US3004836A - Reduction of slag formation in coalfired furnaces, boilers and the like - Google Patents
Reduction of slag formation in coalfired furnaces, boilers and the like Download PDFInfo
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- US3004836A US3004836A US754730A US75473058A US3004836A US 3004836 A US3004836 A US 3004836A US 754730 A US754730 A US 754730A US 75473058 A US75473058 A US 75473058A US 3004836 A US3004836 A US 3004836A
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F15/00—Other methods of preventing corrosion or incrustation
- C23F15/005—Inhibiting incrustation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28G—CLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
- F28G9/00—Cleaning by flushing or washing, e.g. with chemical solvents
Definitions
- the instant invention relates to slag inhibiting compositions
- slag inhibiting compositions comprising a mixture of major proportion of magnesium oxide and a minor proportion of a phosphate salt, both ingredients in the form of small particles.
- This mixture is added to the solid carbonaceous fuel in an amount usually within the range of about 0.1 to 1.0 pounds of the particulate mixture per ton of coal.
- a convenient and economical method of addition of these particles is achieved by the spraying thereof onto the surface of the burning coaleither continuously or intermittently.
- Another object of the invention is to provide new chemical compositions composed of a particulate mixture of magnesium oxide and a phosphate salt as the active,
- Another object of the invention is to provide improvements in the burning of coal and the like.
- a still further object of the invention is to provide methods for burning coal wherein the chemical compositions of this invention are added to the coal while the latter is burning.
- a still further object of the invention is to provide improvements in the firing of furnaces, boilers and the like with solid carbonaceous fuel such as coal.
- magnesium oxide and a phosphate salt are mixed in proportions wherein the magnesium oxide constitutes approximately 50-80% by weight of the mixture and the phosphate salt constitutes about 2050% by weight of the mixture.
- the two components are in the form of solid particles having an average particle size falling within the range of approximately 0.001 inch to 0.05 inch. Extremely fine powders are not recommended for the purposes of this invention because they tend to be entrained in the furnace air and carried out of the fireside area before they can perform their beneficial functions.
- the magnesium oxide particles which are used for purposes of this invention are preferably at least 90% magnesium oxide. It may be magnesium oxide derived by the calcination of magnesium ore such as magnecite or by the calcination of amorphous magnesium hydroxide produced by the recovery of magnesium from sea water.
- the phosphate salt is preferably an alkaline earth metal salt.
- the phosphate salt is ground phosphate rock which has been calcined. This ground, calcined rock analyzes at least 70% by weight as tricalcium phosphate and at least 30% by weight as P 0
- a typical analysis of a ground calcined phosphate rock is:
- the magnesium oxide and phosphate salt such as ground, calcined phosphate rock, may be obtained through commercial channels in the desired average particle size and merely thoroughly mixed to form the slag-inhibiting compositions of this invention. In other cases, they may be obtained in larger particle sizes and ground either. separately or simultaneously and thereafter thoroughly mixed, if necessary.
- the preferred method for adding the slag-inhibiting compositions of this invention is the spraying of the par' ticles through nozzles by the use of high pressure air.
- a convenient way to add these compositions is by supplying the particles in the overfire air which is blown into the furnace above the furnace grate.
- This method of addition suffers the disadvantage that at least' a portion of the particles, in all likelihood, will be entrained in the air flowing upwardly from the furnace grates and, hence, maximum utilization of the particles will not be achieved.
- a more preferred point for addition of the compositions of this invention is at a point in the furnace above the grate but below the overfire air path.
- the horizontal how of the overlire air will tend to hold the particles down and bring them into contact with the burning coal bed on the furnace grates.
- the magnesium oxide and phosphate salt particles may be blown into the furnace by pressurized air or they may be suspended in a liquid hydrocarbon fuel which, in' turn, is sprayed onto the coal being burned.
