US20170122554A1 - Clean coal electrical generation - Google Patents
Clean coal electrical generation Download PDFInfo
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- US20170122554A1 US20170122554A1 US14/756,972 US201514756972A US2017122554A1 US 20170122554 A1 US20170122554 A1 US 20170122554A1 US 201514756972 A US201514756972 A US 201514756972A US 2017122554 A1 US2017122554 A1 US 2017122554A1
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- Prior art keywords
- coal
- clean
- ground
- ground coal
- solids
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D1/00—Burners for combustion of pulverulent fuel
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/04—Raw material of mineral origin to be used; Pretreatment thereof
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
- C10L5/363—Pellets or granulates
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
- C10L5/366—Powders
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L9/00—Treating solid fuels to improve their combustion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K1/00—Preparation of lump or pulverulent fuel in readiness for delivery to combustion apparatus
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/24—Mixing, stirring of fuel components
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/28—Cutting, disintegrating, shredding or grinding
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/30—Pressing, compressing or compacting
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
- C10L2290/546—Sieving for separating fractions, components or impurities during preparation or upgrading of a fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2201/00—Pretreatment of solid fuel
- F23K2201/10—Pulverizing
- F23K2201/1006—Mills adapted for use with furnaces
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2201/00—Pretreatment of solid fuel
- F23K2201/30—Separating
Definitions
- This invention relates generally to electrical generation systems and more particularly to systems that utilize coal.
- Coal is by far the most cost effective method for producing electricity. In the United States the material (coal) is abundant and easily obtained relative to the many other sources of fuel. The major problem with coal has been the polluting characteristics of coal; but, generally, it is not the coal that pollutes but rather the contaminates within the coal that are released when the coal is burned. This includes sulfur, mercury, silica and others.
- contaminates also increase the cost of energy production by wearing on the electrical generators and associated mechanisms, which shortens their productive lives.
- sand and silica within the coal abrade the piping and collect on the heat exchangers, thereby reducing the effectiveness of the heat exchangers requiring increased coal consumption to generate the same electricity.
- the invention produces a mechanism and method to clean coal of pollutants and contaminates for more efficient use in a coal fired electrical generator.
- Coal generators are well known to those of ordinary skill in the art and include those described in: U.S. Pat. No. 5,003,891, entitled “Pulverized Coal Combustion Method”, issued to Kaneko et al. on Apr. 2, 1991; and, U.S. Pat. No. 3,971,639, entitled “Fluid Bed Coal Gasification” issued to Matthews on Jul. 27, 1996; both of which are incorporated hereinto by reference.
- the mined coal is first ground to a chosen mesh size. It has been found that a size of between 10-100 mesh is optimal although other mesh sizes can be employed in this context.
- the now sized coal, with contaminates, is subjected to a vertical separator which separates pollutants and contaminates from the coal.
- the vertical separator uses air motion to separate the coal from contaminates based upon the specific gravity of the two. Although this separation is not absolute, it does remove the vast majority of the contaminates which greatly increases the effectiveness of the coal, improves the life of the generator mechanisms, and reduces the amount of contaminates being released during the burning of the coal.
- the now cleaned coal is ground to a smaller mesh size and injected, via an airstream, into the boiler of the electrical generator.
- the removed contaminates, being solid in nature, are easily collected and disposed properly.
- the above process uses a series of vertical separators which are each adjusted to address different mesh ranges.
- the ground coal with contaminates are passed over a series of separators/screens in a cascading approach. Coal/contaminates which do not fall through the screen of a first separator fall onto the screen of the second separator; coal/contaminates that don't fall through the screen of the second separator, pass to the third separator, etc., until at the end, the excess is returned to the grinder once more.
- the grinding process does not have to be as controlled allowing the grinder to perform a “general” grind.
- the clean coal is not to be used on site by an electrical generator, but rather, is to be used at a remote generator, even one in a foreign country.
- the ground clean coal is difficult to transport when in the mesh size discussed above.
- the clean coal “dust” is formed into solids, ideally of at least four cubic inches, which allow the clean coal to be easily transported. Upon arriving at the remote electrical generator, the coal can be easily ground into the size appropriate for that generator.
- FIG. 1 diagrams the preferred embodiment of the invention.
