MINERAL SLURRY DRYING METHOD AND SYSTEM
The present invention provides methods and systems for reducing moisture in mineral slurries, particularly mineral slurries containing minerals of small particle diameter, using a granular drying material. The invention also relates to novel mineral products and intermediates useful in connection with the process. The method and system reduced moisture by contacting the mineral slurry with the granular drying material. The granular drying material is selected to be readily separated from the dried minerals using a size separation technique such as a sieve screen. The granular drying material is the regenerated, preferably using a process involving heat exchange and cross-flow air. The granular drying material is preferably capable of regeneration and recycling in a continuous process with minimal attrition.
1 - 51 . (canceled)
52 . A method for reducing the moisture content of a mineral slurry comprising:
(a) contacting the mineral slurry with a granular drying media;
(b) transferring moisture from the mineral slurry to the granular drying media to produce a dried mineral having a reduced moisture content and a wet granular drying media;
(c) separating the wet granular drying media from the dried mineral by difference in particle size;
(d) removing moisture from the wet granular drying media by passing the wet granular drying media vertically across heat exchanger plates while exposing the wet granular drying media to a cross-flow of air to produce dried granular drying media; and
(e) recirculating at least a portion of the dried granular drying media to step (a).
53 . The method of claim 52 , wherein the temperature of the heat exchanger plates is controlled to prevent a temperature drop in the cross-flow of air.
54 . The method of claim 52 , wherein the mineral slurry has been subjected to a size separation step prior to step (a).
55 . The method of claim 52 , wherein the mineral slurry has been subjected to a moisture reduction step prior to step (a).
56 . The method of claim 52 , wherein step (c) is conducted using a sieve screen.
57 . The method of claim 52 , wherein the granular drying media is spherical and has a mean particle diameter ranging from approximately 2.0 mm to approximately 4.7 mm.
58 . The method of claim 52 , wherein the granular drying media is spherical and has a mean particle diameter of approximately 3.2 mm.
59 . The method of claim 52 , wherein the granular drying media has a crush strength that exceeds 25 lbs.
60 . The method of claim 52 , wherein the granular drying media has a surface area of greater than or equal to 340 m 2 /g.
61 . The method of claim 52 , wherein the granular drying media is activated alumina.
62 . The method of claim 52 , wherein the granular drying media is activated alumina having a mean particle diameter ranging from approximately 2.0 mm to approximately 4.7 mm, a crush strength exceeding 25 lbs, and a surface area greater than or equal to 340 m 2 /g.
63 . The method of claim 52 , wherein the mineral slurry has greater than 50% of particles smaller than 28 mesh.
64 . The method of claim 52 , wherein the mineral slurry has greater than 80% of particles smaller than 28 mesh.
65 . The method of claim 52 , wherein the moisture content of the mineral slurry is greater than 20% by weight, and the moisture content of the dried mineral is less than 10% by weight after step (c).
66 . The method of claim 52 , wherein the mineral is iron ore.
67 . The method of claim 66 , wherein the iron ore includes quartz, chert, and/or carbonate.
68 . The method of claim 66 , wherein the iron ore is taconite.
69 . The method of claim 52 , wherein the mineral is bauxite.