US1183445A - Compound for treating sulfur-bearing fuel and other substances. - Google Patents

Compound for treating sulfur-bearing fuel and other substances. Download PDF

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Publication number
US1183445A
US1183445A US7944716A US7944716A US1183445A US 1183445 A US1183445 A US 1183445A US 7944716 A US7944716 A US 7944716A US 7944716 A US7944716 A US 7944716A US 1183445 A US1183445 A US 1183445A
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Prior art keywords
fuel
compound
substances
combustion
sulfur
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US7944716A
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Charles Foxwell
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SMOKE-COAL ECONOMIZER Corp
SMOKE COAL ECONOMIZER CORP
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SMOKE COAL ECONOMIZER CORP
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Priority to US7944716A priority Critical patent/US1183445A/en
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L9/00Treating solid fuels to improve their combustion
    • C10L9/10Treating solid fuels to improve their combustion by using additives

Definitions

  • the invention serves the further important purpose of protecting fuel' from slaking or losing its more volatile constituents when stored in exposed places for protracted periods and also counteracting conditions which lead to spontaneous combustion of the fuel.
  • This last named effect may, by the use of the new compound, be realized 7 in connection with certain substances other will not attack iron or steel surfaces of the.
  • the fuel is treated with a water solution of calcium chlorid and an oxygen-bearing compound of boron with the chlorin and boron compounds in such proportions as will establish a molecular balance between these two elements, as hereinafter more fully described.
  • a water solution of calcium chlorid and an oxygen-bearing compound of boron with the chlorin and boron compounds in such proportions as will establish a molecular balance between these two elements, as hereinafter more fully described.
  • the fuel burns as freely and easily as the best coal, notwithstanding the fuel may be rich in sulfur, and give 03 as many calories of heat and evaporate as much water.
  • the products of combustion are rendered substantially inert and thus furnace or heat-absorbing elements of a boiler in connection with which the fuel is used.
  • the sulfur is retained in combi- Specification of Letters Patent.
  • the characteristics recited result mainly from the supply of oxygen for combustion in addition to that available from atmosphere; the combining of the sulfur with the calcium through the intermediate step of forming SO, and the passing of the chlorin first to the-(for example) sodium element and then to the boronof the reagent supplied, so that neither sulfur nor chlorin are released; while during storage, the solution resists escape of the volatile fuel elements and screens it from the access of atmospheric oxygen and moisture that tend to raise the temperature of the fuel and develop spontaneous combustion.
  • the coal is converted to S0,.
  • coal is ready for use.
  • the treat-- ment may proceede on a scale less than that stated, in case it be not important to control all of the contained sulfur; and if the coal be treated with an excess of the solution, no harm will be done.
  • a compound for treating sulfurous fuel consisting in calcium chlorid in conjunction with an oxygen-bearing compound of boron having the qualities of preventing the escape of the sulfuric radical and the chlorin in their nascent state, and the production of oxygen during the process of combustion.
  • a combustion-promoting compound for sulfurous fuels consisting of calcium chlorid and borax in solution.
  • a combustion-promoting compound for sulfurous fuels consisting of calcium chlo rid and borax in solution in the proportion which leaves the chlorin and boron elements of the ingredients, being in substantially the proportions of B01 4:.
  • a substance for resisting spontaneous combustion in materials said substance consisting of a mixture of calcium chlorid and borax.

