Process to increase the effectiveness of bagasse as a source of energy

• US 4,363,636 A
• Filed: 10/15/1981
• Issued: 12/14/1982
• Est. Priority Date: 10/15/1981
• Status: Expired due to Fees

• Current Assignee: Hamakua Sugar Company
• Original Assignee: Davies Hamakua Sugar Company
• Inventors: Suzor, Norland L. C., Bouvet, Pierre E.
• Primary Examiner(s): DEES, CARL
• Application Number:
  US06/311,642
• Time in Patent Office: 425 Days
• Field of Search: 44/1 D, 44/15 B, 44/10 A, 44/10 E, 44/10 G, 44/10 R, 44/32, 44/1 R
• US Class Current: 44/589
• CPC Class Codes: C10L 5/44 on vegetable substances
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

The effectiveness of bagasse as a source of energy is increased by a flexible operation adapted to the power requirements, fuel storage requirements and other variables of a sugar mill operation. Part or all of a primary stream of bagasse from the sugar mill is dried from its initial moisture content, e.g. in the order of 50%, to a lower moisture content, e.g. in the order of 35%, using a portion of the hot flue gases from the boilers which are used to supply power for the sugar mill operation. The resulting drier material is separated to provide an oversize particle stream which may be sent directly to the boiler for burning, to storage in the bagasse house, or to a secondary drying operation, and a secondary stream of fine particle size bagasse components which are most suitable for further process and densification. This secondary stream, with optional addition of oversize particles from the primary drying operation, is then dried in contact with another portion of hot flue gases to a moisture content suitable for densification, about 6-12% where a pellet mill is employed, and is further subjected to particle size selection, if necessary, and then subjected to densification in a pellet mill or other suitable equipment. The densified material is then sent to storage, returned to the boilers for part or all of the fuel requirement or transported to other potential users.

Claims

1. A process for increasing the effectiveness of bagasse as a source of energy in combination with a sugar mill operation in which bagasse from the mill is used as a boiler fuel for the sugar mill operation, comprising:

subjecting a stream of wet bagasse from the mill to a primary drying operation in which said bagasse is contacted with a stream of flue gases from the boiler to reduce the moisture content of the bagasse to about 25-40%, size separating the resulting bagasse into a stream containing larger particle components of the bagasse and a secondary stream containing smaller particle components of the bagasse, subjecting said secondary stream of particles to a secondary drying operation in which said particles are contacted with a stream of flue gases from the boiler to reduce their moisture content to about 8 to 14% and densifying the resulting dried bagasse from the secondary drying operation into compacted shapes suitable for boiler firing.

2. The process of claim 1 wherein at least a portion of the bagasse containing said larger particles is combined with the secondary stream containing said smaller particles prior to introduction into the said secondary drying operation and wherein the particles from the secondary drying operation are subjected to particle size adjustment prior to densification.

3. The process of claim 1 wherein at least a portion of the stream of bagasse containing said larger particles is subjected to comminution and classification to provide additional fine particles and said fine particles are combined with said secondary stream of particles prior to the secondary drying operation.

4. The process of claim 1 wherein the compacted shapes are stored for year round fuel supply to the sugar mill boilers.

5. The process of claim 2 wherein said particle size adjustment comprises size separation of the particles into a fines fraction suitable for pelleting in a pellet mill and an oversize fraction unsuitable for pelleting, comminution of the oversize fraction and return of fines resulting from said comminution to the said fines fraction.

6. A process for increasing the effectiveness of bagasse as a source of energy in combination with a sugar mill operation in which bagasse from the mill is used as boiler fuel for the sugar mill operation, comprising:

subjecting a stream of wet bagasse from the mill to a primary drying operation in which said bagasse is contacted with a stream of flue gases from the sugar mill boiler or boilers to reduce the moisture content of the bagasse to about 25 to 40%, size separating the resulting bagasse into a primary stream of particles which are oversize for densification and a secondary stream of finer particles which contains components of a size suitable for densification, conveying the stream of oversize particles to the sugar mill boiler or boilers for fuel or to a bagasse fuel storage house, subjecting the secondary stream of bagasse particles to further drying in a secondary drying operation in which the bagasse particles are contacted with boiler flue gases to reduce their moisture content to about 8 to 14%, and densifying the resulting dried bagasse from the secondary dryer into compacted shapes suitable for boiler firing.

7. The process of claim 6 wherein the bagasse is dried in the primary drying operation to approximately 30 to 40% moisture and the bagasse is dried in the secondary drying operation to approximately 8 to 12% moisture.

8. The process of claim 7 wherein bagasse particles from the secondary drying operation are compressed into fuel pellets in a pellet mill.

9. The process of claim 8 wherein bagasse particles from the secondary drying operation are compressed into pellets having a size in the range of about 1/4 to 3/8 inch in diameter and up to approximately 1.5 inches maximum length with more than about 50% of the pellets being in excess of 3/4 inch in length.

10. The process of claim 9 wherein the particle length of the bagasse particles subjected to pelletization is up to 1.25 times the diameter of the extruded pellet.

11. The process of claim 7 wherein oversize particles from the primary or secondary drying operation are subjected to size reduction and then recombined with the secondary stream.

12. A process for increasing the effectiveness of bagasse as a source of energy in combination with a sugar mill operation in which bagasse from the mill is used as a boiler fuel for the sugar mill operation, comprising:

subjecting a stream of wet bagasse containing coarse and fine particles from the sugar mill to a drying operation in which said bagasse is contacted with a stream of hot flue gases from the boiler and drying said fine particles to a moisture content of about 8-14%, separating the dried fine particles from the coarse particles and densifying said fine particles at a moisture content of about 8-14% into compacted shapes for use as fuel.

13. Fuel pellets produced by the process of claim 12 comprising compressed bagasse particles, in the absence of added binding agent, said pellets being of approximately 1/4 to 3/8 inch in diameter and approximately 1.5 inches maximum length, said pellets having a bulk density of about 40 to 50 pounds per cubic foot with individual pellets having a specific density of about 80 to 90 pounds per cubic foot, and said pellets developing a B.t.u./lb. of about 7500 to 8000 B.t.u./lb. upon burning.