EP2318489B1 - Targeted reagent injection for slag control from combustion of coals high in iron and/or calcium - Google Patents
Targeted reagent injection for slag control from combustion of coals high in iron and/or calcium Download PDFInfo
- Publication number
- EP2318489B1 EP2318489B1 EP09795277.4A EP09795277A EP2318489B1 EP 2318489 B1 EP2318489 B1 EP 2318489B1 EP 09795277 A EP09795277 A EP 09795277A EP 2318489 B1 EP2318489 B1 EP 2318489B1
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- EP
- European Patent Office
- Prior art keywords
- slag
- coal
- reagent
- pounds
- combustor
- Prior art date
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- 239000002893 slag Substances 0.000 title claims description 47
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims description 22
- 239000003153 chemical reaction reagent Substances 0.000 title claims description 19
- 229910052742 iron Inorganic materials 0.000 title claims description 11
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 title claims description 10
- 239000011575 calcium Substances 0.000 title claims description 10
- 229910052791 calcium Inorganic materials 0.000 title claims description 10
- 238000002485 combustion reaction Methods 0.000 title description 11
- 238000002347 injection Methods 0.000 title description 2
- 239000007924 injection Substances 0.000 title description 2
- 239000003245 coal Substances 0.000 claims description 37
- 239000002002 slurry Substances 0.000 claims description 30
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims description 22
- 239000000347 magnesium hydroxide Substances 0.000 claims description 22
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 16
- 230000008569 process Effects 0.000 claims description 14
- 239000000446 fuel Substances 0.000 claims description 6
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 claims description 5
- 239000000567 combustion gas Substances 0.000 claims description 5
- 239000012530 fluid Substances 0.000 claims description 5
- 230000003247 decreasing effect Effects 0.000 claims description 4
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 claims description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims 1
- 238000001816 cooling Methods 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- MXRIRQGCELJRSN-UHFFFAOYSA-N O.O.O.[Al] Chemical compound O.O.O.[Al] MXRIRQGCELJRSN-UHFFFAOYSA-N 0.000 description 11
- 239000000126 substance Substances 0.000 description 11
- 230000008901 benefit Effects 0.000 description 10
- 239000007787 solid Substances 0.000 description 9
- 239000002245 particle Substances 0.000 description 7
- 230000002829 reductive effect Effects 0.000 description 7
- 239000000654 additive Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 238000012546 transfer Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000011084 recovery Methods 0.000 description 3
- 230000000996 additive effect Effects 0.000 description 2
- 229910021502 aluminium hydroxide Inorganic materials 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910001679 gibbsite Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002105 nanoparticle Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 230000001680 brushing effect Effects 0.000 description 1
- YLUIKWVQCKSMCF-UHFFFAOYSA-N calcium;magnesium;oxygen(2-) Chemical compound [O-2].[O-2].[Mg+2].[Ca+2] YLUIKWVQCKSMCF-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 230000001010 compromised effect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- -1 e.g. Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000000116 mitigating effect Effects 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005067 remediation Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C99/00—Subject-matter not provided for in other groups of this subclass
-
- 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/06—Use of additives to fuels or fires for particular purposes for facilitating soot removal
-
- 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/04—Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J3/00—Removing solid residues from passages or chambers beyond the fire, e.g. from flues by soot blowers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J7/00—Arrangement of devices for supplying chemicals to fire
-
- 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2200/00—Components of fuel compositions
- C10L2200/02—Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
- C10L2200/0204—Metals or alloys
- C10L2200/0213—Group II metals: Be, Mg, Ca, Sr, Ba, Ra, Zn, Cd, Hg
-
- 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2200/00—Components of fuel compositions
- C10L2200/02—Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
- C10L2200/0204—Metals or alloys
- C10L2200/0218—Group III metals: Sc, Y, Al, Ga, In, Tl
-
- 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2200/00—Components of fuel compositions
- C10L2200/02—Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
- C10L2200/0254—Oxygen containing compounds
-
- 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/14—Injection, e.g. in a reactor or a fuel stream during fuel production
- C10L2290/141—Injection, e.g. in a reactor or a fuel stream during fuel production of additive or catalyst
-
- 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/18—Spraying or sprinkling
Definitions
- the invention relates to a process that increases the output of a combustor fired with coal having high iron and/or calcium content, by reducing the tendency of slag to form on heat exchange surfaces, changing the nature of the slag to make it easier to remove and actually removing slag.
- the tendency to form slag and the properties of the slag for such high iron content coals have been a major concern of combustion engineers and plant operators for decades.
- Slag accumulation is a problem that causes decreased heat transfer and often leads to long periods of downtime for cleaning.
- US 2006/0121398 A1 deals with an additive atomizing system for injection into severe operating environments.
- a yet further but more specific object is to provide a process to more effectively control slag by decreasing the amount of downtime associated with slag removal.