- FIG. 2 illustrates the embodiment of the invention in which the cleaned coal is formed into solids and placed into train cars for transport to the coal fired electrical generator.
- FIG. 3 diagrams the embodiment of the invention in which a series of screens are placed in cascading arrangement to classify the coal into various sizes.
- FIG. 1 diagrams the preferred embodiment of the invention.
- coal from coal bin 10 (being mined coal) is ground using grinder 11 to form a first ground coal.
- grinder 11 is adapted to output ground coal within a chosen particle size range.
- This ground coal is communicated to a vertical separator 12 such as those described above to separate the first ground coal into a clean ground coal 13 B and contaminants 13 A. Contaminants 13 A collect 14 , are then removed to be disposed according to their toxicity .
- the clean ground coal 13 B is communicated via duct 16 to a second grinder 15 which grinds the clean ground coal into a second coarseness suitable for use by the coal generator furnace 19 .
- the second clean ground coal is mixed 18 with an air flow 17 prior to being injected into furnace 19 .
- FIG. 1 In the preferred embodiment the operation of FIG. 1 is completely performed within a within a single housing 9 .
- This embodiment is ideal where the coal mine and the power plant are located on a single site.
- FIG. 2 illustrates the embodiment of the invention in which the cleaned coal is formed into solids and placed into train cars for transport to the coal fired electrical generator.
- the ground coal is separated using a vertical separator 22 which communicates the clean ground coal via duct 21 to pelletizer 20 .
- the clean ground coal is to be used off-site requiring transportation, which, in the ground state, would be problematic; but, as “chunks” of at least four cubic inches, is safely and easily transported.
- the clean ground coal is then formed into a solid form using pelletizer 20 which creates solids of at least four cubic inches for ease in transportation.
- the solid formed clean coal is dropped 24 into railroad car 23 for transportation to the coal fired electrical generator (not shown) where the solid formed clean coal is then ground in situ to the size used for that specific genertor.
- the clean ground coal is formed into pellet shapes.
- FIG. 3 diagrams the embodiment of the invention in which a series of screens are placed in cascading arrangement to classify the coal into various sizes.
- the mined coal is stored in bin 30 which feeds grinder 31 , grinding the mined coal into a variety of mesh sizes.
- Grinder 31 feeds the ground coal onto a first separation mechanism 32 A which allows a specified mesh size to fall through to vertical separator 34 A (not shown).
- Coal which is not withdrawn from separation mechanism 32 A cascades onto separation mechanism 32 B (feeding vertical separator 34 B, not shown); the excess coal from separation mechanism 32 B cascades onto separation mechanism 32 C which allows a certain mesh size to fall to vertical separator 34 C, not shown; and the process continues until the final separation mechanism 32 N feeding vertical separator 34 N.
- the clean coal generated by vertical separators 32 A- 32 N is compacted to form the clean ground coal into solids having at least four cubic inches of clean ground coal as described above
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
The invention produces a mechanism and method to clean coal of contaminates/pollutants such as sulfur, mercury, silica, and others, for use in a coal fired electrical generator. The mined coal is first ground to a mesh size and is subjected to a vertical separator which separates contaminates/pollutants from the coal. The now cleaned coal is ground to a smaller mesh size and injected into the boiler of the electrical generator. In some embodiments, the cleaned coal is formed into solids for transport to the coal fired electrical generator.
Description
- This invention relates generally to electrical generation systems and more particularly to systems that utilize coal.
- Coal is by far the most cost effective method for producing electricity. In the United States the material (coal) is abundant and easily obtained relative to the many other sources of fuel. The major problem with coal has been the polluting characteristics of coal; but, generally, it is not the coal that pollutes but rather the contaminates within the coal that are released when the coal is burned. This includes sulfur, mercury, silica and others.
- Further, contaminates also increase the cost of energy production by wearing on the electrical generators and associated mechanisms, which shortens their productive lives. As example, sand and silica within the coal abrade the piping and collect on the heat exchangers, thereby reducing the effectiveness of the heat exchangers requiring increased coal consumption to generate the same electricity.
- To address this problem, there have been a variety of techniques developed which are used to remove contaminates, but these techniques in-and-of-themselves can generate pollutants when the technique uses water or chemicals in the process.