Description

CHARLES FOXWELL, 0F BALTIMORE, MARYLAND, ASSIGNOR TO THE SMOKE-COAL ECONOMIZER CORPORATION, OF BALTIMORE, MARYLAND, A CORPORATION OF MARYLAND.
COMPOUND FOR TREATING SULFUR-BEARING FUEL AND OTHER'SUBSTANCES.
No Drawing.
bustion more complete and thus getting greater benefit from the fuel, but also rendering the products of combustion less harmful to metal parts (particularly iron or steel) of the combustion or heat-absorbing apparatus, in the presence of which c0mbustion takes place, or reducing contamination of metals, for the smelting of which the fuel may be employed.
In addition to the eflects constituting the principal objects of the invention as above outlined, the invention serves the further important purpose of protecting fuel' from slaking or losing its more volatile constituents when stored in exposed places for protracted periods and also counteracting conditions which lead to spontaneous combustion of the fuel. This last named effect may, by the use of the new compound, be realized 7 in connection with certain substances other will not attack iron or steel surfaces of the.
than fuel.
In carrying out the invention, the fuel is treated with a water solution of calcium chlorid and an oxygen-bearing compound of boron with the chlorin and boron compounds in such proportions as will establish a molecular balance between these two elements, as hereinafter more fully described. Among the characteristics of fuel treated by such a solution may be mentioned the following: The fuel burns as freely and easily as the best coal, notwithstanding the fuel may be rich in sulfur, and give 03 as many calories of heat and evaporate as much water. The products of combustion are rendered substantially inert and thus furnace or heat-absorbing elements of a boiler in connection with which the fuel is used. The sulfur is retained in combi- Specification of Letters Patent.
nation instead of being set free, and therefore, prevented fromcontaminating the metal values of ore, for the smelting of which the fuel may be used. The clinker is left lesstenacious and more readily disintegrated. Smoke and soot discharged from the stack are greatly reduced by the more complete combustion, thus not only economizing in the fuel required, but saving in the cost of cleaning.
While the characteristics and effects above recited have been ascertained by burning tests of different bodies of the same fuel and by comparison of treated and untreated masses of the same fuel subjected to the same storage conditions, and while not resting my claim to protection upon a technically correct discussion of the chemical reactions involved, and while these reactions would naturally differ more or less with different analyses of coal and difierent reagents employed in the compound used for treating the coal, the following is a general statement of what I believe to be the chemical phenomena-incident to the practising of my invention. That is to say, the characteristics recited result mainly from the supply of oxygen for combustion in addition to that available from atmosphere; the combining of the sulfur with the calcium through the intermediate step of forming SO, and the passing of the chlorin first to the-(for example) sodium element and then to the boronof the reagent supplied, so that neither sulfur nor chlorin are released; while during storage, the solution resists escape of the volatile fuel elements and screens it from the access of atmospheric oxygen and moisture that tend to raise the temperature of the fuel and develop spontaneous combustion.
Commercial borax (Na BQJ serves well for the boron compound, and this being dis solved in water together with calcium chlorid, in the proportion of, say, 382 pounds of commercial borax to 918 pounds of calcium Patented May 16, 19116.
Application filed February 19, 1916. Serial No. 79,447.
chlorid, of 72% purity which will make the chlorin and boron molecularly equivalent,
and the percentage of sulfur being ascer tained in the coal to be treated, the coal is is converted to S0,.
coal is ready for use. Obviously, the treat-- ment may procede on a scale less than that stated, in case it be not important to control all of the contained sulfur; and if the coal be treated with an excess of the solution, no harm will be done.
The reactions which take place in the burning of fuel treated as above described, (neglecting for convenience minor elements such as iron, alumina, and magnesia which exist in greater or less quantities in coal) may be explained as follows, the fuel in its natural state being represented by C plus S and the mixture in the fire box having the constituency, C plus S plus CaCl plus Na 'B O plus H O :The fire is started, the coal is consumed and the contained sulfur The SO starts to liberate chlorin from the CaCl, and forms CaSO The chlorin now liberated, combines with the sodium of the Na B O forming NaCl and liberating oxygen together with B 0 After satisfying the sodium element of the i a B,,O,, excess of chlorin liberated combines with boron trioxid B 0 liberating more oxygen and forming boron trichlorid B01 which is a fuming liquid that passes out through the stack without injury to the iron or steel surfaces with which it may come in contact. Excess of SO after satisfying the calcium element combines with sodium chlorid forming sodium sulfite Na SO and liberating more chlorin, which still finds its proper proportion" of B 0 and liberates still more oxygen and forms still more BCI, that passes out through the stack. The CaSO and Na SO formed as stated, are reduced by their contact with burning coal to Gas and Na s,
respectively, and in so doing, liberate additional equivalents of oxygen for further promoting the combustion.
From the foregoing description, it will be seen that I have produced a new and useful compound, not only for treating fuel to improve its combustion and render it safe against spontaneous combustion, but for the treatment of other substances in which spontaneous combustion is ordinarily liable to occur.
I claim v 1. A compound for treating sulfurous fuel consisting in calcium chlorid in conjunction with an oxygen-bearing compound of boron having the qualities of preventing the escape of the sulfuric radical and the chlorin in their nascent state, and the production of oxygen during the process of combustion.
A combustion-promoting compound for sulfurous fuels consisting of calcium chlorid and borax in solution.
A combustion-promoting compound for sulfurous fuels consisting of calcium chlo rid and borax in solution in the proportion which leaves the chlorin and boron elements of the ingredients, being in substantially the proportions of B01 4:. A substance for resisting spontaneous combustion in materials; said substance consisting of a mixture of calcium chlorid and borax.
The foregoing specification. signed at Washington, in the District of Columbia, this 19th day of February, 1916.
. CHARLES FOXWELL.
US7944716A 1916-02-19 1916-02-19 Compound for treating sulfur-bearing fuel and other substances. Expired - Lifetime US1183445A (en)

