Process for producing fuel from solid waste

• US 4,113,185 A
• Filed: 06/08/1977
• Issued: 09/12/1978
• Est. Priority Date: 06/08/1977
• Status: Expired due to Term

• Current Assignee: Black Clawson Fibreclaim Incorporated
• Original Assignee: Black Clawson Fibreclaim Incorporated
• Inventors: Marsh, Paul G., Kohlhepp, Dean H.
• Primary Examiner(s): Custer, Jr., Granville Y.
• Application Number:
  US05/804,786
• Time in Patent Office: 461 Days
• Field of Search: 241/21, 241/24, 241/29, 241/30, 241/DIG. 38
• US Class Current: 241/19
• CPC Class Codes: B03B 9/06 specially adapted for refuse
• 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
• CPC Class Codes: Y10S 241/38 Solid waste disposal

Abstract

Municipal refuse is treated to produce fuel particularly useful for the operation of a power generating boiler by a process which is characterized by shredding of the as-received material, separation of the light materials prior to pulping of the heavy materials, and ultimate separation from the pulped materials of the inorganic constituents, after which the remaining slurry of predominantly organic materials is dewatered to produce a particulate fuel. The light materials separated after the initial shredding operation are then directly combind with the dewatered organic residue from the pulping operation to effect further reduction in the moisture content of the resultant mixture. The invention is especially applicable to communities where the garbage and trash are collected separately, with the lights produced by shredding and air classifying the trash being added to the fuel product produced by pulping the garbage.

Claims

1. A process for recovering fuel, as well as other reusable materials, from municipal solid waste which includes paper and other fibrous materials, non-fibrous organic materials, metal, glass and other inorganic materials comprising:

a. dry shredding the waste to pieces of a range of predetermined sizes,

b. separating said shredded refuse by air classification into a light fraction which is predominantly paper and a heavy fraction,

c. treating said heavy fraction to reduce the relatively frangible portions thereof to less than a predetermined particle size by subjecting said heavy fraction in the presence of a liquid to substantial and violent mechanical and hydraulic shear to form a slurry,

d. separating the inorganics in said slurry from the organic material therein,

e. dewatering said organic material to a particulate mass, and

f. combining said particulate mass with said light fraction for use as fuel.

2. A process as defined in claim 1 wherein said particulate mass is dewatered to a moisture content of the order of 50%, and wherein said air classification is so controlled that said light fraction has a moisture content of less than 20%.

3. A process as defined in claim 1 including the step of further shredding said light fraction prior to said step of combining with said dewatered organic material.

4. A process as defined in claim 3 wherein said particle size in said slurry is established by extraction of said slurry through perforations of the order of 1/2 to 11/2 inches in diameter, and wherein said further shredding step is carried out to the extent of reducing said pieces to the same size range as said particle size in said slurry.

5. A process as defined in claim 1 wherein said light fraction comprises between about 30 and 40% by weight of the total refuse.

6. A process as defined in claim 1 wherein said particle size in said slurry is established by extraction of said slurry through perforations of the order of 1/2 to 11/2 inches in diameter.

7. A process as defined in claim 1 which includes the step of separating the waste into a metals-rich fraction and an organics-rich fraction prior to carrying out said steps (a) through (f) on said organics-rich fraction, and which also includes the steps of dry shredding said metals-rich fraction, removing the various metal constituents of said shredded metals-rich fraction, and combining the remainder of said fraction with said heavy fraction of said organics-rich fraction prior to said step (c).

8. A process as defined in claim 1 wherein the solid waste is initially separated into a garbage fraction and a trash fraction, wherein the various metal constituents are removed from said trash fraction prior to carrying out said steps (a) through (f) on said trash fraction, and wherein said garbage fraction and said heavy fraction of said trash fraction are combined prior to said step (c).

9. A process as defined in claim 1 wherein the solid waste is initially separated into a garbage fraction and a trash fraction, wherein the trash fraction is further separated into a metals-rich fraction and an organics-rich fraction, wherein said organics-rich fraction is subjected to said steps (a) through (f), wherein said metals-rich fraction is subjected to dry shredding followed by removal of the various metal constituents thereof, and wherein said garbage fraction and the remainder of said metals-rich fraction are combined with said heavy fraction of said trash fraction prior to said step (c).