- It is clear there is a need to improve the purity of coal used in the generation of electricity
- The invention produces a mechanism and method to clean coal of pollutants and contaminates for more efficient use in a coal fired electrical generator.
- Coal generators are well known to those of ordinary skill in the art and include those described in: U.S. Pat. No. 5,003,891, entitled “Pulverized Coal Combustion Method”, issued to Kaneko et al. on Apr. 2, 1991; and, U.S. Pat. No. 3,971,639, entitled “Fluid Bed Coal Gasification” issued to Matthews on Jul. 27, 1996; both of which are incorporated hereinto by reference.
- In the process of this invention, the mined coal is first ground to a chosen mesh size. It has been found that a size of between 10-100 mesh is optimal although other mesh sizes can be employed in this context.
- Grinding or milling of materials is well known to those of ordinary skill in the art, including, but not limited to those described in U.S. Pat. No. 4,597,537, entitled “Vertical Mill” issued to Misaka et al. on Jul. 1, 1986; U.S. Pat. No. 5,987,966, entitled “Device for Measuring the Quantity of Coal in a Ball Grinder” issued to Fontanille et al. on Nov. 23, 1999; and U.S. Pat. No. 6,138,585, entitled “Clinker Grinder Seal in Coal-Burning Utility Electrical Power Generation Plant” issued to Racine on Oct. 31, 2000; all of which are incorporated hereinto by reference.
- The now sized coal, with contaminates, is subjected to a vertical separator which separates pollutants and contaminates from the coal. The vertical separator uses air motion to separate the coal from contaminates based upon the specific gravity of the two. Although this separation is not absolute, it does remove the vast majority of the contaminates which greatly increases the effectiveness of the coal, improves the life of the generator mechanisms, and reduces the amount of contaminates being released during the burning of the coal.
- Those of ordinary skill in the art readily recognize a variety of vertical separators which may be used in this context, including, but not limited to that described in: U.S. Pat. No. 9,073,087, entitled “Injector Mechanism” issued to Abbott on Jul. 7, 2015; and, U.S. Pat. No. 5,103,981, entitled “Particle Separator/Classification Mechanism” issued to Abbott et al. on Apr. 14 1992; both of which are incorporated hereinto by reference.
- For use in a coal-fired electrical generator, the now cleaned coal is ground to a smaller mesh size and injected, via an airstream, into the boiler of the electrical generator. The removed contaminates, being solid in nature, are easily collected and disposed properly.
- In some embodiments, the above process uses a series of vertical separators which are each adjusted to address different mesh ranges. In this embodiment, the ground coal with contaminates are passed over a series of separators/screens in a cascading approach. Coal/contaminates which do not fall through the screen of a first separator fall onto the screen of the second separator; coal/contaminates that don't fall through the screen of the second separator, pass to the third separator, etc., until at the end, the excess is returned to the grinder once more.
- In this manner, the grinding process does not have to be as controlled allowing the grinder to perform a “general” grind.
- In some embodiments, the clean coal is not to be used on site by an electrical generator, but rather, is to be used at a remote generator, even one in a foreign country. In this case, the ground clean coal is difficult to transport when in the mesh size discussed above. For transportation, in these situations, the clean coal “dust” is formed into solids, ideally of at least four cubic inches, which allow the clean coal to be easily transported. Upon arriving at the remote electrical generator, the coal can be easily ground into the size appropriate for that generator.
- Those of ordinary skill in the art readily recognize a variety of mechanisms which can be employed to create solids from coal particles, including, but not limited to those described in: U.S. Pat. No. 5,762,656, entitled “Dense Core Charcoal Briquet” issued to Burke et al. on Jun. 9, 1998; U.S. Pat. No. 8,377,153, entitled “Densified Fuel Pellets” issued to Kluko on Feb. 19, 2013; and U.S. Pat. No. 9,096,810 entitled “Method for Producing a Bio-Coal” issued to Hung et al. on Aug. 4, 2015; all of which are incorporated hereinto by reference.
- The invention together with various embodiments will be more fully explained by the accompanying drawings and the following descriptions thereof.
