Systems and methods for producing engineered fuel feed stocks from waste material
View Patent ↗Systems and methods for producing engineered fuels from solid waste material are described herein. In some embodiments, a method includes receiving a waste stream at a multi-material processing platform and separating the waste stream to remove non-processable waste and marketable recyclables. The method further includes conveying processable materials to a material classification system and incorporating additives to produce an engineered fuel from the constituents of the waste stream.
1. A system, comprising:
a first bunker of waste constituents of a first type separated from a mixed municipal solid waste stream;
a second bunker of waste constituents of a second type separated from the mixed municipal solid waste stream, the waste constituents of the first type being different from the waste constituents of the second type based on at least one of the bulk density of the waste constituents and the chemical composition of the waste constituents;
a densifier configured and disposed to receive the waste constituents of the first and the second types from the first and the second bunkers and to compress the waste constituents of the first type and the waste constituents of the second type to form a densified engineered fuel feed stock; and
a control unit configured to control a rate of withdrawal of a first amount of the waste constituents of the first type from the first bunker based on information associated with a BTU content of the waste constituents of the first type, the control unit configured to control a rate of withdrawal of a first amount of the waste constituents of the second type from the second bunker based on information associated with a BTU content of the waste constituents of the second type.
2. The system of claim 1 , wherein the waste constituents of the first type include hard plastic.
3. The system of claim 2 , wherein the waste constituents of the first type consists essentially of hard plastic.
4. The system of claim 1 , wherein the waste constituents of the first type consists essentially of mixed plastic.
5. The system of claim 1 , wherein the waste constituents of the second type include soft plastic.
6. The system of claim 5 , wherein the waste constituents of the second type consists essentially of soft plastic.
7. The system of claim 1 , wherein the waste constituents of the second type consists essentially of fiber.
8. The system of claim 1 , wherein the densifier is configured and disposed to compress the waste constituents of the first type and the waste constituents of the second type with an additive to form the densified engineered fuel feed stock.
9. The system of claim 8 , wherein the additive is at least one of sodium sesquicarbonate (Trona), sodium bicarbonate, sodium carbonate, zinc ferrite, zinc copper ferrite, zinc titanate, copper ferrite aluminate, copper aluminate, copper manganese oxide, nickel supported on alumina, zinc oxide, iron oxide, copper, copper (I) oxide, copper (II) oxide, limestone, lime, Fe, FeO, Fe 2 O 3 , Fe 3 O 4 , iron filings, CaCO 3 , Ca(OH) 2 , CaCO 3 .MgO, silica, alumina, china clay, kaolinite, bauxite, emathlite, attapulgite, coal ash, egg shells, organic salts, calcium magnesium acetate (CMA), calcium acetate (CA), calcium formate (CF), calcium benzoate (CB), calcium propionate (CP) magnesium acetate (MA), urea, calcium bromide, sodium bromide, ammonium bromide, hydrogen bromide, ammonium sulfate, Lignosulfonate and Ca-montmorillonite.
10. The system of claim 8 , wherein the additive is formulated to reduce emissions of least one of sulfur dioxide (SO 2 ), sulfur trioxide (SO 3 ), nitrogen oxides (NO x ), hydrochloric acid (HCl), mercury (Hg) and non-Hg metals during combustion of the densified engineered fuel feed stock.
11. The system of claim 8 , wherein the additive is a sorbent.
12. The system of claim 1 , wherein the densifier is configured to form a densified engineered fuel feed stock pellet.
13. The system of claim 1 , wherein the waste constituents of the first type are different from the waste constituents of the second type based on the bulk density of the waste constituents.
14. The system of claim 1 , wherein the waste constituents of the first type are different from the waste constituents of the second type based on the chemical composition of the waste constituents.
15. The system of claim 1 , wherein the waste constituents of the first type include soft plastic.
16. The system of claim 1 , wherein the waste constituents of the second type include soft fiber.
17. The system of claim 1 , wherein the densified engineered fuel feed stock has
a hard plastic content of between about 0 wt. % and about 40 wt. %;
a soft plastic content of between about 0 wt. % and about 40 wt. %; and
a fiber content of between about 30 wt. % and about 80 wt. %.
