Synthetic fuel pellet and methods

Abstract
The present invention includes a synthetic fuel pellet, the pellet comprising a compressed agglomeration of: (a) coal fines; (b) a fibrous cellulosic material wherein the fibers of the fibrous cellulosic material have been substantially disintegrated; and (c) at least one binder, the binder adapted to form a pellet of the coal fines and the fibrous cellulosic material.
Description
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

In accordance with the foregoing summary, the following describes a preferred embodiment of the invention which is presently considered to be the best mode thereof.


To prepare a synthetic fuel pellet in accordance with one embodiment of the present invention, a mixture of: (a) coal fines; (b) a fibrous cellulosic material wherein the fibers of the fibrous cellulosic material have been substantially disintegrated; and (c) at least one binder, the binder adapted to form a pellet of the coal fines and the fibrous cellulosic material.


The fibrous cellulosic material is obtained by subjecting wood chips or other acceptable source of cellulosic material, such as that derived from waste digesters, to pneumatic shear so as to disintegrate the cellulosic fibers. This may be done by obtaining the mechanical or pneumatic shear-treated material commercially, such as the kinetic disintegration technology commercially available from Alternative Green Energy Systems Inc. (AGES) of Canada or First American Scientific Corporation of Bakersfield, Calif. Examples of devices capable of performing this method are the KDS Model 250 and KDS Model 3000 (in development), commercially available from First American Scientific Corporation of Bakersfield, Calif. Another source is municipal waste autoclaving, such as is commercially available from Estech USA LLC of Canal Winchester, Ohio.


The fibrous cellulosic material is typically first mixed with the cellulose binder in a suitable industrial charger as is known and used in the art. Mixing is continued until a uniform slurry is formed.


The coal fines are obtained from on-going or past coal mining operations, such as from waste ponds. The coal fines are collected and permitted to dry before being incorporated into the slurry. The coal fines are admixed to form a mixture with the coal fines binder that is prepared to be pelletized.


The mixture may be formed into pellets using machinery and methods known and used in the art, or which hereafter may be developed.


The pellets are articles of commerce that can be easily transported by rail or shipped from the palletizing operation to combustion chambers, such as for energy generation at electric generating plants. Because electric generating plants are often geographically separated from the mining operations, the pellets must be durable to provide stability during transport. The pellets are typically crushed just prior to feeding the combustion chamber.


EXAMPLES
Coal Fines Binder Step.

It is essential that the binder be non-water-soluble. While there are numerous such binders commercially available, one of the less expensive options appears to be that of a highly-hydrolyzed grade of polyvinyl alcohol (PVOH) such as Elvanol 90-50 (commercially available from Dupont). This material provides a high degree of cold-water insolubility, and its use as a binder is well known.


Experimentation with PVOH show that water resistant briquettes can be made with PVOH alone, with addition rates in the range of 0.1-1% (solids ratio), and preferably in the range of 0.1-0.4%.


PVOH also crosslinks with a number of materials, and experiments with crosslinkers have shown that the PVOH does indeed insolubilize, but the crosslinked material has a tendency to gel. Various crosslinkers were tested, ranging from aldehydes to metals. Invariably, as gelation occurs, the structural integrity of the briquette diminishes.


Testing has confirmed that gelation does not occur in alkaline environments. As an example, briquettes were formed with PVOH (using 90-50 Elvanol as an example) at 0.4% addition, and a glyoxol-based crosslinker (Curesan, from BASF), at 0.1% addition. Sufficient alkalinity was added to raise the pH above 8 (with sodium hydroxide), and briquettes were formed at room temperature at about 9000 psi. The briquettes were heated to accelerate drying to ˜200 F. Upon drying, the PVOH and Curesan react and cure. The resulting briquettes were both physically durable and waterproof. The alkaline insolubility of PVOH and coal is described in U.S. Pat. No. 6,709,472, which is hereby incorporated herein by reference.