-
FIG. 1 diagrams the preferred embodiment of the invention. -
FIG. 2 illustrates the embodiment of the invention in which the cleaned coal is formed into solids and placed into train cars for transport to the coal fired electrical generator. -
FIG. 3 diagrams the embodiment of the invention in which a series of screens are placed in cascading arrangement to classify the coal into various sizes. -
FIG. 1 diagrams the preferred embodiment of the invention. - In this embodiment, coal from coal bin 10 (being mined coal) is ground using grinder 11 to form a first ground coal. In this embodiment, grinder 11 is adapted to output ground coal within a chosen particle size range.
- This ground coal is communicated to a
vertical separator 12 such as those described above to separate the first ground coal into a clean ground coal 13B andcontaminants 13A. Contaminants 13A collect 14, are then removed to be disposed according to their toxicity . - The clean ground coal 13B is communicated via
duct 16 to asecond grinder 15 which grinds the clean ground coal into a second coarseness suitable for use by thecoal generator furnace 19. The second clean ground coal is mixed 18 with anair flow 17 prior to being injected intofurnace 19. - In the preferred embodiment the operation of
FIG. 1 is completely performed within a within a single housing 9. This embodiment is ideal where the coal mine and the power plant are located on a single site. -
FIG. 2 illustrates the embodiment of the invention in which the cleaned coal is formed into solids and placed into train cars for transport to the coal fired electrical generator. - As with the embodiment described above, the ground coal is separated using a
vertical separator 22 which communicates the clean ground coal viaduct 21 topelletizer 20. In this embodiment, the clean ground coal is to be used off-site requiring transportation, which, in the ground state, would be problematic; but, as “chunks” of at least four cubic inches, is safely and easily transported. - The clean ground coal is then formed into a solid
form using pelletizer 20 which creates solids of at least four cubic inches for ease in transportation. The solid formed clean coal is dropped 24 intorailroad car 23 for transportation to the coal fired electrical generator (not shown) where the solid formed clean coal is then ground in situ to the size used for that specific genertor. - In the ideal embodiment of this technique, the clean ground coal is formed into pellet shapes.
-
FIG. 3 diagrams the embodiment of the invention in which a series of screens are placed in cascading arrangement to classify the coal into various sizes. - The mined coal is stored in
bin 30 which feedsgrinder 31, grinding the mined coal into a variety of mesh sizes. Grinder 31 feeds the ground coal onto afirst separation mechanism 32A which allows a specified mesh size to fall through tovertical separator 34A (not shown). Coal which is not withdrawn fromseparation mechanism 32A, cascades ontoseparation mechanism 32B (feedingvertical separator 34B, not shown); the excess coal fromseparation mechanism 32B cascades ontoseparation mechanism 32C which allows a certain mesh size to fall tovertical separator 34C, not shown; and the process continues until the final separation mechanism 32N feedingvertical separator 34N. - Any coal not removed via the cascade above, is collected and fed back via
duct 33 to thecoal bin 30. - In this manner, a less than
perfect grinder 31 is able to obtain clean coal as outlined above. - In one application, the clean coal generated by
vertical separators 32A-32N is compacted to form the clean ground coal into solids having at least four cubic inches of clean ground coal as described above - It is clear that the present invention provides a highly improved purity of coal to be used in the generation of electricity
Claims (15)
1. A coal fired generator operation comprising the steps of:
a) grinding coal to a first coarseness to form a first ground coal;
b) separating contaminates from the first ground coal using a particle density vertical separator to form a clean ground coal by precipitating the contaminates;
c) grinding the clean ground coal into a second coarseness to form a second ground coal; and,
d) injecting the second ground coal into a boiler adapted to generate electricity.
2. The coal fired generator according to claim 1 , wherein the steps of grinding coal to a first coarseness, separating contaminates from the first ground coal, and grinding the clean ground coal into a second coarseness are all performed within a single housing.
3. The coal fired generator according to claim 1 , further including the step of forming the clean ground coal into solids having at least four cubic inches of clean ground coal.
4. The coal fired generator according to claim 3 , wherein the step of forming the clean ground coal into solids includes the step of forming the clean ground coal into pellet shape.
5. The coal fired generator according to claim 4 , further including the step of transporting the clean coal pellets to the site for grinding the clean ground coal to the second ground coal.