- the invention provides a process for reducing slag cohesiveness and/or adhesiveness in a combustor, thereby decreasing the rate of fouling as defined in the claim.
- the aluminum trihydroxide reagent is introduced in the form of an aqueous liquid and computational fluid dynamics is employed to determine flow rates and select reagent introduction rates, reagent introduction location(s), reagent concentration, reagent droplet size and/or reagent momentum.
- Magnesium hydroxide is introduced as an aqueous slurry along with the slurry of aluminum trihydroxide.
- Fig. 1 is a schematic view of one embodiment of the invention.
- Fig. 1 shows a large combustor 10 of the type used for producing steam for electrical power generation, process steam, heating or incineration. Coal is fed by burners 20 and 20a and burned with air in a combustion zone 21 .
- coal that is high in iron (e.g., iron contents of greater than 15%, e.g., from 20 to 35%, based on the weight of the ash and expressed as Fe 2 O 3 ) and/or calcium content (e.g., calcium contents of greater than 5%, e.g., from 10 to 25%, based on the weight of the ash and expressed as CaO).
- iron e.g., iron contents of greater than 15%, e.g., from 20 to 35%, based on the weight of the ash and expressed as Fe 2 O 3
- calcium content e.g., calcium contents of greater than 5%, e.g., from 10 to 25%, based on the weight of the ash and
- Air for combustion supplied by fan 22 and ductwork 24, is preferably preheated by a gas-to-gas heat exchangers (not shown) which transfer heat from ductwork (not shown) at the exit end of the combustor.
- Hot combustion gases rise and flow past heat exchangers 26, which transfer heat from the combustion gases to water for the generation of steam.
- Other heat exchangers including an economizer (downstream and not shown) may also be provided according to the design of the particular boiler. Slag left untreated would tend to form on these heat exchanger surfaces, which are positioned within specific combustors based on design considerations important to individual locations.
- modeling techniques such as computational fluid dynamics, are employed to initially direct treatment chemicals (especially, those identified as effective for particular types of coal according to the invention) to the optimum locations for reducing and/or controlling slag buildup and maintaining efficient operation of the boiler.
- a series of suitable, preferably air assisted atomizing, nozzles in each of nozzle banks 30 and 30a are provided for introducing aluminum trihydroxide with magnesium hydroxide slurry from vessels 40 and 40a respectively. Both the ATH and the magnesium hydroxide are aqueous slurries.
- Supply lines e.g., 41
- Valves e.g., 42
- temperature sensors e.g., 44
- Both valves 42 and temperature sensors 44 are connected to controller 46 via electrical leads (e.g., 48) shown in dotted lines.
- the controller 46 can be a general purpose digital computer programmed in accord with a predetermined control regimen with both feed forward and feedback features.
- Aluminum trihydroxide (Al(OH) 3 ), which has been found effective according to the invention for greatly lessening the deposition of slag or cleaning deposited slag from troublesome coal types, is also known under other names such as ATH, aluminum hydroxide and hydrated alumina. Regardless of the form of aluminum trihydroxide raw material, it is preferred that it is mixed with water for introduction from tank 40 through associated lines 41, with or without chemical stabilizers, to concentrations suitable for storage and handling, e.g., at least 25%, and preferably at least 65%, solids by weight.
- the concentration and flow rates will be initially determined by modeling to assure that the proper amount of chemical is supplied to the correct location in the combustor in the correct physical form to achieve the desired results of reduced slagging and ease of clean up.
- it is diluted as determined, e.g ., by computational fluid dynamics (CFD) to within the range of from 0.1 to 10 %, more narrowly from 1 to 5 %.
- CFD computational fluid dynamics
- the aqueous aluminum trihydroxyde contacts the hot gases in the combustor, it is believed to be reduced to very small particles, e.g ., nano-sized particles, e.g ., under 200 nanometers and preferably below 100 nanometers.
- Median particle sizes of from 50 to 150 nanometers are useful ranges for the process of the invention. To approach this size, it is important that the ATH be introduced with water. The small particles are believed to disrupt the normal crystalline or glass that forms the slag. Regardless of the mechanism involved it is a distinct advantage of the invention that the slag that does form is highly friable and breaks easily with brushing and can be crushed by hand.
- the friability of slag that is formed is increased, making it easier to remove.
- the invention also slows or eliminates the buildup of slag.
- the invention can actually remove slag that has already formed.
- increase the friability of the slag it is meant that the slag after treatment requires less force per unit area to crush than slag formed under the same conditions without the treatment.
- remove slag it is meant that the weight of the slag adhering to boiler, particularly heat exchange, surfaces is reduced from initial values by the treatment of the invention.
- the process for most coals works best with a combination of ATH and magnesium hydroxide. While some coals, e.g ., with low silicate compositions can be burned with reduced problems attributed to slag, the use of magnesium hydroxide, at least initially, is preferred.