Cellulose binder

Several reaction pathways are available to produce “waterproof” cellulose. One pathway teaches that waterproof cellulose composites can be created using a thermoset binder extracted from (wood) cellulose by prescribed steam treatments: the steam hydrolyzes cellulose components which, after concentration, can be utilized as a glue or binder by thermosetting with heat and pressure.


Another pathway utilizes a Maillard reaction to bind “particulated” cellulose, such as that found in the preferred feedstocks of this patent. U.S. Pat. No. 5,582,682 to Ferretti (hereby incorporated herein by reference) regarding forming cellulose composites, teaches that the Maillard reaction resin is compatible with the surface of cellulose, and the particulation increases the binding site population with which the resin reacts. This patent also describes the ammoniation/protein (starch) binder for cellulose.


Indeed, experimentations have demonstrated that a water insoluble material can be formed from fibers derived from the autoclave processing of municipal waste (previously cited). In one experiment, a 50 gram sample of fiber (available from Estech USA LLC of Canal Winchester, Ohio) was combined with 50 grams of 2% ammonia (a commercial home product) and 20 grams of soy protein isolate, briquetted at under 100 psi, and heated cause the briquette core to rise to 350 F. The resulting briquette was porous, but insoluble.


Combined Binder

A synthetic coal briquette was made using techniques identical or similar to those outlined above. 70 grams of coal, along with its binder, and 30 grams of cellulose, along with its binder, were combined and briquetted using standard briquetting techniques at a pressure of about 10,000 psi. The resulting briquette was heated briefly to 350 degrees F. While not wishing to be bound by theory, prior work with the coal/PVOH system has shown that heating a stronger briquette, and indeed, the resulting synthetic fuel briquette was strong and did not dissolve after in 24 hours in water.


Additional information regarding the formulation and production of synthetic fuel pellets is provided in the following patents and published patent applications which are hereby incorporated by reference:













