Process for the dewatering of coal and mineral slurries

• US 5,771,601 A
• Filed: 05/21/1996
• Issued: 06/30/1998
• Est. Priority Date: 05/23/1995
• Status: Expired due to Fees

• Current Assignee: Commonwealth Scientific & Industrial Research Organisation (Commonwealth Of Australia As Represented By Department Of Industry, Innovation, Climate Change, Science, Research And Tertiary Education)
• Original Assignee: Commonwealth Scientific & Industrial Research Organisation (Commonwealth Of Australia As Represented By Department Of Industry, Innovation, Climate Change, Science, Research And Tertiary Education)
• Inventors: Nicol, Stuart K., Johnston, Barry Kenneth, Veal, Christopher John
• Primary Examiner(s): Bennett, Henry A.
• Assistant Examiner(s): GRAVINI, STEPHEN MICHAEL
• Application Number:
  US08/651,669
• Time in Patent Office: 770 Days
• Field of Search: 34/312, 34/314, 34/320, 34/326, 34/328, 34/363, 34/370, 34/371, 34/58, 34/138, 34/164, 34/197, 210/360.1, 210/372, 210/374, 210/377, 210/380.1, 210/384, 210/388, 210/393, 210/787, 210/53, 494/58
• US Class Current: 34/314
• CPC Class Codes: B04B 3/06 discharging solid particles by vibrating the bowl
• CPC Class Codes: F26B 17/26 with movement performed by reciprocating or oscillating conveyors propelling materials over stationary surfaces; with movement performed by reciprocating or oscillating shelves, sieves, or trays F26B17/006 takes precedence
• CPC Class Codes: F26B 5/08 by centrifugal treatment

Abstract

Coal or other mineral slurry is dewatered by establishing a bed of the slurry and injecting a gas stream such as air into the bed to establish turbulent flow to strip moisture. This slurry may use particles in the range 0.5 mm to 30 mm with air injected at about 10 m/sec, and suitable novel apparatus includes a centrifuge or a vibratory conveyor with a closed tunnel and transverse air flow for stripping moisture.

Claims

1. A method of reducing moisture content of a bed of solid particles comprising subjecting the bed to a stream of gas to establish turbulent flow through the bed to strip a significant proportion of the moisture contained in the bed, wherein said moisture content of said bed is reduced predominantly by means of a mass transport mechanism effected by the established turbulent flow.

2. A method as claimed in claim 1 and wherein the bed is arranged in a processing zone of a centrifuge.

3. A method as claimed in claim 2, comprising subjecting the bed to said stream of gas in a vibrating basket centrifuge having an air discharge manifold located nearer the open end of the basket and having air discharge nozzles extending into the basket.

4. A method as claimed in claim 3 and comprising using an air discharge manifold wherein the nozzles are provided spaced along tubes which are disposed parallel to the axis of the centrifuge and the nozzles directing airflow radially outwardly.

5. A method as claimed in claim 2 and comprising using a scroll centrifuge providing a pressurised gas stream which is discharged through apertures in a conical inner wall of the centrifuge.

6. A method as claimed in claim 2, comprising subjecting the bed in said centrifuge to a centrifugal force of about 60 G.

7. A method as claimed in claim 1 and wherein the bed of solid particles is continuously advanced along a path and the path is intersected with the stream of air which is discharged together with moisture removed from the bed.

8. A method as claimed in claim 1, and including selecting the bed of particles to be principally sized in the range 0.5 mm to 30 mm.

9. A method as claimed in claim 1, and including selecting the bed of solid particles with at least 90% of the particles sized greater than 1.5 mm and less than 30 mm.

10. A method as claimed in claim 1, comprising injecting into the bed, said stream of gas at a speed of about 10 m/sec, wherein said stream of gas is air.