- the magnesium hydroxide reagent can preferably be prepared from brines containing calcium and other salts, usually from underground brine pools or seawater. Dolomitic lime is mixed with these brines to form calcium chloride solution and magnesium hydroxide which is precipitated and filtered out of the solution. This form of magnesium hydroxide can be mixed with water, with or without stabilizers, to concentrations suitable for storage and handling, e.g ., from 25 to 65% solids by weight.
- CFD computational fluid dynamics
- it is diluted as determined by computational fluid dynamics (CFD) to within the range of from 0.1 to 10%, more narrowly from 1 to 5%.
- CFD computational fluid dynamics
- nano-sized particles e.g ., under 200 nanometers and preferably below 100 nanometers.
- Median particle sizes of from 50 to 150 nanometers are useful ranges for the process of the invention.
- Other forms of MgO can also be employed where necessary or desired, e . g ., "light burn” or "caustic” can be employed where it is available in the desired particle size range.
- the invention will preferably take advantage of CFD to project initial flow rates and select initial reagent introduction rates, reagent introduction location(s), reagent concentration, reagent droplet size and reagent momentum.
- CFD is a well understood science, and it is utilized with full benefit in this case, where it is desired to supply a minimum amount of chemical for maximum effect.
- the initial feed rate for the best economics for combustors operating similar to the one exemplified below can be up to 2.7 kg (6 pounds) of ATH(as dry active ATH) or 3.6 kg (8 pounds) (as a 65-70% slurry) per ton of coal.
- amounts of from 0.45 to 2.7 kg (1 to 6 pounds) of slurry will be effective (more narrowly, e.g ., 0.9 to 1.36 kg (2 to 3 pounds) of slurry).
- amounts of from 0.23 to 0.9 kg (0.5 to 2 pounds) of Mg(OH) 2 slurry per ton of coal, e.g ., from 0.3 to 0.45 kg (0.7 to 1 pounds) of Mg(OH) 2 slurry per ton of coal can be utilized.
- the slurries are diluted as necessary, typically to a solids concentration of from about 5% for smaller applications to 35% or more.
- the weight of the slag adhering to a combustor, particularly heat exchange, surfaces is effectively reduced from initial values by the treatment of the invention, especially when the ATH and Mg(OH) 2 are used at high concentrations within the above ranges, i.e. from 1.36 to 2.7 kg (3 to 6 pounds) of ATH per ton of coal and 0.45 to 0.9 kg (1 to 2 pounds) of Mg(OH) 2 per ton of coal.
- This ability to remove slag provides the ability to provide a cleaning and maintenance regimen wherein the initial dosing is as just mentioned for removing slag, with the dosing then reduced to from 10 to 50% of the initial values for maintaining the combustor clean and operating efficiently.
- combustion catalysts and or effluent treatment chemicals can be added to the fuel, combustion zone or otherwise as described, for example in U. S. Patent No. 7,162,960 to Smyrniotis, et al.
- Al(OH) 3 aluminum trihydroxide slurry or ATH for short
- aqueous slurry at a rate of 2.3 kg (5 pounds) slurry per ton of coal consumed from two banks of three air-cooled nozzles positioned on the wall opposite of two banks of pulverized coal burners - one bank at an elevation between the two burners and one bank at an elevation above the uppermost coal burners.
- the slurry is diluted to a concentration of 35 weight % ATH.
- the density of the ATH slurry before dilution is 6.3 kg/3.8 1 (14 pounds/gallon), meaning that the feed rate is 730.6 1 (193 gallons) per day (2.3 kg (5 pounds) per ton of coal) for ATH slurry.
- an effective feed rate for this particular combustor will be from 0.45 to 2.7 kg (1 to 6 pounds) of ATH slurry per ton of coal, e.g., 0.9 to 1.36 kg (2 to 3 pounds) per ton.
- Example 2 This example illustrates the effect of introducing Mg(OH) 2 (magnesium hydroxide) into a furnace burning 540 tons of coal per day in addition to the aluminum trihydroxide fed in Example 1.
- the coal was a blend of Illinois basin and Appalachian bituminous coals, as illustrated in Example 1.
- the magnesium hydroxide was fed as a slurry at 0.9 kg (2 lbs) of 50 to 60 weight % slurry per ton of coal consumed. Density of the magnesium hydroxide slurry was approximately 5.4 kg/3.8 1 (12 lbs/gallon). Therefore, the feed rate was about 340.7 1 (90 gallons) per day for the Mg(OH) 2 slurry. As before, we fed the aluminum trihydroxide slurry at 2.3 kg (5 pounds) of slurry per ton of coal consumed. The density of the ATH was 6.3 kg/3.8 1 (14 pounds/gallon), making the feed rate 730.6 1 (193 gallons) per day for ATH.
- Fig . 2 is a photograph of a slag sample obtained after operation for 24 hours of ATH feed only. The slag was unexpectedly friable.