- Example 1 Magnesium oxide and phosphate rock having the'previously described typical analysis are ground to a particle size wherein 95.5% of the particles pass through a 40 mesh screen, 88% of the particles pass through an mesh screen and 58% of the particles pass through a 200 mesh screen. The ground particles are thoroughly mixed in an amount wherein the magnesium oxide constitutesf 70% by weight of the mixture and the phosphate rock constitutes 30% by weight of the mixture. The mixture is then packaged and is ready for distribution as a slaginhibiting composition.
- Example II A mixture constituting 80% magnesium oxide and' 20% phosphate rock is prepared by a procedure similar to Example I.
- the particles have an average particle size of about 0.003 inch.
- Example 111 Seventy-five percent of magnesium oxide particles having an average particle size of about 0.006 inch and 25 of tricalcium phosphate having an average particle size of about-0.003 inch are thoroughly mixed together. The mixed particles are packaged and ready for distribution as a slag-inhibiting composition for use in coal-fired furnaces, boilers and the like.
- Example I a test was conducted with the composition of Example I in a coal-fired boiler.
- the test composition was added by spraying the same onto the burning coal via the overfire air.
- the boiler was a Wickes-Type B bo'der having a steam capacity of 75,000 pounds per hour at 4 35 p.s.i. with 590 F. superheat. 1
- the boiler had a spreader stoker. On an average day, the boiler burns -75 tons of coal.
- the test was conducted over'a six-week period, and the magnesium oxide-phosphate rock composition was added intermittently by each eight-hour shift.
- the feed ofthe magnesium oxide-phos- During the fifth week the feed was started at a rate of 7 1/6 pound per ton of coal fired, but was reduced gradual- 1y so that during the sixth and last week of the trial the treatment was down to about 1/ of one pound per ton of coal fired.
- the stack gas temperature will start to rise after about two weeks and will eventually get up to 620-630" F. Also, it was noted during the trial that the superheat temperature ran approximately 10 higher than normal.
- the treatments provided by the instant invention provide economies in the operation of furnaces, boilers and the? like.
- boilers may be operated at consider- 8,004,836 is I 4 ably longer periods of time before shutdown is necessary to clean the boilers.
- the boilers can be operated at more effective heat transfer efficiency than is possible without the addition of the treating compounds of this invention.
- a composition useful in slag prevention in coalfired furnaces comprising a mixture of small, dense particles of an average particle size in the range of 0.001 to 0.05 inch of 50-80% by weight of magnesium oxide particles obtained by the calcination of a member of the group consisting of magnesium ore and amorphous magnesium hydroxide and 20-50% by weight of alkaline earth phosphate salt particles.
- a composition useful in slag prevention in coalfired furnaces comprising a 'mixture of small, dense particles of 50-80% by weight of magnesium oxide particles obtained by the calcination of a member of the group consisting of magnesium ore and amorphous magnesium hydroxide and 20-50% by weight of calcined phosphate rock particles.
- a composition useful in slag prevention in coal fired furnaces comprising a mixture of small, dense particles of 50-80% by weight of magnesium oxide particles and 20-50% by'weight of calcined phosphate rock particles, analyzing at'least by weight as tricalcium phosphate and at least 30% by weight as P 0 4.
- a process for firing furnaces which comprises burning coal and adding to the burning coal a composition comprising a mixture of small particles of an average particle size in the range of 0.001 to 0.05 inch of 50-80% by Weight of magnesium oxide particles and 20-50% by weight of alkaline earth phosphate salt particles in an amount in the range of 0.1 to l'pound of said composition per ton of said coal.
- a process for firing furnaces which comprises burning a solid carbonaceous fuel and adding to the burning fuel a composition comprising a mixture of small particles of 50-80% by weight of magnesium oxide particles and 20-50 by weight of calcined phosphate rock particles.
- a process for firing furnaces which comprises burning a solid carbonaceous fuel and adding to the burning fuel a composition comprising a mixture of small particles having 50-80% by weight of magnesium oxide particles and 20-50% by weight of calcined phosphate rock particles, analyzing at least 70% by weight as tricalcium phosphate and at least 30% by weight as P 0 7.
