초록 ▼

Refuse derived fuel is produced by taking raw refuse, pulverizing it and n screening it to remove fines and oversize material, the screened residue being passed to an air classifier where the light fraction, rich in paper and plastics, is separated. This light combustible refuse fraction is then pa

Refuse derived fuel is produced by taking raw refuse, pulverizing it and n screening it to remove fines and oversize material, the screened residue being passed to an air classifier where the light fraction, rich in paper and plastics, is separated. This light combustible refuse fraction is then passed to a densifying machine, either directly or via a secondary shredder, to produce partially compacted material which is then dried in a rotary dryer. The dried material can be passed to a second densifying machine which produces pellets in the form of small dense cylinders or blocks having a calorific value equal to about half that of coal. Coal dust or other combustible particulate material can be added to and mixed with the combustible fraction between the two densifying machines.

대표청구항 ▼

1. In a process of producing fuel from raw refuse material comprising the steps of: subjecting the material to a dry separating step to separate therefrom a light moist combustible fraction having a moisture content not greater than 40% by weight; subsequently partially compacting the thus separ

1. In a process of producing fuel from raw refuse material comprising the steps of: subjecting the material to a dry separating step to separate therefrom a light moist combustible fraction having a moisture content not greater than 40% by weight; subsequently partially compacting the thus separated light moist combustible material in a first densifying step; and drying the thus separated light moist combustible material, to a moisture content of from 10 to 25% by weight, by passing air through the said material, the improvement which comprises carrying out said drying step after said partial compaction step whereby said light moist combustible material is in a partially compacted state when it is air dried in said drying step. 2. A process according to claim 1 wherein the first densifying step results in a partially compacted material having a bulk density of from 200 to 350 Kgm -3 . 3. A process according to claim 2 wherein the first densifying step results in a partially compacted material having a bulk density of from 310 to 330 Kgm -3 . 4. A process according to claim 1 wherein the partially compacted material is dried in a rotary drier. 5. A process according to claim 1 wherein the partially compacted material is dried to a moisture content of from 15 to 20% by weight. 6. A process according to claim 5 wherein the partially compacted material is dried to a moisture content of about 171/2% by weight. 7. A process according to claim 1 wherein the partially compacted and dried material is thereafter further compacted in a second densifying step. 8. A process according to claim 7 wherein said second densifying step forms solid fuel pellets, the bulk density of the solid fuel pellets resulting from the second densifying step being from 350 to 850 Kgm -3 . 9. A process according to claim 8 wherein the bulk density of the solid fuel pellets resulting from the second densifying step is from 450 to 550 Kgm -3 . 10. A process according to claim 7 wherein at least one of the densifyng steps comprises compacting the material being processed by forcing it through a screen. 11. A process according to claim 7 wherein other combustible material is added to and mixed with the partially compacted combustible fraction of the refuse material between the first and second densification steps. 12. A process according to claim 11 wherein the other combustible material is added after the drying step. 13. A process according to claim 12 wherein the said other combustible material is coal dust. 14. A process according to claim 13 wherein the coal dust is screened to a size less than 1/4 inch prior to addition to the refuse material. 15. A process according to claim 1 wherein the refuse is shredded prior to the first densifying step. 16. A process according to claim 1 wherein the dry separating step is carried out in an air classifier. 17. In an apparatus for producing fuel from raw refuse material of the type comprising means for subjecting the material to a dry separating step to separate a light moist combustible fraction therefrom, a first densifying machine for partially compacting the thus separated light moist combustible material, and a drying device adapted to pass air through the thus separated light moist combustible material to dry said material to a moisture content of from 10 to 25% by weight, the improvement which comprises so arranging said first densifying machine and said drying device relative to one another and relative to the passage of said material thereto that said material is compacted by said first densifying machine prior to the drying of said partially compacted material by said drying device. 18. Apparatus according to claim 17 wherein the drying device is a rotary drier. 19. Apparatus according to claim 17 comprising a second densifying machine for compacting further the dried material received from the drying machine. 20. Apparatus according to claim 19 wherein at least one of the densifying machines comprises a die screen and rollers arranged to cause material to be densified to be forced through the screen. 21. Apparatus according to claim 17 including a shredder for shredding material being fed to the first densifying machine. 22. Apparatus according to claim 19 including, between the first and the second densifying machine, means for adding other combustible material in particulate form to the combustible fraction, and means for mixing the combustible fraction and the other combustible material. 23. Apparatus according to claim 1 wherein the means for adding other combustible material is downstream of the drying device.