Description
- The invention relates to a process that increases the output of a combustor fired with coal having high iron and/or calcium content, by reducing the tendency of slag to form on heat exchange surfaces, changing the nature of the slag to make it easier to remove and actually removing slag.
- Combustion of coal, like other fossil fuels, is invariably less efficient than desired and can be a source of pollution. Maintaining combustor operation at high efficiency and controlling the quality of the emissions is essential for maintaining the energy needed to power our economy while preserving the quality of the air we require for survival. Because efficiency and emissions are interrelated and some technological solutions have been shown to be competitive with each other, it has been difficult to achieve both. Economic operation of power plants and incinerators is in the public interest, and new technologies are essential to this effort.
- Fuel selection plays an important role in mitigating some pollution problems, but it cannot eliminate them. Some coals, such as certain Appalachian and Illinois Basin bituminous coals, are important in many plants designed for coal where economics limits other options. The tendency to form slag and the properties of the slag for such high iron content coals have been a major concern of combustion engineers and plant operators for decades. There are a number of factors that impact the physical and chemical properties of slag. See, for example, Combustion Fossil Power, 1991, Joseph G. Singer, P.E., editor, Chapter 3, Combustion Engineering. However, as the industry stands today, there is a compromise between selection of low-cost coal and the actual economics of energy production where slagging becomes a problem. Slag accumulation is a problem that causes decreased heat transfer and often leads to long periods of downtime for cleaning.
- An interrelated problem with coal is that large amounts of ash and fine particulates are formed that must be captured and disposed of. The art has used additives to control slag formation and properties, but the additives can stress the solids recovery systems employed in terms of sheer volume. Accordingly, optimum slag control has often been compromised because the solids recovery system could not effectively remove all of the solids necessary. This is especially a problem with older plants where increasing the solids collection capacity is not an option.
- Making the problem more complex is the fact that coals react differently to additives as a function of their composition. As a general rule, there are no known formulae that make it possible to address all different coal compositions with suitable additives at effective levels that can be adequately handled by solids recovery equipment. The discovery of individual coal composition and additive regimens are highly sought after to assure that economical power can be supplied while generating sufficient revenues for effective pollution control.
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US 4,498,402 describes a method for reducing high temperature slagging in furnaces and a conditioner fo use therein. -
US 2006/0121398 A1 deals with an additive atomizing system for injection into severe operating environments. - There is a need for an improved process that more effectively control slagging, especially with problem fuels, such as coals with sulfur contents that cause them to play an increased role in slagging and also those having high iron and/or calcium contents, to improve boiler efficiency and economics.
- It is an object of the invention to provide an improved technology for slag control in combustors utilizing fuels tending toward the production of slag.
- It is another object to provide a process to control slag from the combustion of coal with high iron and/or calcium contents while reducing chemical utilization.
- It is another object to provide a process to remove slag from boiler heat exchange surfaces due to the combustion of coal with high iron and/or calcium contents while reducing chemical utilization.
- A yet further but more specific object is to provide a process to more effectively control slag by decreasing the amount of downtime associated with slag removal.
- It is a more specific object of some aspects of the invention to achieve the above objects while at the same time improving combustor efficiency.
- These and other objects are achieved by the present invention in at least its preferred aspects which provides an improved process for slag control in combustors burning slag-forming coal with high iron and/or calcium content.
- In one aspect, the invention provides a process for reducing slag cohesiveness and/or adhesiveness in a combustor, thereby decreasing the rate of fouling as defined in the claim.
- The aluminum trihydroxide reagent is introduced in the form of an aqueous liquid and computational fluid dynamics is employed to determine flow rates and select reagent introduction rates, reagent introduction location(s), reagent concentration, reagent droplet size and/or reagent momentum.
- Magnesium hydroxide is introduced as an aqueous slurry along with the slurry of aluminum trihydroxide.
- Other preferred aspects and their advantages are set out in the description which follows.
- The invention will be better understood and its advantages will become more apparent when the following detailed description is read in conjunction with the accompanying drawings, in which:
-
Fig. 1 is a schematic view of one embodiment of the invention. -
Fig. 2 is a photograph of a slag sample obtained after operation for 24 hours of aluminum trihydroxide into a combustor operated on a high iron content coal as set out in Example 2 below. - Reference will first be made to
Fig. 1 , which is a schematic view of one embodiment of the invention.Fig. 1 shows alarge combustor 10 of the type used for producing steam for electrical power generation, process steam, heating or incineration. Coal is fed byburners combustion zone 21. It is an advantage of the invention that coal that is high in iron (e.g., iron contents of greater than 15%, e.g., from 20 to 35%, based on the weight of the ash and expressed as Fe2O3) and/or calcium content (e.g., calcium contents of greater than 5%, e.g., from 10 to 25%, based on the weight of the ash and expressed as CaO). It is also an advantage of the invention that slag can be effectively controlled even for coals having significant sulfur contents, e.g., above 1% and in the range of from 3 to 5%. Here, and throughout this description, all parts and percentages are by weight. - Air for combustion, supplied by
fan 22 andductwork 24, is preferably preheated by a gas-to-gas heat exchangers (not shown) which transfer heat from ductwork (not shown) at the exit end of the combustor. Hot combustion gases rise and flowpast heat exchangers 26, which transfer heat from the combustion gases to water for the generation of steam. Other heat exchangers, including an economizer (downstream and not shown) may also be provided according to the design of the particular boiler. Slag left untreated would tend to form on these heat exchanger surfaces, which are positioned within specific combustors based on design considerations important to individual locations. It is an advantage of the present invention that modeling techniques, such as computational fluid dynamics, are employed to initially direct treatment chemicals (especially, those identified as effective for particular types of coal according to the invention) to the optimum locations for reducing and/or controlling slag buildup and maintaining efficient operation of the boiler. - A series of suitable, preferably air assisted atomizing, nozzles in each of
nozzle banks vessels valves 42 andtemperature sensors 44 are connected tocontroller 46 via electrical leads (e.g., 48) shown in dotted lines. These valves, temperature sensors and leads are illustrative only, and the skilled worker using the principles outlined herein will place them strategically to provide appropriate control signals and responses. Thecontroller 46 can be a general purpose digital computer programmed in accord with a predetermined control regimen with both feed forward and feedback features. - Aluminum trihydroxide (Al(OH)3), which has been found effective according to the invention for greatly lessening the deposition of slag or cleaning deposited slag from troublesome coal types, is also known under other names such as ATH, aluminum hydroxide and hydrated alumina. Regardless of the form of aluminum trihydroxide raw material, it is preferred that it is mixed with water for introduction from
tank 40 through associatedlines 41, with or without chemical stabilizers, to concentrations suitable for storage and handling, e.g., at least 25%, and preferably at least 65%, solids by weight. - As will be described, the concentration and flow rates will be initially determined by modeling to assure that the proper amount of chemical is supplied to the correct location in the combustor in the correct physical form to achieve the desired results of reduced slagging and ease of clean up. For use in the process, it is diluted as determined, e.g., by computational fluid dynamics (CFD) to within the range of from 0.1 to 10 %, more narrowly from 1 to 5 %. When the aqueous aluminum trihydroxyde contacts the hot gases in the combustor, it is believed to be reduced to very small particles, e.g., nano-sized particles, e.g., under 200 nanometers and preferably below 100 nanometers. Median particle sizes of from 50 to 150 nanometers are useful ranges for the process of the invention. To approach this size, it is important that the ATH be introduced with water. The small particles are believed to disrupt the normal crystalline or glass that forms the slag. Regardless of the mechanism involved it is a distinct advantage of the invention that the slag that does form is highly friable and breaks easily with brushing and can be crushed by hand.
- It is a significant advantage of the invention that the friability of slag that is formed is increased, making it easier to remove. The invention also slows or eliminates the buildup of slag. Advantageously, at high doses, the invention can actually remove slag that has already formed. By the term "increase the friability of the slag" it is meant that the slag after treatment requires less force per unit area to crush than slag formed under the same conditions without the treatment. By the term "remove slag" it is meant that the weight of the slag adhering to boiler, particularly heat exchange, surfaces is reduced from initial values by the treatment of the invention. There are several additional and attendant advantages of the invention, including the reduction of SO3 for high sulfur coals, the reduction of the pressure drop across heat exchange apparatus, the ability to use lower cost coal, lower CO generation, lower CO2 generation due to increased fuel consumption, better heat transfer, less down time, higher throughput, cleaning on line, cleaner heat exchange surfaces, ability to clean the whole combustor, and the ability to run at all loads with greater efficiency.
- The process for most coals works best with a combination of ATH and magnesium hydroxide. While some coals, e.g., with low silicate compositions can be burned with reduced problems attributed to slag, the use of magnesium hydroxide, at least initially, is preferred. The magnesium hydroxide reagent can preferably be prepared from brines containing calcium and other salts, usually from underground brine pools or seawater. Dolomitic lime is mixed with these brines to form calcium chloride solution and magnesium hydroxide which is precipitated and filtered out of the solution. This form of magnesium hydroxide can be mixed with water, with or without stabilizers, to concentrations suitable for storage and handling, e.g., from 25 to 65% solids by weight. For use in the process, it is diluted as determined by computational fluid dynamics (CFD) to within the range of from 0.1 to 10%, more narrowly from 1 to 5%. When it contacts the effluent in combustor, it is believed reduced to nano-sized particles, e.g., under 200 nanometers and preferably below 100 nanometers. Median particle sizes of from 50 to 150 nanometers are useful ranges for the process of the invention. Other forms of MgO can also be employed where necessary or desired, e.g., "light burn" or "caustic" can be employed where it is available in the desired particle size range.
