초록 ▼

Methods involve adding sorbent components, such as calcium oxide, alumina, and silica, as well as optional halogens as part of environmental control. Use of the sorbents leads to significant reductions in sulfur and mercury emissions that otherwise would result from burning coal. Use of the sorbents

Methods involve adding sorbent components, such as calcium oxide, alumina, and silica, as well as optional halogens as part of environmental control. Use of the sorbents leads to significant reductions in sulfur and mercury emissions that otherwise would result from burning coal. Use of the sorbents leads to production of waste coal ash that, while higher in mercury, is nevertheless usable as a commercial product because the mercury in the ash is non-leaching and because the coal ash has a higher cementitious nature by virtue of the increased content of the sorbent components in the ash. Thus, the methods involve adding powders having qualities that lead to the production of a cementitious coal ash while at the same time reducing emissions from a coal burning facility.

대표청구항 ▼

1. A method of increasing the value of coal burned in a coal burning facility, the method comprising: combusting coal containing mercury in the presence of at least one sorbent to produce heat energy, ash, and flue gases, said ash containing at least 90% by weight of the mercury originally present i

1. A method of increasing the value of coal burned in a coal burning facility, the method comprising: combusting coal containing mercury in the presence of at least one sorbent to produce heat energy, ash, and flue gases, said ash containing at least 90% by weight of the mercury originally present in the coal, said ash having a concentration of acid leachable mercury that is less than a concentration of acid leachable mercury in an ash produced by combusting the coal without the at least one sorbent;monitoring said flue gases for said mercury and adjusting the presence of the at least one sorbent to achieve a desired mercury emission to comply with an environmental regulation; andrealizing a monetary savings by an avoidance of disposal costs of said fly ash produced. 2. The method according to claim 1 further comprising reflecting said monetary savings on one or more financial statements. 3. The method according to claim 2, wherein said financial statements are at least one of a tax return, a balance sheet, a cash flow analysis, a shareholder equity statement, and an income statement. 4. The method according to claim 1 further comprising calculating a net savings per unit of coal burned. 5. The method according to claim 4 further comprising offsetting a cost of at least one of said coal and said at least one sorbent with a said net savings per unit of coal burned. 6. The method according to claim 1, wherein said monetary savings from said presence of said at least one sorbent increases the value of said coal that is combusted by at least 50%. 7. The method according to claim 1, wherein said monetary savings from said presence of said at least one sorbent is greater than a cost of said presence of said at least one sorbent. 8. The method according to claim 1, wherein said at least one sorbent comprises at least one of CaO, SiO2, Al2O3, Fe2O3, Na2O, and K2O. 9. The method according to claim 1, wherein said coal burning facility is an electric utility plant. 10. The method according to claim 1, wherein said coal burning facility is a cement plant. 11. The method according to claim 1 further comprising creating mercury emissions trading credits. 12. A method of operating a coal burning facility comprising: combusting coal in a furnace and in the presence of a sorbent composition; andgenerating energy by the combusting coal;wherein said sorbent composition is at least one of added onto said coal prior to said combusting, applied into said furnace during said combusting and applied into flue gases downstream of said furnace,wherein said presence of said sorbent composition reduces emissions of at least one of mercury and sulfur compared to combusting coal without said sorbent composition, andwherein said presence of said sorbent composition produces a coal ash more cementitious in nature compared to a coal ash produced from combusting coal without said presence of said sorbent composition. 13. The method according to claim 12 further comprising selling said energy. 14. The method according to claim 13, wherein said energy is electricity. 15. The method according to claim 12, wherein said combusting coal in said presence of said sorbent composition increases a power generation per unit of coal burned as compared to combusting coal without said presence of said sorbent composition. 16. The method according to claim 12, wherein said sorbent composition comprises at least one of CaO, SiO2, Al2O3, Fe2O3, Na2O, and K2O. 17. The method according to claim 12 further comprising using said energy in the production of cement. 18. A method of operating a coal plant to produce energy and waste ash, the method comprising: burning coal in the presence of a sorbent composition to produce a waste ash with a reduced concentration of acid leachable mercury when compared to the concentration of acid leachable mercury in the waste ash produced from burning coal without the sorbent composition;recovering the waste ash having a reduced concentration of acid leachable mercury; andmixing it with cementitious powder to make a cement product. 19. The method according to claim 18 further comprising selling said cement product into a commercial market. 20. The method according to claim 18, wherein said cementitious powder is at least one of a Portland cement, a pozzolan material, a slag, and a cement kiln dust. 21. The method according to claim 18 further comprising creating mercury emissions trading credits. 22. The method according to claim 18, wherein said sorbent composition comprises at least one of CaO, SiO2, Al2O3, Fe2O3, Na2O, and K2O. 23. A method of operating a coal burning plant to produce heat energy and fly ash, the method comprising: burning coal in the presence of at least one sorbent that increases a concentration of a heavy metal in the fly ash and that decreases a concentration of acid leachable heavy metal in the fly ash when compared to the concentration of heavy metal and the concentration of acid leachable heavy metal in the fly ash produce by burning the coal without said at least one sorbent; andselling said fly ash as an industrial raw material. 24. The method according to claim 23 further comprising producing electricity. 25. The method according to claim 24 further comprising selling said electricity. 26. The method according to claim 23 further comprising using said heat energy in producing cement. 27. The method according to claim 26 further comprising selling said cement. 28. The method according to claim 23, wherein said at least one sorbent comprises at least one of CaO, SiO2, Al2O3, Fe2O3, Na2O, and K2O.