- a process for firing furnaces which comprises burning a solid carbonaceous fuel in the presence of a juxtaposulate mixture of an average particle size in the range of 0.001 to 0.05 inch of 50-80% by Weight of magnesium oxide and 20-50% by weight of an alkaline earth phosphate salt.
- a process for firing furnaces which comprises burning a solid carbonaceous fuel in the presence of a particulate mixture of an average particle size in the range of 0.001 to 0.05 inch of 50-80% by weight of magnesium oxide and 20-50% by weight of an alkaline earth phosphate salt present with said fuel in an amount in the range of 0.1 to 1 pound of said mixture per ton of said solid carbonaceous fuel.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
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- Solid Fuels And Fuel-Associated Substances (AREA)
Description
United States Patentf) 3,004,836 REDUCTION OF SLAG FORMATION 1N COAL- FIRED FURNACES, BOILERS AND THE LIKE Harris Thompson, Downers Grove, 111., assignor to Nalco Chemical Company, a corporation of Delaware No Drawing. Filed Aug. 13, 1958, Ser. No. 754,730 9 Claims. (Cl. 44-4) This invention, in general, relates to chemical compositions which are useful in the reduction of slag formation and fireside deposits in coal-fired furnaces, boilers and the like, and to methods for burning solid carbonaceous fuels such as coal in the presence of these compounds.
In furnaces, boilers, and the like wherein the fuel employed is a solid carbonaceous fuel such as coal, it is desirable to reduce as much as possible the slag formation resulting from the burning of the coal, particularly slag deposits on boiler walls, boiler tubes and other fireside heat transfer surfaces. In units such as boilers, wherein the heat derived from the burning of coal is transferred through metal surfaces to heat a iluid, the amount of deposits on the surfaces is a serious factor because these deposits materially decrease the efiectiveness of heat transfer to the fluid being heated. Furthermore, some deposits are corrosive to the metal heat transfer surfaces, particularly at the high boiler temperatures, and the reduction or elimination of these deposits is beneficial in the prevention of corrosion of the metals.
Briefly, the instant invention relates to slag inhibiting compositions comprising a mixture of major proportion of magnesium oxide and a minor proportion of a phosphate salt, both ingredients in the form of small particles. This mixture is added to the solid carbonaceous fuel in an amount usually within the range of about 0.1 to 1.0 pounds of the particulate mixture per ton of coal. A convenient and economical method of addition of these particles is achieved by the spraying thereof onto the surface of the burning coaleither continuously or intermittently.
It is an object of the present invention to provide chemical compositions useful in the reduction of slag formation and fireside deposits resulting from the burning of solid carbonaceous fuel such as coal.
Another object of the invention is to provide new chemical compositions composed of a particulate mixture of magnesium oxide and a phosphate salt as the active,
essential ingredients with respect to the reduction of slag formation and fireside deposits resulting from burning of solid carbonaceous fuel such as coal.
Another object of the invention is to provide improvements in the burning of coal and the like.
A still further object of the invention is to provide methods for burning coal wherein the chemical compositions of this invention are added to the coal while the latter is burning.
A still further object of the invention is to provide improvements in the firing of furnaces, boilers and the like with solid carbonaceous fuel such as coal.
In accordance with the invention, magnesium oxide and a phosphate salt are mixed in proportions wherein the magnesium oxide constitutes approximately 50-80% by weight of the mixture and the phosphate salt constitutes about 2050% by weight of the mixture. The two components are in the form of solid particles having an average particle size falling within the range of approximately 0.001 inch to 0.05 inch. Extremely fine powders are not recommended for the purposes of this invention because they tend to be entrained in the furnace air and carried out of the fireside area before they can perform their beneficial functions.