- To best achieve these effects, the invention will preferably take advantage of CFD to project initial flow rates and select initial reagent introduction rates, reagent introduction location(s), reagent concentration, reagent droplet size and reagent momentum. CFD is a well understood science, and it is utilized with full benefit in this case, where it is desired to supply a minimum amount of chemical for maximum effect.
- It is noted as highly significant that the amount of chemical will be substoichiometric in terms of affecting the fusion point of the slag - often considered to be the controlling factor in slag control. According to the present invention, there is good evidence besides the relatively small amount of reagent employed that the results of the invention are due to a physical disruption of slag formation with possible boundary chemical and kinetic effects not explained by the literature.
- Testing has shown that initial feed rates determined by CFD can be utilized with good effect and then adjusted based on observed results. As a guide to feed rates, the initial feed rate for the best economics for combustors operating similar to the one exemplified below can be up to 2.7 kg (6 pounds) of ATH(as dry active ATH) or 3.6 kg (8 pounds) (as a 65-70% slurry) per ton of coal. For example, when added as a preferred 70% slurry, amounts of from 0.45 to 2.7 kg (1 to 6 pounds) of slurry will be effective (more narrowly, e.g., 0.9 to 1.36 kg (2 to 3 pounds) of slurry). Also used are up to 0.9 kg (2 pounds) of Mg(OH)2 slurry (at about 50 - 60 % solids) per ton of coal. For example, when added as a preferred 60% slurry, amounts of from 0.23 to 0.9 kg (0.5 to 2 pounds) of Mg(OH)2 slurry per ton of coal, e.g., from 0.3 to 0.45 kg (0.7 to 1 pounds) of Mg(OH)2 slurry per ton of coal can be utilized. The slurries are diluted as necessary, typically to a solids concentration of from about 5% for smaller applications to 35% or more.
- The weight of the slag adhering to a combustor, particularly heat exchange, surfaces is effectively reduced from initial values by the treatment of the invention, especially when the ATH and Mg(OH)2 are used at high concentrations within the above ranges, i.e. from 1.36 to 2.7 kg (3 to 6 pounds) of ATH per ton of coal and 0.45 to 0.9 kg (1 to 2 pounds) of Mg(OH)2 per ton of coal. This ability to remove slag provides the ability to provide a cleaning and maintenance regimen wherein the initial dosing is as just mentioned for removing slag, with the dosing then reduced to from 10 to 50% of the initial values for maintaining the combustor clean and operating efficiently.
- It is essential for optimum slag remediation according to the invention, that the correct initial concentrations, rates and introduction rates be calculated and employed for the effective physical form of aluminum trihydroxide, and preferably, optionally magnesium hydroxide, to be introduced into the hot combustion gases in
chamber 20 to enable the chemical to be added with the desired effect. The implementation of CFD to the invention can be accomplished as set out inU. S. Patent No. 7,162,960 to Smyrniotis, et al. Particulate removal equipment (not shown) can be employed to remove particulates prior to passing the effluent up the stack. - In another alternate form of the invention, combustion catalysts and or effluent treatment chemicals can be added to the fuel, combustion zone or otherwise as described, for example in
U. S. Patent No. 7,162,960 to Smyrniotis, et al. - The following examples are presented to further explain and illustrate the invention and are not to be taken as limiting in any regard. Unless otherwise indicated, all parts and percentages are by weight.
- This example illustrates introduction of aluminum trihydroxide into a furnace burning 540 tons of coal per day. The coal is a blend of Illinois basin and Appalachian bituminous coals, giving the following analysis as combined:
Sample 1 2 3 Moisture, % 11.28 10.85 10.19 Ash, % 14.91 13.63 13.91 Volatile Matter, % 36.03 35.04 Fixed Carbon, % 39.49 40.86 Total, % 100 100 Sulfur, % 3.95 4.44 HHV, BTU/lb 10,742 10,730 - For the test Al(OH)3 (aluminum trihydroxide slurry or ATH for short) is fed as a 70% by weight aqueous slurry at a rate of 2.3 kg (5 pounds) slurry per ton of coal consumed from two banks of three air-cooled nozzles positioned on the wall opposite of two banks of pulverized coal burners - one bank at an elevation between the two burners and one bank at an elevation above the uppermost coal burners. The slurry is diluted to a concentration of 35 weight % ATH. The density of the ATH slurry before dilution is 6.3 kg/3.8 1 (14 pounds/gallon), meaning that the feed rate is 730.6 1 (193 gallons) per day (2.3 kg (5 pounds) per ton of coal) for ATH slurry.
- Based on this test, it is estimated that an effective feed rate for this particular combustor will be from 0.45 to 2.7 kg (1 to 6 pounds) of ATH slurry per ton of coal, e.g., 0.9 to 1.36 kg (2 to 3 pounds) per ton.
- This example illustrates the effect of introducing Mg(OH)2 (magnesium hydroxide) into a furnace burning 540 tons of coal per day in addition to the aluminum trihydroxide fed in Example 1. The coal was a blend of Illinois basin and Appalachian bituminous coals, as illustrated in Example 1.