6. The coal fired generator according to claim 5 , wherein the step of transporting the clean coal pellets includes the step of loading the clean coal pellets into a rail-road car.
7. A mechanism to clean coal of contaminates comprising:
a. a container holding mined coal;
b. a first grinder receiving the mined coal and adapted to grind the mined coal to a first coarseness, forming a first ground coal; and,
c. a vertical particle separator receiving the first ground coal and adapted to separate contaminates from the first ground coal to form clean ground coal.
8. The mechanism to clean coal of pollutants according to claim 7 , further including a mechanism adapted to form the clean ground coal into solids having at least four cubic inches of clean ground coal.
9. The mechanism to clean coal of pollutants according to claim 8 , wherein the mechanism adapted to form the clean ground coal into solids forms the clean ground coal into pellet shape solids.
10. The mechanism to clean coal according to claim 9 , further including a conveyor mechanism transporting the pellet shaped solids into a rail-road car.
11. A mechanism used in conjunction with a coal fired generator comprising:
a) a container holding mined coal;
b) a first grinder receiving the mined coal and adapted to grind the mined coal to a first ground coal;
c) N separation systems, each of said separation systems receiving said first ground coal in an cascading series from the prior separation system such that each separation system withdraws a specified size of said first ground coal and delivers said specified size to an associated vertical particle separator such that said vertical particle separator separates contaminates from the first ground coal to produce a clean ground coal.
12. The mechanism used in conjunction with a coal fired generator according to claim 11 , further including a compaction mechanism adapted to form the clean ground coal from the separation systems into solids having at least four cubic inches of clean ground coal.
13. The mechanism used in conjunction with a coal fired generator according to claim 12 , wherein the compaction mechanism adapted to form the clean ground coal into solids forms the clean ground coal into pellet shape solids.
14. The mechanism used in conjunction with a coal fired generator according to claim 13 , further including a conveyor mechanism transporting the pellet shaped solids into a rail-road car.
15. The mechanism used in conjunction with a coal fired generator according to claim 12 , further including:
a) a second grinder receiving the clean ground coal and creating coal of a second size to form second ground coal;
b) a blending mechanism for mixing Blending the second ground coal into an airstream; and,
c) an injector applying the airstream into a boiler of the coal fired generator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US14/756,972 US20170122554A1 (en) | 2015-11-02 | 2015-11-02 | Clean coal electrical generation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US14/756,972 US20170122554A1 (en) | 2015-11-02 | 2015-11-02 | Clean coal electrical generation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20170122554A1 true US20170122554A1 (en) | 2017-05-04 |
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ID=58634435
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US14/756,972 Abandoned US20170122554A1 (en) | 2015-11-02 | 2015-11-02 | Clean coal electrical generation |
Country Status (1)
| Country | Link |
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| US (1) | US20170122554A1 (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3400465A (en) * | 1967-01-26 | 1968-09-10 | Ireland James D | Permeable bed drying process |
| US8157193B2 (en) * | 2009-01-13 | 2012-04-17 | Robbins & Avant Mineral Ventures, Llc | Waterless separation methods and systems for coal and minerals |
| US20140130723A1 (en) * | 2011-07-13 | 2014-05-15 | Promecon Prozess undMesstechnik Conrads GmbH | Device and Method for Controlling The Fuel-Air Ratio in the Combustion of Ground Coal in a Firing System of a Coal-Fired Power Station |
-
2015
- 2015-11-02 US US14/756,972 patent/US20170122554A1/en not_active Abandoned
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3400465A (en) * | 1967-01-26 | 1968-09-10 | Ireland James D | Permeable bed drying process |
| US8157193B2 (en) * | 2009-01-13 | 2012-04-17 | Robbins & Avant Mineral Ventures, Llc | Waterless separation methods and systems for coal and minerals |
| US20140130723A1 (en) * | 2011-07-13 | 2014-05-15 | Promecon Prozess undMesstechnik Conrads GmbH | Device and Method for Controlling The Fuel-Air Ratio in the Combustion of Ground Coal in a Firing System of a Coal-Fired Power Station |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: LOST DUTCHMAN MINES LLC, ARIZONA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:OGRAM, MARK E.;REEL/FRAME:039336/0723 Effective date: 20160721 |
|
| STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |