COAL AND MINERAL SLURRY DRYING METHOD AND SYSTEM
The present invention provides methods and systems for reducing moisture in coal and mineral slurries, particularly slurries containing small diameter particles, using a granular drying material. The invention also relates to novel products and intermediates useful in connection with the process. The method and system reduced moisture by contacting the slurry with the granular drying material. The granular drying material is selected to be readily separated from the dried coal or 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 . A method for reducing the moisture content of a coal or mineral slurry comprising:
(a) contacting the slurry with a granular drying media;
(b) transferring moisture from the slurry to the granular drying media to produce a dried product having a reduced moisture content and a wet granular drying media;
(c) separating the wet granular drying media from the dried product 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).
2 . The method of claim 1 , wherein the temperature of the heat exchanger plates is controlled to prevent a temperature drop in the cross-flow of air.
3 . The method of claim 1 , wherein the slurry has been subjected to a size separation step prior to step (a).
4 . The method of claim 1 , wherein the slurry has been subjected to a moisture reduction step prior to step (a).
5 . The method of claim 1 , wherein step (c) is conducted using a sieve screen.
6 . The method of claim 1 , wherein the granular drying media is spherical and has a mean particle diameter ranging from approximately 2.0 mm to approximately 4.7 mm.
7 . The method of claim 1 , wherein the granular drying media is spherical and has a mean particle diameter of approximately 3.2 mm.
8 . The method of claim 1 , wherein the granular drying media has a crush strength that exceeds 25 lbs.
9 . The method of claim 1 , wherein the granular drying media has a surface area of greater than or equal to 340 m 2 /g.
10 . The method of claim 1 , wherein the granular drying media is activated alumina.
11 . The method of claim 1 , 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.
12 . The method of claim 1 , wherein the slurry has greater than 50% of particles smaller than 28 mesh.
13 . The method of claim 1 , wherein the slurry has greater than 80% of particles smaller than 28 mesh.
14 . The method of claim 1 , wherein the moisture content of the slurry is greater than 20% by weight, and the moisture content of the dried product is less than 10% by weight after step (c).
15 . The method of claim 1 , wherein the slurry is a mineral slurry.
16 . The method of claim 15 , wherein the mineral comprises iron ore.
17 . The method of claim 1 , wherein slurry is a coal slurry.
18 . The method of claim 17 , wherein the coal has a particle size of 28 mesh or smaller.
19 . A system for reducing coal moisture comprising:
(a) a combination unit for contacting a first volume of coal and a second volume of granular drying media to transfer moisture from the coal to the granular drying media;
(b) a separation unit for separating the granular drying material from the coal by difference in particle size.
(c) a regeneration unit for removing moisture from the granular drying media, the regeneration unit comprising heat exchange and cross-flow air.
20 . The system of claim 19 , wherein the regeneration unit removes 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.
21 . The system of claim 19 , wherein the temperature of the heat exchanger plates is controlled to prevent a temperature drop in the cross-flow of air.
22 . The system of claim 19 , wherein the combination unit comprises at least one mixer.
23 . The system of claim 22 , wherein at least one of the mixers is a paddle mixer.
24 . The system of claim 19 , wherein the combination unit comprises at least two mixers and a bypass unit.
25 . The system of claim 22 , wherein the bypass unit comprises a flop gate.