Mechanical dewatering process

• US 4,810,257 A
• Filed: 03/12/1986
• Issued: 03/07/1989
• Est. Priority Date: 04/26/1985
• Status: Expired due to Fees

• Current Assignee: Institute of Gas Technology 3424 South State Street Chicago Illinois A Non-Profit Corporation of Illinois
• Original Assignee: Institute Of Gas Technology (GTI Energy)
• Inventors: Lau, Francis S., Pyrcioch, Eugene J., Mensinger, Michael C.
• Primary Examiner(s): DEES, CARL
• Application Number:
  US06/839,119
• Time in Patent Office: 1,091 Days
• Field of Search: 44/1 D, 44/1 G, 44/27, 44/31, 44/33, 44/32, 44/605, 44/589, 210/93
• US Class Current: 44/490
• CPC Class Codes: C10F 5/00 Drying or de-watering peat drying in general F26B

Abstract

An improved mechanical dewatering process wherein high moisture content organic carbonaceous materials are mixed with hard, non-porous particulates prior to mechanical dewatering by conventional methods, and the particulates are removed after mechanical dewatering treatment to yield organic carbonaceous product having a moisture content of less than about 50 weight percent total water suitable for use directly as a fuel or as substrate for subsequent conversion processes.

Claims

1. An improved process for mechanically dewatering high moisture content organic carbonaceous materials comprising the steps of:

adding hard, non-porous solid particulates which are inert to said organic carbonaceous materials and water having average particle diameters of from about 0.04 mm to about 7.0 mm to the high moisture content organic carbonaceous feed materials and mixing said particulates with said organic materials evenly distributing said particulates throughout said organic materials and particulates admixture, said particulates comprising about 25 to about 60 weight percent of said admixture;

mechanically dewatering said admixture by a mechanical dewatering emans capable of delivering pressure of at least 50 psi, said solid particulates providing in situ dewatering of said organic carbonaceous materials at sites on surfaces of said non-porous solid particulates;

removing water released from said admixture during dewatering; and

separating said particulates from the organic materials to provide a dewatered organic carbonaceous product unaltered in physical and chemical properties from said organic carbonaceous feed material, except for the reduction in moisture content.

2. An improved process according to claim 1 comprising an additional step of:

recirculating said separated particulates for addition to high moisture content organic carbonaceous materials.

3. An improved process according to claim 1, wherein said high moisture content organic carbonaceous materials comprise about 55 to about 98 weight percent total water.

4. An improved process according to claim 3, wherein said high moisture content organic carbonaceous materials are selected from the group consisting of peat, agricultural waste, municipal waste, sewage sludge, biomass, and mixtures thereof.

5. An improved process according to claim 1, wherein said particulates have average particle diameters of about 0.25 mm to about 3.0 mm.

6. An improved process according to claim 1, wherein said particulates comprise about 40 to about 60 weight percent of said admixture.

7. An improved process according to claim 1, wherein said mechanical dewatering means comprises a roll and belt press.

8. An improved process according to claim 1, wherein said mechanical dewatering means comprises a filter press.

9. An improved process according to claim 1, wherein said mechanical dewatering means comprises a screw press.

10. An improved process according to claim 1, wherein said mechanical dewatering means comprises a centrifuge.

11. An improved process according to claim 1, wherein said mechanical dewatering means is capable of delivering pressures to about 10,000 psi.

12. An improved process according to claim 1, wherein said mechanical dewatering means is capable of delivering pressures to about 3,500 psi.

13. An improved process according to claim 1, wherein said hard, non-porous particulates comprise sand.

14. An improved process according to claim 1, wherein said hard, non-porous particulates comprise magnetite.

15. An improved process according to claim 14, wherein said particulates are separated from said organic materials by a magnetic separator means.

16. An improved process according to claim 1, wherein said dewatered organic carbonaceous product comprises less than 50 weight percent total water.

17. An improved process for mechanically dewatering organic carbonaceous materials having a moisture content of about 55 to about 98 weight percent total water, said improvement comprising adding hard, non-porous solid particulates which are inert to said organic carbonaceous materials and water having average particle diameters of from about 0.04 mm to about 7.0 mm to the organic carbonaceous feed materials, forming an admixture thereof having about 25 to about 60 weight percent of said particulates, mechanically dewatering said admixture, said solid particulates providing in situ dewatering of said organic carbonaceous materials on the surfaces of said non-porous solid particulates, and separating said particulates from the organic carbonaceous materials subsequent to application of the mechanical dewatering means to provide a dewatered organic carbonaceous product unaltered in physical and chemical properties from said organic carbonaceous feed material, except for the reduction in moisture content, said dewatered organic carbonaceous product having a moisture content of less than about 50 weight percent total water.

18. An improved process according to claim 17, wherein said hard, non-porous particulates comprise sand.

19. An improved process according to claim 17, wherein said hard, non-porous particulates comprise magnetite.