The magnesium oxide particles which are used for purposes of this invention are preferably at least 90% magnesium oxide. It may be magnesium oxide derived by the calcination of magnesium ore such as magnecite or by the calcination of amorphous magnesium hydroxide produced by the recovery of magnesium from sea water.
The phosphate salt is preferably an alkaline earth metal salt. In one preferred form of the invention, the phosphate salt is ground phosphate rock which has been calcined. This ground, calcined rock analyzes at least 70% by weight as tricalcium phosphate and at least 30% by weight as P 0 A typical analysis of a ground calcined phosphate rock is:
The magnesium oxide and phosphate salt, such as ground, calcined phosphate rock, may be obtained through commercial channels in the desired average particle size and merely thoroughly mixed to form the slag-inhibiting compositions of this invention. In other cases, they may be obtained in larger particle sizes and ground either. separately or simultaneously and thereafter thoroughly mixed, if necessary.
The preferred method for adding the slag-inhibiting compositions of this invention is the spraying of the par' ticles through nozzles by the use of high pressure air. A convenient way to add these compositions is by supplying the particles in the overfire air which is blown into the furnace above the furnace grate. This method of addition, however, suffers the disadvantage that at least' a portion of the particles, in all likelihood, will be entrained in the air flowing upwardly from the furnace grates and, hence, maximum utilization of the particles will not be achieved.
A more preferred point for addition of the compositions of this invention is at a point in the furnace above the grate but below the overfire air path. By this method of addition, the horizontal how of the overlire air will tend to hold the particles down and bring them into contact with the burning coal bed on the furnace grates. The magnesium oxide and phosphate salt particles may be blown into the furnace by pressurized air or they may be suspended in a liquid hydrocarbon fuel which, in' turn, is sprayed onto the coal being burned.
Some preferred embodiments of the invention are illus-l trated in the following examples, wherein the parts are by weight unless otherwise indicated.
Example 1 Magnesium oxide and phosphate rock having the'previously described typical analysis are ground to a particle size wherein 95.5% of the particles pass through a 40 mesh screen, 88% of the particles pass through an mesh screen and 58% of the particles pass through a 200 mesh screen. The ground particles are thoroughly mixed in an amount wherein the magnesium oxide constitutesf 70% by weight of the mixture and the phosphate rock constitutes 30% by weight of the mixture. The mixture is then packaged and is ready for distribution as a slaginhibiting composition.
Example II A mixture constituting 80% magnesium oxide and' 20% phosphate rock is prepared by a procedure similar to Example I. The particles have an average particle size of about 0.003 inch.
3 Example 111 Seventy-five percent of magnesium oxide particles having an average particle size of about 0.006 inch and 25 of tricalcium phosphate having an average particle size of about-0.003 inch are thoroughly mixed together. The mixed particles are packaged and ready for distribution as a slag-inhibiting composition for use in coal-fired furnaces, boilers and the like.
To determine the slag-inhibiting properties of the compositions of this invention, a test was conducted with the composition of Example I in a coal-fired boiler. The test composition was added by spraying the same onto the burning coal via the overfire air. The boiler was a Wickes-Type B bo'der having a steam capacity of 75,000 pounds per hour at 4 35 p.s.i. with 590 F. superheat. 1 The boiler had a spreader stoker. On an average day, the boiler burns -75 tons of coal.
The test was conducted over'a six-week period, and the magnesium oxide-phosphate rock composition was added intermittently by each eight-hour shift. For the first two weeks the feed ofthe magnesium oxide-phos- During the fifth week the feed was started at a rate of 7 1/6 pound per ton of coal fired, but was reduced gradual- 1y so that during the sixth and last week of the trial the treatment was down to about 1/ of one pound per ton of coal fired.
Prior to the test, trouble had been encountered with slag and with a consequent increase in stack gas temperature. This increase in the stack gas temperature was usually'noticed about two weeks after the fireside of the boilers had been cleaned. Near the end of the fourth week of the trial with the magnesium oxide-phosphate rock treatment, no rise in stack gas temperature had been noted since the start of the trial.
While the trial was being conducted, a shipment of bad coal was received. This coal was so poor that considerable trouble was experienced in even burning the fuel; Finally, the boiler operators had to resort to blending the bad coal on a 50-50 basis with some better coal. Due to this bad coal, there was some slag built up immediately above the grates, evidenced when the boiler was torn down for cleaning. This slag was very friable and could be pulled away from the boiler tubes by hand and had a spongy, honeycomb appearance. The rest of the boiler was in excellent condition. The overhead screen tubes and superheater showed no sign of slag build-up. The tubes were about 75% bare metal, with the remaining 25% covered by a very light coating no more than /8" thick. In previous operations even with good coal, but withoutthe. addition of the magnesium oxide-phosphate rock mixture, the overhead usually becomes plugged with slag--requiring boiler shutdown to manually clean off the slag. Further, it was reported after the trial that this was the first time in operation of the boiler that no manual cleaning of the superheater section was required. Also, during the six-week trial the stack gas temperature remained steady at 550 F.
Under normal conditions, without the treatment in accordance with the invention, the stack gas temperature will start to rise after about two weeks and will eventually get up to 620-630" F. Also, it was noted during the trial that the superheat temperature ran approximately 10 higher than normal.
Thus, it will be seen that, the treatments provided by the instant invention provide economies in the operation of furnaces, boilers and the? like. By materially reducing slag deposits on boiler walls, boiler tubes and other heat transfer surfaces, boilers may be operated at consider- 8,004,836 is I 4 ably longer periods of time before shutdown is necessary to clean the boilers. Further, by reducing slag deposits, the boilers can be operated at more effective heat transfer efficiency than is possible without the addition of the treating compounds of this invention. V
The invention is hereby claimed as follows:
1. A composition useful in slag prevention in coalfired furnaces comprising a mixture of small, dense particles of an average particle size in the range of 0.001 to 0.05 inch of 50-80% by weight of magnesium oxide particles obtained by the calcination of a member of the group consisting of magnesium ore and amorphous magnesium hydroxide and 20-50% by weight of alkaline earth phosphate salt particles.
2. A composition useful in slag prevention in coalfired furnaces comprising a 'mixture of small, dense particles of 50-80% by weight of magnesium oxide particles obtained by the calcination of a member of the group consisting of magnesium ore and amorphous magnesium hydroxide and 20-50% by weight of calcined phosphate rock particles.
3. A composition useful in slag prevention in coal fired furnaces comprising a mixture of small, dense particles of 50-80% by weight of magnesium oxide particles and 20-50% by'weight of calcined phosphate rock particles, analyzing at'least by weight as tricalcium phosphate and at least 30% by weight as P 0 4. A process for firing furnaces which comprises burning coal and adding to the burning coal a composition comprising a mixture of small particles of an average particle size in the range of 0.001 to 0.05 inch of 50-80% by Weight of magnesium oxide particles and 20-50% by weight of alkaline earth phosphate salt particles in an amount in the range of 0.1 to l'pound of said composition per ton of said coal.
5. A process for firing furnaces which comprises burning a solid carbonaceous fuel and adding to the burning fuel a composition comprising a mixture of small particles of 50-80% by weight of magnesium oxide particles and 20-50 by weight of calcined phosphate rock particles. p
6. A process for firing furnaces which comprises burning a solid carbonaceous fuel and adding to the burning fuel a composition comprising a mixture of small particles having 50-80% by weight of magnesium oxide particles and 20-50% by weight of calcined phosphate rock particles, analyzing at least 70% by weight as tricalcium phosphate and at least 30% by weight as P 0 7. A process for firing furnaces which comprises burning a solid carbonaceous fuel in the presence of a partieulate mixture of an average particle size in the range of 0.001 to 0.05 inch of 50-80% by Weight of magnesium oxide and 20-50% by weight of an alkaline earth phosphate salt.
. 8. A process for firing furnaces which comprises burning a solid carbonaceous fuel in the presence of a particulate mixture of an average particle size in the range of 0.001 to 0.05 inch of 50-80% by weight of magnesium oxide and 20-50% by weight of an alkaline earth phosphate salt present with said fuel in an amount in the range of 0.1 to 1 pound of said mixture per ton of said solid carbonaceous fuel. 1
9. The process of. claim 8 wherein said solid carbonaceous fuel is coal.
References (Iited in the file of this patent UN TED ST T PATENTS.
2,222,969 Kistler Nov. 26, 1940 2,532,548 Heide Dec. 5, 1950 2,702,965 Boyd Mar. 1, 1955 UNITED STATES PATENT. OFFICE CERTIFICATE OF CORRECTION Patent No. 3,004,836 October 17, 196
Harris Thompson It is hereby certified that error appears in the above numbered patent requiring correction and that the said Letters Patent should read as corrected below.
Column 2, line 57, for "95.5%" read 99.5%
Signed and sealed this 17th day of April 1962.
( SEA Attest:
ESTON G. JOHNSON DAVID L. LADD Attesting Officer Commissioner of Patents
Claims (1)
1. A COMPOSITION USEFUL IN SLAG PREVENTION IN COALFIRED FURNACES COMPRISING A MIXTURE OF SMALL, DENSE PARTICLES OF AN AVERAGE PARTICLE SIZE IN THE RANGE OF 0.001 TO 0.05 INCH OF 50-80% BY WEIGHT OF MAGNESIUM OXIDE PARTICLES OBTAINED BY THE CALCINATION OF A MEMBER OF THE GROUP CONSISTING OF MAGNESIUM ORE AND AMORPHOUS MAGNESIUM HYDROXIDE AND 20-50% BY WEIGHT OF ALKALINE EARTH PHOSPHATE SALT PARTICLES.
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US754730A US3004836A (en) | 1958-08-13 | 1958-08-13 | Reduction of slag formation in coalfired furnaces, boilers and the like |
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US754730A US3004836A (en) | 1958-08-13 | 1958-08-13 | Reduction of slag formation in coalfired furnaces, boilers and the like |
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Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
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US3628925A (en) * | 1970-02-16 | 1971-12-21 | Trimex Corp | Combustion adjuvant |
US3630696A (en) * | 1969-10-27 | 1971-12-28 | Trimex Corp | Combustion adjuvant |
US3948617A (en) * | 1972-10-11 | 1976-04-06 | Benjamin Withorn | Method of reducing sulphur dioxide emissions from combustible materials |
DE3023520A1 (en) * | 1979-06-28 | 1981-01-08 | Svenska Rexas Ab | METHOD AND MEANS FOR REDUCING THE THICKNESS OF DEPOSITS ON SMOKE-COATED SURFACES OF FIREPLACING SYSTEMS |
US5741764A (en) * | 1996-10-15 | 1998-04-21 | The Lubrizol Corporation | Two-cycle lubricant containing solvent and high molecular weight polymer |
WO2001005913A1 (en) * | 1999-07-16 | 2001-01-25 | Reatech | Phosphor addition in gasification |
US6203848B1 (en) * | 1996-12-20 | 2001-03-20 | Pohang Iron & Steel Co., Ltd. | Method for increasing the charring ratio of coal |
US6484651B1 (en) * | 2000-10-06 | 2002-11-26 | Crown Coal & Coke Co. | Method for operating a slag tap combustion apparatus |
US20020184817A1 (en) * | 2000-06-26 | 2002-12-12 | Ada Environmental Solutions, Llc | Low sulfur coal additive for improved furnace operation |
US20040040438A1 (en) * | 2002-08-30 | 2004-03-04 | Baldrey Kenneth E. | Oxidizing additives for control of particulate emissions |