18. The system of claim 1 , further comprising:
a third bunker of waste constituents of a third type separated from the mixed municipal solid waste stream.
19. The system of claim 18 , wherein the waste constituents of the first type consists essentially of hard plastic.
20. The system of claim 18 , wherein the waste constituents of the second type consists essentially of soft plastic.
21. The system of claim 18 , wherein the waste constituents of the third type consists essentially of fiber.
22. The system of claim 1 , further comprising a pre-treatment mechanism configured to treat at least one of the waste constituents of the first type and the waste constituents of the second type prior to being densified.
23. The system of claim 22 , wherein the pre-treatment mechanism is a heater.
24. The system of claim 22 , wherein the pre-treatment mechanism includes a flowing carrier gas, wherein the carrier gas is at least one of air and nitrogen.
25. The system of claim 1 , further comprising a grinder configured to form a granulated engineered fuel feed stock.
26. A system, comprising:
a first bunker of waste constituents of a first type separated from a mixed municipal solid waste stream;
a second bunker of waste constituents of a second type separated from the mixed municipal solid waste stream, the waste constituents of the first type being different from the waste constituents of the second type based on at least one of the bulk density of the waste constituents and the chemical composition of the waste constituents;
a first densifier configured and disposed to receive the waste constituents of the first type from the first bunker and to compress the waste constituent of the first type and an additive to form a densified intermediate material;
a grinder configured and disposed to receive the densified intermediate material from the first densifier and to grind the densified intermediate material;
a second densifier configured and disposed to receive the ground intermediate material from the grinder and the waste constituents of the second type from the second bunker and to compress the ground intermediate material and the waste constituents of the second type to form a densified engineered fuel feed stock; and
a control unit configured to control a rate of withdrawal of a first amount of the waste constituents of the first type from the first bunker based on information associated with a BTU content of the waste constituents of the first type, the control unit configured to control a rate of withdrawal of a first amount of the waste constituents of the second type from the second bunker based on information associated with a BTU content of the waste constituents of the second type.
27. The system of claim 26 , wherein the ground intermediate material has an average particle size less than about ⅜ inch.
28. The system of claim 27 , wherein the ground intermediate material has an average particle size less than about ¼ inch.
29. The system of claim 26 , wherein the densified engineered fuel feed stock has
a hard plastic content of between about 0 wt. % and about 40 wt. %;
a soft plastic content of between about 0 wt. % and about 40 wt. %;
a fiber content of between about 30 wt. % and about 80 wt. %; and
a sorbent content of between about 5 wt. % and about 50 wt. %.
30. The system of claim 29 , wherein the hard plastic content is between about 0 wt. % and about 20 wt. %.
31. The system of claim 29 , wherein the soft plastic content is between about 0 wt. % and about 20 wt. %.
32. The system of claim 29 , wherein the fiber content is between about 30 wt. % and about 60 wt. %.
33. The system of claim 29 , wherein the sorbent content is between about 10 wt. % and about 40 wt. %.
34. The system of claim 26 , wherein the additive is at least one of sodium sesquicarbonate (Trona), sodium bicarbonate, sodium carbonate, zinc ferrite, zinc copper ferrite, zinc titanate, copper ferrite aluminate, copper aluminate, copper manganese oxide, nickel supported on alumina, zinc oxide, iron oxide, copper, copper (I) oxide, copper (II) oxide, limestone, lime, Fe, FeO, Fe 2 O 3 , Fe 3 O 4 , iron filings, CaCO 3 , Ca(OH) 2 , CaCO 3 .MgO, silica, alumina, china clay, kaolinite, bauxite, emathlite, attapulgite, coal ash, egg shells, organic salts, calcium magnesium acetate (CMA), calcium acetate (CA), calcium formate (CF), calcium benzoate (CB), calcium propionate (CP) magnesium acetate (MA), urea, calcium bromide, sodium bromide, ammonium bromide, hydrogen bromide, ammonium sulfate, Lignosulfonate and Ca-montmorillonite.
35. The system of claim 26 , wherein the additive is formulated to reduce emissions of least one of sulfur dioxide (SO 2 ), sulfur trioxide (SO 3 ), nitrogen oxides (NO x ), hydrochloric acid (HCl), mercury (Hg) and non-Hg metals during combustion of the densified engineered fuel feed stock.
36. A system, comprising:
a first bunker of waste constituents of a first type separated from a mixed municipal solid waste stream;
a second bunker of waste constituents of a second type separated from the mixed municipal solid waste stream, the waste constituents of the first type being different from the waste constituents of the second type based on at least one of the bulk density of the waste constituents and the chemical composition of the waste constituents;
a first densifier configured and disposed to receive the waste constituents of the first type from the first bunker and to compress the waste constituent of the first type and an additive to form a densified intermediate material;
a grinder configured and disposed to receive the densified intermediate material from the first densifier and to grind the densified intermediate material;
a second densifier configured and disposed to receive the ground intermediate material from the grinder and the waste constituents of the second type from the second bunker and to compress the ground intermediate material and the waste constituents of the second type to form a densified engineered fuel feed stock; and
a control unit configured to control a rate of withdrawal of a first amount of the waste constituents of the first type from the first bunker based on information associated with a chemical composition of the waste constituents of the first type, the control unit configured to control a rate of withdrawal of a first amount of the waste constituents of the second type from the second bunker based on information associated with a chemical composition of the waste constituents of the second type.
37. The system of claim 36 , wherein the ground intermediate material has an average particle size less than about ⅜ inch.
38. The system of claim 37 , wherein the ground intermediate material has an average particle size less than about ¼ inch.
39. The system of claim 36 , wherein the densified engineered fuel feed stock has
a hard plastic content of between about 0 wt. % and about 40 wt. %;
a soft plastic content of between about 0 wt. % and about 40 wt. %;
a fiber content of between about 30 wt. % and about 80 wt. %; and
a sorbent content of between about 5 wt. % and about 50 wt. %.
40. The system of claim 39 , wherein the hard plastic content is between about 0 wt. % and about 20 wt. %.
41. The system of claim 39 , wherein the soft plastic content is between about 0 wt. % and about 20 wt. %.
42. The system of claim 39 , wherein the fiber content is between about 30 wt. % and about 60 wt. %.
43. The system of claim 39 , wherein the sorbent content is between about 10 wt. % and about 40 wt. %.
44. The system of claim 36 , wherein the additive is at least one of sodium sesquicarbonate (Trona), sodium bicarbonate, sodium carbonate, zinc ferrite, zinc copper ferrite, zinc titanate, copper ferrite aluminate, copper aluminate, copper manganese oxide, nickel supported on alumina, zinc oxide, iron oxide, copper, copper (I) oxide, copper (II) oxide, limestone, lime, Fe, FeO, Fe 2 O 3 , Fe 3 O 4 , iron filings, CaCO 3 , Ca(OH) 2 , CaCO 3 .MgO, silica, alumina, china clay, kaolinite, bauxite, emathlite, attapulgite, coal ash, egg shells, organic salts, calcium magnesium acetate (CMA), calcium acetate (CA), calcium formate (CF), calcium benzoate (CB), calcium propionate (CP) magnesium acetate (MA), urea, calcium bromide, sodium bromide, ammonium bromide, hydrogen bromide, ammonium sulfate, Lignosulfonate and Ca-montmorillonite.
45. The system of claim 36 , wherein the additive is formulated to reduce emissions of least one of sulfur dioxide (SO 2 ), sulfur trioxide (SO 3 ), nitrogen oxides (NO x ), hydrochloric acid (HCl), mercury (Hg) and non-Hg metals during combustion of the densified engineered fuel feed stock.
46. A system, comprising:
a first bunker of waste constituents of a first type separated from a mixed municipal solid waste stream;
a second bunker of waste constituents of a second type separated from the mixed municipal solid waste stream, the waste constituents of the first type being different from the waste constituents of the second type based on at least one of the bulk density of the waste constituents and the chemical composition of the waste constituents;
a densifier configured and disposed to receive the waste constituents of the first and the second types from the first and the second bunkers and to compress the waste constituents of the first type, and the waste constituents of the second type to form a densified engineered fuel feed stock; and
a control unit configured to control a rate of withdrawal of a first amount of the waste constituents of the first type from the first bunker based on information associated with a chemical composition of the waste constituents of the first type, the control unit configured to control a rate of withdrawal of a first amount of the waste constituents of the second type from the second bunker based on information associated with a chemical composition of the waste constituents of the second type.