- The magnesium hydroxide was fed as a slurry at 0.9 kg (2 lbs) of 50 to 60 weight % slurry per ton of coal consumed. Density of the magnesium hydroxide slurry was approximately 5.4 kg/3.8 1 (12 lbs/gallon). Therefore, the feed rate was about 340.7 1 (90 gallons) per day for the Mg(OH)2 slurry. As before, we fed the aluminum trihydroxide slurry at 2.3 kg (5 pounds) of slurry per ton of coal consumed. The density of the ATH was 6.3 kg/3.8 1 (14 pounds/gallon), making the feed rate 730.6 1 (193 gallons) per day for ATH.
- Based on this test, we estimate optimal feed rate for the best economics for the this particular combustor to be 0.23 to 0.9 kg (0.5 to 2 pounds) Mg(OH)2 slurry per ton of coal (e.g., 0.45 kg (1 pound) per ton) plus from 0.45 to 2.7 kg (1 to 6 pounds) ATH slurry per ton (e.g., 0.9 to 1.36 kg (2 to 3 pounds per ton).
Fig. 2 is a photograph of a slag sample obtained after operation for 24 hours of ATH feed only. The slag was unexpectedly friable. - The above description is for the purpose of teaching the person of ordinary skill in the art how to practice the invention. It is not intended to detail all of those obvious modifications and variations, which will become apparent to the skilled worker upon reading the description. It is intended, however, that all such obvious modifications and variations be included within the scope of the invention which is defined by the following claim. The claim is meant to cover the claimed components and steps in any sequence that is effective to meet the objectives there intended, unless the context specifically indicates the contrary.
Claims (1)
- A process for reducing slag cohesiveness and/or adhesiveness in a combustor and thereby decreasing the rate of fouling, comprising:combusting a slag-forming coal, having an iron content of greater than 15 % based on the weight of the ash and expressed as Fe2O3 and/or a calcium content of greater than 5 % based on the weight of the ash and expressed as CaO, with an overall excess of oxygen;moving the resulting combustion gases through heat exchange equipment under conditions which cause cooling of slag formed by burning the fuel;prior to contact with said heat exchange equipment introducing into hot combustion gases from initially 1.36 to 2.7 kg (3 to 6 pounds) per ton of coal burned of aluminium trihydroxide as an aqueous slurry and from 0.45 to 0.9 kg (1 to 2 pounds) per ton of coal burned of magnesium hydroxide as an aqueous slurry, with droplet sizes and concentrations effective to decrease the rate of fouling by slag,reducing the rate of introduction of the aluminium trihydroxide and magnesium hydroxide to from 10 to 50 % of the initial values for maintaining the combustor clean and operating efficiently,wherein computational fluid dynamics is employed to determine initial flow rates and select reagent introduction rates, reagent introduction location(s), reagent concentrations, reagent droplet size and reagent momentum.
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PL09795277T PL2318489T3 (en) | 2008-07-11 | 2009-07-13 | Targeted reagent injection for slag control from combustion of coals high in iron and/or calcium |
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US8000408P | 2008-07-11 | 2008-07-11 | |
PCT/US2009/050354 WO2010006325A1 (en) | 2008-07-11 | 2009-07-13 | Targeted reagent injection for slag control from combustion of coals high in iron and/or calcium |
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EP2318489A1 EP2318489A1 (en) | 2011-05-11 |
EP2318489A4 EP2318489A4 (en) | 2013-05-15 |
EP2318489B1 true EP2318489B1 (en) | 2015-09-02 |
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US (1) | US20100006014A1 (en) |
EP (1) | EP2318489B1 (en) |
JP (1) | JP5657533B2 (en) |
KR (1) | KR101298932B1 (en) |
CN (1) | CN102089413B (en) |
AR (1) | AR072502A1 (en) |
AU (1) | AU2009268391C1 (en) |
CA (1) | CA2729959C (en) |
CL (1) | CL2009001571A1 (en) |
CO (1) | CO6300873A2 (en) |
ES (1) | ES2554165T3 (en) |
HK (1) | HK1157810A1 (en) |
MX (1) | MX2011000275A (en) |
MY (1) | MY156010A (en) |
PL (1) | PL2318489T3 (en) |
RU (1) | RU2493240C2 (en) |
