US1112547A - Composition of matter to be used as an oxygenizer in connection with combustibles. - Google Patents
Composition of matter to be used as an oxygenizer in connection with combustibles. Download PDFInfo
- Publication number
- US1112547A US1112547A US80252813A US1913802528A US1112547A US 1112547 A US1112547 A US 1112547A US 80252813 A US80252813 A US 80252813A US 1913802528 A US1913802528 A US 1913802528A US 1112547 A US1112547 A US 1112547A
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- US
- United States
- Prior art keywords
- oxygenizer
- fuel
- combustibles
- connection
- matter
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- 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
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/10—Treating solid fuels to improve their combustion by using additives
Definitions
- ADoLrnn Molun LOUIS l lAMON
- Eunns'r llnss all of the city of Montreal, province of Quebec, Canada, have jointly invented a certain new and useful Composition of Matter to be Used as an Oxygenizer in Connection with Combustibles, and of which the ti'illowingr is a specification.
- the oxygenizer is to be sprayed over the fuel to mix therewith and thus augment coinbustion by supplying the oxygen necessary to insure complete combustion and therefore the n'iaximum efficiency of the fuel.
- the oxygenizer is made up of chlorate of sodium and permanganate of sodium, these chemicals being respectively dissolved in Water and mixed together.
- Vt hile the proportions of the constituents may vary according to the requirements of each case the preferred mixture is prepared as follows: 80 parts. by weight, of chlorate of sodium is dissolved at ordinary temperature in 100 parts, by Weight, of Water and 100 parts, by Weight, of permanganate of sodium is dissolved at critlii'iary temperature in 100 parts, by Weight, of vvater. The two solutions are then mixed, the reaction being that the resultant mixture will contain, by Weight, 526 per cent. of Water, 21.0 per cent. of chlorate or sodium and QtL-l per cent. of permanganate of sodium.
- a vehicle or carrier is provided, the mixture, being diluted preferably with 50 times its volume of vater and the quantity supplied ton of fuel varied in connection with rlitlerent fuels.
- Vt hen low grade coal or the like is used, the oxygenizer composed as above described, is diluted with 50 times its volume of water, and is sprayed overthe fuel, prior to the burning of the same. at the rate ot about ten (lOl gallons for e: ch ton of fuel. in connection with coke the mixture supplied at the rate oi twenty-live gallons for each ton of fuel and to secure the most eliicient Specification or Letters Patent.
- the heat of the furnace acts on the solution and fur nishes the oxygen necessary for thecombustion of the particles of carbon in suspension in the smoke while the provision of the oxygen also permits of the reduction of the amount ct air admitted to the furnace.
- the decreaser draft will result in a smaller consumption of fuel While the heated gases will pass more slowly am one the Water tubes and therefore prolong their heating period. While the consumption of the suspended carbon will avoid the deposit of soot in the tubes and on boiler sections thus leaving them in the best condition for heating.
- the use of our oxygenizer diet is commonly and non-technically known as cinders and SCOJlh.
- the water employed for diluting the mixture also serves as a vehicle to enable the solution to penetrate to all parts of the mass being treated and particularly to the cinder-s and scorize while the oxyge brings the particles of coal contained in the cinders into contact with the oxygen developed under action at the heat ot the tn rnace permits 1 the combustion thereof.
- an enriching composition consisting of chlorate of sodium, permanganate of sodium and Water the latter in quantity by Weight approximately equaling the combined quantities by Weight of said salts.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Treating Waste Gases (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Description
i wimlaaso CQMPQSIIION OF MATTER TO BE USED AS AN OXYGENIZER IN F a u .T 'irrr. a
or MONTREAL, eunsnc, CANADA.
counncrxou WITH COI'IIBUSTIBLES.
To (117 Whom it may (102100171,-
Be it known that we, ADoLrnn Molun, LOUIS l lAMON, and Eunns'r llnss, all of the city of Montreal, Province of Quebec, Canada, have jointly invented a certain new and useful Composition of Matter to be Used as an Oxygenizer in Connection with Combustibles, and of which the ti'illowingr is a specification.
The oxygenizer is to be sprayed over the fuel to mix therewith and thus augment coinbustion by supplying the oxygen necessary to insure complete combustion and therefore the n'iaximum efficiency of the fuel.
The oxygenizer is made up of chlorate of sodium and permanganate of sodium, these chemicals being respectively dissolved in Water and mixed together.
Vt hile the proportions of the constituents may vary according to the requirements of each case the preferred mixture is prepared as follows: 80 parts. by weight, of chlorate of sodium is dissolved at ordinary temperature in 100 parts, by Weight, of Water and 100 parts, by Weight, of permanganate of sodium is dissolved at critlii'iary temperature in 100 parts, by Weight, of vvater. The two solutions are then mixed, the reaction being that the resultant mixture will contain, by Weight, 526 per cent. of Water, 21.0 per cent. of chlorate or sodium and QtL-l per cent. of permanganate of sodium.
To secure the best results a vehicle or carrier is provided, the mixture, being diluted preferably with 50 times its volume of vater and the quantity supplied ton of fuel varied in connection with rlitlerent fuels.
The great solubility of chlorate and permaiu niale of sodium enables a pmvertul oxvgenizer to be produced in reduced volume, while there is no danger troir the infiaminability of the chlorate it is maintained in a permanent sta of humidity by r ason of the great hygroscopic qualities of the permanganate of sodium with which it is mixed.
Vt hen low grade coal or the like is used, the oxygenizer composed as above described, is diluted with 50 times its volume of water, and is sprayed overthe fuel, prior to the burning of the same. at the rate ot about ten (lOl gallons for e: ch ton of fuel. in connection with coke the mixture supplied at the rate oi twenty-live gallons for each ton of fuel and to secure the most eliicient Specification or Letters Patent.
' Patented cm. s, ire-la Application filed November 22, 1813. Serial No. 802,528.
results when spraying What is commonly and non-tecn1ically known as cinders or scoriie" with the solution, it has been found: preferable to spray the solution at the rate of titty gallons for each ton of fuel.
lleretofore the presence or" carbon in the smoke a rising from the burning fuel in furnaces or the like, coated the Water tubes of the boiler which therefore could not be properly heated and the draft necessarily employed was such as to quickly sweep the heated gases up the chimney and therefore prevent all but a short heating action upon the tubes.
When using the oxygenizer the heat of the furnace acts on the solution and fur nishes the oxygen necessary for thecombustion of the particles of carbon in suspension in the smoke while the provision of the oxygen also permits of the reduction of the amount ct air admitted to the furnace. The decreaser draft will result in a smaller consumption of fuel While the heated gases will pass more slowly am one the Water tubes and therefore prolong their heating period. While the consumption of the suspended carbon will avoid the deposit of soot in the tubes and on boiler sections thus leaving them in the best condition for heating.
ll the use of our oxygenizer diet is commonly and non-technically known as cinders and SCOJlh. can be used as combustibles as the same time as coal and the maxinnun etliciency secured ovvingto the fact that. the water employed for diluting the mixture also serves as a vehicle to enable the solution to penetrate to all parts of the mass being treated and particularly to the cinder-s and scorize while the oxyge brings the particles of coal contained in the cinders into contact with the oxygen developed under action at the heat ot the tn rnace permits 1 the combustion thereof. tam pra'iportion of on i i dciicnipositi of the i used.
What weclaim as follows 1. As a means of aiding the complete combustion of fuel and residues, an enriching composition consisting of chlorate of sodium, permanganate of sodium and Water the latter in quantity by Weight approximately equaling the combined quantities by Weight of said salts.