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US7944716A US1183445A (en) 1916-02-19 1916-02-19 Compound for treating sulfur-bearing fuel and other substances.

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US7944716A US1183445A (en) 1916-02-19 1916-02-19 Compound for treating sulfur-bearing fuel and other substances.

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Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4057398A (en) * 1976-02-24 1977-11-08 Apollo Chemical Corporation Process for reducing the fusion point of coal ash
US4886522A (en) * 1988-03-03 1989-12-12 Malin Research Corporation Process, for the desulfurization of coal
US20060210463A1 (en) * 2005-03-17 2006-09-21 Comrie Douglas C Reducing mercury emissions from the burning of coal
US20070168213A1 (en) * 2006-01-18 2007-07-19 Comrie Douglas C Methods of operating a coal burning facility
US20070184394A1 (en) * 2006-02-07 2007-08-09 Comrie Douglas C Production of cementitious ash products with reduced carbon emissions
US20080286703A1 (en) * 2004-06-28 2008-11-20 Nox Ii International Ltd. Reducing Sulfur Gas Emissions Resulting from the Burning of Carbonaceous Fuels
US7758827B2 (en) 2005-03-17 2010-07-20 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal
US8124036B1 (en) 2005-10-27 2012-02-28 ADA-ES, Inc. Additives for mercury oxidation in coal-fired power plants
US8372362B2 (en) 2010-02-04 2013-02-12 ADA-ES, Inc. Method and system for controlling mercury emissions from coal-fired thermal processes
US8383071B2 (en) 2010-03-10 2013-02-26 Ada Environmental Solutions, Llc Process for dilute phase injection of dry alkaline materials
US8496894B2 (en) 2010-02-04 2013-07-30 ADA-ES, Inc. Method and system for controlling mercury emissions from coal-fired thermal processes
US8524179B2 (en) 2010-10-25 2013-09-03 ADA-ES, Inc. Hot-side method and system
US8784757B2 (en) 2010-03-10 2014-07-22 ADA-ES, Inc. Air treatment process for dilute phase injection of dry alkaline materials
US8883099B2 (en) 2012-04-11 2014-11-11 ADA-ES, Inc. Control of wet scrubber oxidation inhibitor and byproduct recovery
US8951487B2 (en) 2010-10-25 2015-02-10 ADA-ES, Inc. Hot-side method and system
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
US10465137B2 (en) 2011-05-13 2019-11-05 Ada Es, Inc. Process to reduce emissions of nitrogen oxides and mercury from coal-fired boilers
US10767130B2 (en) 2012-08-10 2020-09-08 ADA-ES, Inc. Method and additive for controlling nitrogen oxide emissions
US11298657B2 (en) 2010-10-25 2022-04-12 ADA-ES, Inc. Hot-side method and system

Cited By (68)

* Cited by examiner, † Cited by third party
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US4057398A (en) * 1976-02-24 1977-11-08 Apollo Chemical Corporation Process for reducing the fusion point of coal ash
US4886522A (en) * 1988-03-03 1989-12-12 Malin Research Corporation Process, for the desulfurization of coal
US20080286703A1 (en) * 2004-06-28 2008-11-20 Nox Ii International Ltd. Reducing Sulfur Gas Emissions Resulting from the Burning of Carbonaceous Fuels
US9133408B2 (en) 2004-06-28 2015-09-15 Nox Ii, Ltd. Reducing sulfur gas emissions resulting from the burning of carbonaceous fuels
US8574324B2 (en) 2004-06-28 2013-11-05 Nox Ii, Ltd. Reducing sulfur gas emissions resulting from the burning of carbonaceous fuels
US11732888B2 (en) 2005-03-17 2023-08-22 Nox Ii, Ltd. Sorbents for coal combustion
US10641483B2 (en) 2005-03-17 2020-05-05 Nox Ii, Ltd. Sorbents for coal combustion
US20090117019A1 (en) * 2005-03-17 2009-05-07 Comrie Douglas C Reducing mercury emissions from the burning of coal
US7674442B2 (en) 2005-03-17 2010-03-09 Comrie Douglas C Reducing mercury emissions from the burning of coal
US7758827B2 (en) 2005-03-17 2010-07-20 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal
US7776301B2 (en) 2005-03-17 2010-08-17 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal
US7955577B2 (en) 2005-03-17 2011-06-07 NOx II, Ltd Reducing mercury emissions from the burning of coal
US20110203499A1 (en) * 2005-03-17 2011-08-25 Nox Ii, Ltd. Reducing Mercury Emissions From The Burning Of Coal
US9702554B2 (en) 2005-03-17 2017-07-11 Nox Ii, Ltd. Sorbents for coal combustion
US9169453B2 (en) 2005-03-17 2015-10-27 Nox Ii, Ltd. Sorbents for coal combustion
US8226913B2 (en) 2005-03-17 2012-07-24 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal
US9822973B2 (en) 2005-03-17 2017-11-21 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal
US20060210463A1 (en) * 2005-03-17 2006-09-21 Comrie Douglas C Reducing mercury emissions from the burning of coal
US9416967B2 (en) 2005-03-17 2016-08-16 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal
US11732889B2 (en) 2005-03-17 2023-08-22 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal by remote sorbent addition
US8501128B2 (en) 2005-03-17 2013-08-06 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal
US11060723B2 (en) 2005-03-17 2021-07-13 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal by remote sorbent addition
US8545778B2 (en) 2005-03-17 2013-10-01 Nox Ii, Ltd. Sorbents for coal combustion
US9945557B2 (en) 2005-03-17 2018-04-17 Nox Ii, Ltd. Sorbents for coal combustion
US8658115B2 (en) 2005-03-17 2014-02-25 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal
US8703081B2 (en) 2005-03-17 2014-04-22 Nox Ii, Ltd. Sorbents for coal combustion
US10962224B2 (en) 2005-03-17 2021-03-30 Nox Ii, Ltd. Sorbents for coal combustion
US7507083B2 (en) 2005-03-17 2009-03-24 Douglas C Comrie Reducing mercury emissions from the burning of coal
US8920158B2 (en) 2005-03-17 2014-12-30 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal
US10612779B2 (en) 2005-03-17 2020-04-07 Nox Ii, Ltd. Sorbents for coal combustion
US10359192B2 (en) 2005-03-17 2019-07-23 Nox Ii, Ltd. Reducing mercury emissions from the burning of coal
US8293196B1 (en) 2005-10-27 2012-10-23 ADA-ES, Inc. 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
US20070168213A1 (en) * 2006-01-18 2007-07-19 Comrie Douglas C Methods of operating a coal burning facility
US8150776B2 (en) 2006-01-18 2012-04-03 Nox Ii, Ltd. Methods of operating a coal burning facility
US20070184394A1 (en) * 2006-02-07 2007-08-09 Comrie Douglas C Production of cementitious ash products with reduced carbon emissions
US8372362B2 (en) 2010-02-04 2013-02-12 ADA-ES, Inc. Method and system for controlling mercury emissions from coal-fired thermal processes
US10427096B2 (en) 2010-02-04 2019-10-01 ADA-ES, Inc. Method and system for controlling mercury emissions from coal-fired thermal processes
US9352275B2 (en) 2010-02-04 2016-05-31 ADA-ES, Inc. Method and system for controlling mercury emissions from coal-fired thermal processes
US9221013B2 (en) 2010-02-04 2015-12-29 ADA-ES, Inc. Method and system for controlling mercury emissions from coal-fired thermal processes
US9884286B2 (en) 2010-02-04 2018-02-06 ADA-ES, Inc. Method and system for controlling mercury emissions from coal-fired thermal processes
US8496894B2 (en) 2010-02-04 2013-07-30 ADA-ES, Inc. Method and system for controlling mercury emissions from coal-fired thermal processes
US11213787B2 (en) 2010-02-04 2022-01-04 ADA-ES, Inc. Method and system for controlling mercury emissions from coal-fired thermal processes
US10843130B2 (en) 2010-02-04 2020-11-24 ADA-ES, Inc. Method and system for controlling mercury emissions from coal-fired thermal processes
US8383071B2 (en) 2010-03-10 2013-02-26 Ada Environmental Solutions, Llc Process for dilute phase injection of dry alkaline materials
US9149759B2 (en) 2010-03-10 2015-10-06 ADA-ES, Inc. Air treatment 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
US8951487B2 (en) 2010-10-25 2015-02-10 ADA-ES, Inc. Hot-side method and system
US10124293B2 (en) 2010-10-25 2018-11-13 ADA-ES, Inc. Hot-side method and system
US9657942B2 (en) 2010-10-25 2017-05-23 ADA-ES, Inc. Hot-side method and system
US11298657B2 (en) 2010-10-25 2022-04-12 ADA-ES, Inc. Hot-side method and system
US8524179B2 (en) 2010-10-25 2013-09-03 ADA-ES, Inc. Hot-side method and system
US10730015B2 (en) 2010-10-25 2020-08-04 ADA-ES, Inc. Hot-side method and system
US11118127B2 (en) 2011-05-13 2021-09-14 ADA-ES, Inc. Process to reduce emissions of nitrogen oxides and mercury from coal-fired boilers
US10731095B2 (en) 2011-05-13 2020-08-04 ADA-ES, Inc. Process to reduce emissions of nitrogen oxides and mercury from coal-fired boilers
US10465137B2 (en) 2011-05-13 2019-11-05 Ada Es, Inc. Process to reduce emissions of nitrogen oxides and mercury from coal-fired boilers
US9017452B2 (en) 2011-11-14 2015-04-28 ADA-ES, Inc. System and method for dense phase sorbent injection
US9409123B2 (en) 2012-04-11 2016-08-09 ASA-ES, Inc. Control of wet scrubber oxidation inhibitor and byproduct recovery
US8883099B2 (en) 2012-04-11 2014-11-11 ADA-ES, Inc. Control of wet scrubber oxidation inhibitor and byproduct recovery
US11065578B2 (en) 2012-04-11 2021-07-20 ADA-ES, Inc. Control of wet scrubber oxidation inhibitor and byproduct recovery
US10159931B2 (en) 2012-04-11 2018-12-25 ADA-ES, Inc. Control of wet scrubber oxidation inhibitor and byproduct recovery
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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
US10767130B2 (en) 2012-08-10 2020-09-08 ADA-ES, Inc. Method and additive for controlling nitrogen oxide emissions
US11384304B2 (en) 2012-08-10 2022-07-12 ADA-ES, Inc. Method and additive for controlling nitrogen oxide emissions
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US10350545B2 (en) 2014-11-25 2019-07-16 ADA-ES, Inc. Low pressure drop static mixing system

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