Patent/Publication Number
Title







3,954,443
Aluminum process


4,025,596
Method for pelletizing finely divided solids


4,152,119
Briquette comprising caking coal and



municipal solid waste


4,219,519
Method for agglomerating carbonaceous



fines


4,225,457
Briquette comprising caking coal and



municipal solid waste


4,234,320
Process for the agglomeration of solids


4,243,393
Coal article


4,357,145
Carbonaceous pellets and method of



making


4,369,054
Fiber/slag composition


4,385,995
Method of recovering and using fine coal


4,395,265
Fuel pellets


4,396,396
Deashing of coal by the oil agglomeration



process


4,398,917
Process for the preparation of fuel pellets


4,405,331
Refuse derived fuel and a process for the



production thereof


4,417,899
Self-bursting coal pellets and a method of



making them


4,483,840
Synthetic carbonaceous granules having



high mechanical characteristics


4,494,962
Fuel Product


4,497,661
Formed briquettes, process for forming the



same and process for utilizing the same in



the manufacture of metals


4,501,593
Process for the production of



agglomerated fuels


4,529,439
Energy conservation during the smelting of



ores


4,615,712
Fuel agglomerates and method of



agglomeration


4,670,240
Energy conservation during the smelting of



ores


4,681,597
Method for agglomerating powdered coal



by compaction


4,720,346
Flocculation processes


4,741,278
Solid fuel and a process for its combustion


4,802,890
Agglomeration of coal fines


4,828,573
Method of manufacturing a pelletized fuel


4,830,637
Preagglomeration of fine coal before



thermal dryer in a preparation plant


4,943,378
Flocculation processes


4,981,494
Water-resistant fuel agglomerate, process



for preparing it and composition of matter



employed in the process


5,171,781
Polymeric compositions


5,242,470
Pelletizing coal or coke with starch



particles


5,298,040
Process for the preparation of a water-



resistant fuel agglomerate


5,371,194
Biomass derived thermosetting resin


5,411,560
Method of producing binderless pellets



from low rank coal


5,421,838
Binding composition for the preparation of



a novel agglomerate based on finely



divided materials, process using the said



composition and thus obtained



agglomerate


5,429,645
Solid fuel and process for combustion of



the solid fuel


5,431,702
Waste conversion process and products


5,562,743
Binder enhanced refuse derived fuel


5,589,118
Process for recovering iron from iron-



containing material


5,658,357
Process for forming coal compact without



a binder


5,685,153
Efficient utilization of chlorine and/or



moisture-containing fuels and wastes


5,698,007
Process for agglomerating particulate



material


5,711,768
Sewage sludge disposal process and



product


5,738,694
Process for recovering iron from iron-



containing material


5,743,924
Pelletized fuel composition and method of



manufacture


5,752,993
Blast furnace fuel from reclaimed



carbonaceous materials and related



methods


5,797,972
Sewage sludge disposal process and



product


5,807,420
Process for reduction of iron with solid fuel



objects as amended by exam


5,916,826
Pelletizing and briquetting of coal fines



using binders produced by liquefaction of



biomass


5,922,261
Process for recovering iron from iron-rich



material


6,013,116
Briquette binder composition


6,015,527
Facility for producing reduced iron


6,071,325
Binder composition and process for



agglomerating particulate material


6,099,770
Method of and apparatus for dewatering



and pelletizing particulate fuel


6,165,238
Fuel pellet and method for its production


6,214,064
Process for making a fuel product from



coal fines and sewage sludge


6,284,017
Method and facility for producing reduced



iron


6,375,447
Apparatus for dewatering and pelletizing



particulate fuel


6,384,126
Binder formulation and use thereof in



process for forming mineral pellets having



both low and high temperature strength


6,451,092
System and process for agglomeration



and processing of carbonaceous fines and



dust


6,506,223
Pelletizing and briquetting of combustible



organic-waste materials using binders



produced by liquefaction of biomass


6,530,966
Coal binder compositions and methods


6,558,442
Synthetic fuel production method


6,685,761
Method for producing beneficiated titanium



oxides


6,692,544
Municipal waste briquetting system and



method of filling land


6,709,472
Insolubly bound particulate products


6,786,949
Method and apparatus for using a pre-jel



for producing self-reducing agglomerates


20010013197
Pelletizing and briquetting of combustible



organic-waste materials using binders



produced by liquefaction of biomass


20020014155
System and process for agglomeration



and processing of carbonaceous fines and



dust


20020020109
Synthetic fuel production method


20020050094
Synthetic fuel and methods for producing



synthetic fuel


20020170388
Method for using a pre-jel for producing



self-reducing agglomerates


20030041509
Synthetic fuel comprising coal dust, water



and a reactive organic compound, and a



process for making such synthetic fuel


20040010968
Synthetic Fuel Production Method


20040049973
Synthetic fuel production method


20050132643
Methods for binding particulate solids


20050183544
Method for producing mineral ore



agglomerates using a hemicellulose binder



and associated products


20050274224
Method and apparatus for carrying out a



metallurgical process








Claims
  • 1. A synthetic fuel pellet, said pellet comprising a compressed agglomeration of: a. coal fines;b. a fibrous cellulosic material wherein the fibers of said fibrous cellulosic material have been substantially disintegrated; andc. at least one binder, said binder adapted to form a pellet of said coal fines and said fibrous cellulosic material.
  • 2. A synthetic fuel pellet according to claim 1 wherein said at least one binder comprises a plasticized organic material.
  • 3. A synthetic fuel pellet according to claim 1 wherein said at least one binder comprises nylon.
  • 4. A synthetic fuel pellet according to claim 1 wherein said at least one binder comprises polyvinyl alcohol.
  • 5. A synthetic fuel pellet according to claim 4 wherein said polyvinyl alcohol is present in said pellet in the range of from about 0.1% to about 1% of solids.
  • 6. A synthetic fuel pellet according to claim 1 wherein at least one binder is substantially free of epoxy resins.
  • 7. A synthetic fuel pellet according to claim 1 wherein at least one binder is adapted to make said fibrous cellulosic material substantially waterproof.
  • 8. A synthetic fuel pellet according to claim 1 wherein said binder includes a thermoset binder derived from steam treatment of cellulose.
  • 9. A synthetic fuel pellet according to claim 1 wherein said binder includes a Maillard reaction resin.
  • 10. A synthetic fuel pellet according to claim 1 wherein said at least one binder comprises polyvinyl alcohol, and a binder selected from the group consisting of Maillard reaction resins and thermoset binders derived from steam treatment of cellulose.
  • 11. A synthetic fuel pellet according to claim 1 wherein the percent by weight ratio of the coal fines to the fibrous cellulosic material is in the range of from about 10 to 1 to about 2 to 1.
  • 12. A synthetic fuel pellet according to claim 1 wherein said coal fines are present in an amount in the range of from about 70 to about 90 percent by weight of said pellet.
  • 13. A synthetic fuel pellet according to claim 1 wherein said fibrous cellulosic material is present in an amount in the range of from about 10 to about 30 percent by weight of said pellet.
  • 14. A synthetic fuel pellet according to claim 1 wherein said fibrous cellulosic material has an average fiber length in the range of from about 0.5 to about 4.0 millimeters.
  • 15. A synthetic fuel pellet according to claim 1 wherein the fibers of said fibrous cellulosic material have been has been subjected to pneumatic or mechanical fibril disintegration prior to being incorporated into said compressed agglomeration.
  • 16. A synthetic fuel pellet, said pellet comprising a compressed agglomeration of: a. coal fines;b. a fibrous cellulosic material wherein the fibers of said fibrous cellulosic material have been substantially disintegrated; andc. at least one binder, said binder adapted to render said fibrous cellulosic material substantially waterproof and to form a pellet of said coal fines and said fibrous cellulosic material.
  • 17. A method of preparing a synthetic fuel pellet, said method comprising the steps of: a. bringing into contact a mixture of: i. coal fines;ii. a fibrous cellulosic material wherein the fibers of said fibrous cellulosic material have been substantially disintegrated; andiii. at least one binder, said binder adapted to render said fibrous cellulosic material substantially waterproof and to form a pellet of said coal fines and said fibrous cellulosic material; andb. compressing said mixture for sufficient time to form a pellet.
  • 18. A method according to claim 18 wherein said compression is at a pressure below about 10,000 pounds per square inch.
  • 19. A method according to claim 18 wherein said compression is carried out at a temperature below about 400 degrees Fahrenheit.
  • 20. A method according to claim 18 wherein said at least one binder is first admixed with said fibrous cellulosic material prior to forming said mixture by the addition of said coal fines.
  • 21. A method of preparing a synthetic fuel pellet, said method comprising the steps of: a. bringing into contact a mixture of: i. coal fines;ii. a fibrous cellulosic material wherein the fibers of said fibrous cellulosic material have been substantially disintegrated by pneumatic or mechanical fibril disintegration; wherein said coal fines are present in an amount in the range of from about 70 to about 90 percent by weight of said mixture; andwherein said fibrous cellulosic material is present in an amount in the range of from about 10 to about 30 percent by weight of said mixture; andiii. at least one binder, said binder adapted to render said fibrous cellulosic material substantially waterproof and to form a pellet of said coal fines and said fibrous cellulosic material; andb. compressing said mixture for sufficient time to form a pellet.
  • 22. A pelletizable mixture for making a synthetic fuel pellet, said pellet mixture comprising: a. coal fines;b. a fibrous cellulosic material wherein the fibers of said fibrous cellulosic material have been substantially disintegrated; and
PRIOR APPLICATION DATA

The present application claims the benefit of provisional patent application Ser. No. 60/795,401, the entire disclosure of all of which are incorporated herein by reference.

Provisional Applications (1)
Number Date Country
60795401 Apr 2006 US