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US20090178599A1 (en) | 2008-01-15 | 2009-07-16 | Environmental Energy Services, Inc. | Process for operating a coal-fired furnace with reduced slag formation |
AU2012205350B2 (en) | 2011-01-14 | 2016-03-24 | Environmental Energy Services, Inc. | Process for operating a furnace with a bituminous coal and method for reducing slag formation therewith |
US9920929B2 (en) * | 2011-06-13 | 2018-03-20 | Ecolab Usa Inc. | Method for reducing slag in biomass combustion |
WO2017053499A1 (en) * | 2015-09-25 | 2017-03-30 | Fuel Tech, Inc. | Process and apparatus for reducing plume |
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JP3153091B2 (en) * | 1994-03-10 | 2001-04-03 | 株式会社荏原製作所 | Waste treatment method and gasification and melting and combustion equipment |
CA1136078A (en) * | 1978-09-21 | 1982-11-23 | George P. Masologites | Process for removing sulfur from coal |
US4428310A (en) * | 1982-07-26 | 1984-01-31 | Nalco Chemical Company | Phosphated alumina as slag modifier |
JPS59189144A (en) * | 1983-04-12 | 1984-10-26 | Hokuriku Electric Power Co Inc:The | Filler for rubber |
US4498402A (en) | 1983-06-13 | 1985-02-12 | Kober Alfred E | Method of reducing high temperature slagging in furnaces and conditioner for use therein |
JPH0586374A (en) * | 1991-09-26 | 1993-04-06 | Teikoku Sekiyu Kk | Decomposition of carbohydrate into combustible gas |
RU2086293C1 (en) * | 1993-05-28 | 1997-08-10 | Олег Порфирьевич Кочетков | Method and device for gas scrubbing |
US6289827B1 (en) * | 1999-06-24 | 2001-09-18 | Martin Marietta Magnesia Specialties Inc. | Process for the control of ash accumulation and corrosivity associated with selective catalytic reduction technology |
US6729248B2 (en) * | 2000-06-26 | 2004-05-04 | Ada Environmental Solutions, Llc | Low sulfur coal additive for improved furnace operation |
US6613110B2 (en) * | 2001-01-11 | 2003-09-02 | Benetech, Inc. | Inhibition of reflective ash build-up in coal-fired furnaces |
JP3745973B2 (en) * | 2001-03-23 | 2006-02-15 | タイホー工業株式会社 | Coal additive for preventing slagging and coal combustion method |
JP2003090530A (en) * | 2001-07-10 | 2003-03-28 | Ishikawajima Harima Heavy Ind Co Ltd | Clinker accumulation preventing device |
JP3746026B2 (en) * | 2002-08-28 | 2006-02-15 | タイホー工業株式会社 | Fuel additive for preventing slagging and fuel combustion method |
CN1890021B (en) * | 2003-12-05 | 2013-01-16 | 英特凯特公司 | Mixed metal oxide sorbents |
US7162960B2 (en) * | 2004-01-08 | 2007-01-16 | Fuel Tech, Inc. | Process for reducing plume opacity |
TWI342335B (en) * | 2004-06-02 | 2011-05-21 | Intercat Inc | Mixed metal oxide additives |
US20060121398A1 (en) * | 2004-12-07 | 2006-06-08 | Meffert Michael W | Additive atomizing systems and apparatus |
PL1848524T3 (en) * | 2005-02-04 | 2015-04-30 | Fuel Tech Inc | Targeted duct injection for so3 control |
WO2006138715A1 (en) * | 2005-06-16 | 2006-12-28 | Warner Chilcott Company, Inc. | Estrogen compositions for vaginal administration |
US20090071067A1 (en) * | 2007-09-17 | 2009-03-19 | Ian Macpherson | Environmentally-Friendly Additives And Additive Compositions For Solid Fuels |
US20090178599A1 (en) * | 2008-01-15 | 2009-07-16 | Environmental Energy Services, Inc. | Process for operating a coal-fired furnace with reduced slag formation |
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AU2009268391C1 (en) | 2014-12-11 |
KR101298932B1 (en) | 2013-08-22 |
TWI482852B (en) | 2015-05-01 |
RU2011103846A (en) | 2012-08-20 |
RU2493240C2 (en) | 2013-09-20 |
CN102089413A (en) | 2011-06-08 |
CO6300873A2 (en) | 2011-07-21 |
WO2010006325A1 (en) | 2010-01-14 |
ES2554165T3 (en) | 2015-12-16 |
HK1157810A1 (en) | 2012-07-06 |
PL2318489T3 (en) | 2016-03-31 |
CL2009001571A1 (en) | 2010-03-12 |
CA2729959C (en) | 2015-09-01 |
EP2318489A1 (en) | 2011-05-11 |
EP2318489A4 (en) | 2013-05-15 |
AU2009268391B2 (en) | 2014-05-08 |
MY156010A (en) | 2015-12-31 |
TW201009067A (en) | 2010-03-01 |
KR20110043656A (en) | 2011-04-27 |
JP2011527000A (en) | 2011-10-20 |
JP5657533B2 (en) | 2015-01-21 |
MX2011000275A (en) | 2011-03-02 |
AR072502A1 (en) | 2010-09-01 |
CA2729959A1 (en) | 2010-01-14 |
AU2009268391A1 (en) | 2010-01-14 |
US20100006014A1 (en) | 2010-01-14 |
CN102089413B (en) | 2013-12-18 |
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