherein at least 80% by weight of the resultant particulate has an E.S.D. of less than 2 microns, said output product being further characterized by a brightness of at least 94 on the G.E. scale.
Claim 3
Dependent Claim
44 words
A method in accordance with claim 1, wherein said coarse-milling effects reduction of said natural calcitic ore such that no more than 5% by weight of the particles thereof are +325 mesh, and no more than 35% are of less than 2 microns E.S.D.
Claim 4
Dependent Claim
16 words
A method in accordance with claim 2, wherein said wet milling is effected by sand grinding.
Claim 5
Dependent Claim
18 words
A method in accordance with claim 2, wherein said froth flotation product is dewatered to over 65% solids.
Claim 6
Dependent Claim
15 words
A method in accordance with claim 1, wherein said coarse-milling is effected by dry grinding.