US20080213146A1 (en) * | 2007-01-05 | 2008-09-04 | Bert Zauderer | Technical and economic optimization of combustion, nitrogen oxides, sulfur dioxide, mercury, carbon dioxide, coal ash and slag and coal slurry use in coal fired furnaces/boilers |
US20110030592A1 (en) * | 2000-06-26 | 2011-02-10 | Ada Environmental Solutions, Llc | Additives for mercury oxidation in coal-fired power plants |
US8124036B1 (en) | 2005-10-27 | 2012-02-28 | ADA-ES, Inc. | Additives for mercury oxidation in coal-fired power plants |
US8383071B2 (en) | 2010-03-10 | 2013-02-26 | Ada Environmental Solutions, Llc | Process for dilute phase injection of dry alkaline materials |
US8784757B2 (en) | 2010-03-10 | 2014-07-22 | ADA-ES, Inc. | Air treatment process for dilute phase injection of dry alkaline materials |
US8974756B2 (en) | 2012-07-25 | 2015-03-10 | ADA-ES, Inc. | Process to enhance mixing of dry sorbents and flue gas for air pollution control |
US9017452B2 (en) | 2011-11-14 | 2015-04-28 | ADA-ES, Inc. | System and method for dense phase sorbent injection |
US10350545B2 (en) | 2014-11-25 | 2019-07-16 | ADA-ES, Inc. | Low pressure drop static mixing system |
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Cited By (34)
Publication number | Priority date | Publication date | Assignee | Title |
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US3630696A (en) * | 1969-10-27 | 1971-12-28 | Trimex Corp | Combustion adjuvant |
US3628925A (en) * | 1970-02-16 | 1971-12-21 | Trimex Corp | Combustion adjuvant |
US3948617A (en) * | 1972-10-11 | 1976-04-06 | Benjamin Withorn | Method of reducing sulphur dioxide emissions from combustible materials |
DE3023520A1 (en) * | 1979-06-28 | 1981-01-08 | Svenska Rexas Ab | METHOD AND MEANS FOR REDUCING THE THICKNESS OF DEPOSITS ON SMOKE-COATED SURFACES OF FIREPLACING SYSTEMS |
US5741764A (en) * | 1996-10-15 | 1998-04-21 | The Lubrizol Corporation | Two-cycle lubricant containing solvent and high molecular weight polymer |
US6203848B1 (en) * | 1996-12-20 | 2001-03-20 | Pohang Iron & Steel Co., Ltd. | Method for increasing the charring ratio of coal |
US6615751B1 (en) | 1999-07-16 | 2003-09-09 | Raetech | Method for reducing agglomeration, sintering and deposit formation in gasification and combustion of biomass |
WO2001005913A1 (en) * | 1999-07-16 | 2001-01-25 | Reatech | Phosphor addition in gasification |
WO2001005911A2 (en) * | 1999-07-16 | 2001-01-25 | Reatech | A method for reducing agglomeration, sintering and deposit formation |
WO2001005911A3 (en) * | 1999-07-16 | 2001-08-09 | Reatech | A method for reducing agglomeration, sintering and deposit formation |
US8439989B2 (en) | 2000-06-26 | 2013-05-14 | ADA-ES, Inc. | Additives for mercury oxidation in coal-fired power plants |
US20040016377A1 (en) * | 2000-06-26 | 2004-01-29 | Oil Sands Underground Mining, Inc. | Low sulfur coal additive for improved furnace operation |
US11168274B2 (en) | 2000-06-26 | 2021-11-09 | ADA-ES, Inc. | Low sulfur coal additive for improved furnace operation |
US6729248B2 (en) * | 2000-06-26 | 2004-05-04 | Ada Environmental Solutions, Llc | Low sulfur coal additive for improved furnace operation |
US6773471B2 (en) | 2000-06-26 | 2004-08-10 | Ada Environmental Solutions, Llc | Low sulfur coal additive for improved furnace operation |
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