9,. As a means for aiding the complete combustion of fuel and residues, an enrich.-
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US80252813A US1112547A (en) | 1913-11-22 | 1913-11-22 | Composition of matter to be used as an oxygenizer in connection with combustibles. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US80252813A US1112547A (en) | 1913-11-22 | 1913-11-22 | Composition of matter to be used as an oxygenizer in connection with combustibles. |
Publications (1)
Publication Number | Publication Date |
---|---|
US1112547A true US1112547A (en) | 1914-10-06 |
Family
ID=3180732
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US80252813A Expired - Lifetime US1112547A (en) | 1913-11-22 | 1913-11-22 | Composition of matter to be used as an oxygenizer in connection with combustibles. |
Country Status (1)
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US (1) | US1112547A (en) |
Cited By (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2704523A (en) * | 1955-03-22 | F walters | ||
US3328137A (en) * | 1965-08-27 | 1967-06-27 | United States Packaging Corp | Rapid ignition charcoal briquette and method of making the same |
US4344847A (en) * | 1979-02-13 | 1982-08-17 | Grenet Edouard P | Process for obtaining energy, soft water and by-products from aqueous substances |
US4759772A (en) * | 1987-07-22 | 1988-07-26 | Carus Corporation | Method of controlling self-ignition of low rank coal |
US7507083B2 (en) | 2005-03-17 | 2009-03-24 | Douglas C Comrie | 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 |
US8124036B1 (en) | 2005-10-27 | 2012-02-28 | ADA-ES, Inc. | Additives for mercury oxidation in coal-fired power plants |
US8150776B2 (en) | 2006-01-18 | 2012-04-03 | Nox Ii, Ltd. | Methods of operating a coal burning facility |
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 |
US8574324B2 (en) | 2004-06-28 | 2013-11-05 | Nox Ii, Ltd. | Reducing sulfur gas emissions resulting from the burning of carbonaceous fuels |
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 |
-
1913
- 1913-11-22 US US80252813A patent/US1112547A/en not_active Expired - Lifetime
Cited By (65)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2704523A (en) * | 1955-03-22 | F walters | ||
US3328137A (en) * | 1965-08-27 | 1967-06-27 | United States Packaging Corp | Rapid ignition charcoal briquette and method of making the same |
US4344847A (en) * | 1979-02-13 | 1982-08-17 | Grenet Edouard P | Process for obtaining energy, soft water and by-products from aqueous substances |
US4759772A (en) * | 1987-07-22 | 1988-07-26 | Carus Corporation | Method of controlling self-ignition of low rank coal |
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 |
US8501128B2 (en) | 2005-03-17 | 2013-08-06 | Nox Ii, Ltd. | 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 |
US7955577B2 (en) | 2005-03-17 | 2011-06-07 | 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 |
US9822973B2 (en) | 2005-03-17 | 2017-11-21 | Nox Ii, Ltd. | Reducing mercury emissions from the burning of coal |
US8226913B2 (en) | 2005-03-17 | 2012-07-24 | Nox Ii, Ltd. | Reducing mercury emissions from the burning of coal |
US9169453B2 (en) | 2005-03-17 | 2015-10-27 | Nox Ii, Ltd. | Sorbents for coal combustion |
US11732889B2 (en) | 2005-03-17 | 2023-08-22 | Nox Ii, Ltd. | Reducing mercury emissions from the burning of coal by remote sorbent addition |
US11732888B2 (en) | 2005-03-17 | 2023-08-22 | Nox Ii, Ltd. | Sorbents for coal combustion |
US7758827B2 (en) | 2005-03-17 | 2010-07-20 | Nox Ii, Ltd. | 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 |
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 |
US7776301B2 (en) | 2005-03-17 | 2010-08-17 | Nox Ii, Ltd. | Reducing mercury emissions from the burning of coal |
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 |
US10670265B2 (en) | 2005-03-17 | 2020-06-02 | Nox Ii, Ltd. | 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 |
US10641483B2 (en) | 2005-03-17 | 2020-05-05 | Nox Ii, Ltd. | Sorbents for coal combustion |
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 |
US7507083B2 (en) | 2005-03-17 | 2009-03-24 | Douglas C Comrie | Reducing mercury emissions from the burning of coal |
US9945557B2 (en) | 2005-03-17 | 2018-04-17 | Nox Ii, Ltd. | Sorbents for coal combustion |
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 |
US8150776B2 (en) | 2006-01-18 | 2012-04-03 | Nox Ii, Ltd. | Methods of operating a coal burning facility |
US8496894B2 (en) | 2010-02-04 | 2013-07-30 | 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 |
US8372362B2 (en) | 2010-02-04 | 2013-02-12 | 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 |
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