47. The system of claim 46 , wherein the waste constituents of the first type are different from the waste constituents of the second type based on the bulk density of the waste constituents.
48. The system of claim 46 , wherein the waste constituents of the first type are different from the waste constituents of the second type based on the chemical composition of the waste constituents.
49. The system of claim 46 , wherein the densified engineered fuel feed stock has a hard plastic content of between about 0 wt. % and about 40 wt. %;
a soft plastic content of between about 0 wt. % and about 40 wt. %; and
a fiber content of between about 30 wt. % and about 80 wt. %.
50. The system of claim 46 , wherein the waste constituents of the first type include hard plastic.
51. The system of claim 50 , wherein the waste constituents of the first type consists essentially of hard plastic.
52. The system of claim 46 , wherein the waste constituents of the first type include soft plastic.
53. The system of claim 46 , wherein the waste constituents of the first type consists essentially of mixed plastic.
54. The system of claim 46 , wherein the waste constituents of the second type include soft plastic.
55. The system of claim 54 , wherein the waste constituents of the second type consists essentially of soft plastic.
56. The system of claim 46 , wherein the waste constituents of the second type include fiber.
57. The system of claim 56 , wherein the additive is a sorbent.
58. The system of claim 57 , wherein the densified engineered fuel feed stock has
a hard plastic content of between about 0 wt. % and about 40 wt. %;
a soft plastic content of between about 0 wt. % and about 40 wt. %;
a fiber content of between about 30 wt. % and about 80 wt. %; and
a sorbent content of between about 5 wt. % and about 50 wt. %.
59. The system of claim 57 , wherein the additive is at least one of sodium sesquicarbonate (Trona), sodium bicarbonate, sodium carbonate, zinc ferrite, zinc copper ferrite, zinc titanate, copper ferrite aluminate, copper aluminate, copper manganese oxide, nickel supported on alumina, zinc oxide, iron oxide, copper, copper (I) oxide, copper (II) oxide, limestone, lime, Fe, FeO, Fe 2 O 3 , Fe 3 O 4 , iron filings, CaCO 3 , Ca(OH) 2 , CaCO 3 .MgO, silica, alumina, china clay, kaolinite, bauxite, emathlite, attapulgite, coal ash, egg shells, organic salts, calcium magnesium acetate (CMA), calcium acetate (CA), calcium formate (CF), calcium benzoate (CB), calcium propionate (CP) magnesium acetate (MA), urea, calcium bromide, sodium bromide, ammonium bromide, hydrogen bromide, ammonium sulfate, Lignosulfonate and Ca-montmorillonite.
60. The system of claim 57 , wherein the additive is formulated to reduce emissions of least one of sulfur dioxide (SO 2 ), sulfur trioxide (SO 3 ), nitrogen oxides (NO x ), hydrochloric acid (HCl), mercury (Hg) and non-Hg metals during combustion of the densified engineered fuel feed stock.
61. The system of claim 56 , wherein the waste constituents of the second type consists essentially of fiber.
62. The system of claim 46 , wherein the densifier is configured and disposed to compress the waste constituents of the first type and the waste constituents of the second type with an additive to form the densified engineered fuel feed stock.
63. The system of claim 46 , wherein the densifier is configured to form a densified engineered fuel feed stock pellet.
64. The system of claim 63 , wherein the waste constituents of the first type consists essentially of hard plastic.
65. The system of claim 63 , wherein the waste constituents of the second type consists essentially of soft plastic.
66. The system of claim 63 , wherein the waste constituents of the third type consists essentially of fiber.
67. The system of claim 46 , further comprising:
a third bunker of waste constituents of a third type separated from the mixed municipal solid waste stream.
68. The system of claim 46 , further comprising a pre-treatment mechanism configured to treat at least one of the waste constituents of the first type and the waste constituents of the second type prior to being densified.
69. The system of claim 68 , wherein the pre-treatment mechanism is a heater.
70. The system of claim 68 , wherein the pre-treatment mechanism includes a flowing carrier gas, wherein the carrier gas is at least one of air and nitrogen.
71. The system of claim 46 , further comprising a grinder configured to form a granulated engineered fuel feed stock.