AR072502A1 - PROCESS TO REDUCE THE COHESIVITY AND / OR ADHERENCE OF ESCORIA IN A CHAMBER OF COMBUSTION AND PROCESS OF CLEANING AND MAINTENANCE OF A BOILER. - Google Patents

PROCESS TO REDUCE THE COHESIVITY AND / OR ADHERENCE OF ESCORIA IN A CHAMBER OF COMBUSTION AND PROCESS OF CLEANING AND MAINTENANCE OF A BOILER.

Info

Publication number
AR072502A1
AR072502A1 ARP090102634A ARP090102634A AR072502A1 AR 072502 A1 AR072502 A1 AR 072502A1 AR P090102634 A ARP090102634 A AR P090102634A AR P090102634 A ARP090102634 A AR P090102634A AR 072502 A1 AR072502 A1 AR 072502A1
Authority
AR
Argentina
Prior art keywords
slag
reagent
carbon
pounds
per ton
Prior art date
Application number
ARP090102634A
Other languages
Spanish (es)
Original Assignee
Fuel Tech Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Fuel Tech Inc filed Critical Fuel Tech Inc
Publication of AR072502A1 publication Critical patent/AR072502A1/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C99/00Subject-matter not provided for in other groups of this subclass
    • 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/06Use of additives to fuels or fires for particular purposes for facilitating soot removal
    • 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/04Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J3/00Removing solid residues from passages or chambers beyond the fire, e.g. from flues by soot blowers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J7/00Arrangement of devices for supplying chemicals to fire
    • 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
    • C10L2200/00Components of fuel compositions
    • C10L2200/02Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
    • C10L2200/0204Metals or alloys
    • C10L2200/0213Group II metals: Be, Mg, Ca, Sr, Ba, Ra, Zn, Cd, Hg
    • 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
    • C10L2200/00Components of fuel compositions
    • C10L2200/02Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
    • C10L2200/0204Metals or alloys
    • C10L2200/0218Group III metals: Sc, Y, Al, Ga, In, Tl
    • 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
    • C10L2200/00Components of fuel compositions
    • C10L2200/02Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
    • C10L2200/0254Oxygen containing compounds
    • 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
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/14Injection, e.g. in a reactor or a fuel stream during fuel production
    • C10L2290/141Injection, e.g. in a reactor or a fuel stream during fuel production of additive or catalyst
    • 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
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/18Spraying or sprinkling

Abstract

Se describe un proceso que aumenta el rendimiento de una cámara de combustion alimentada con carbon que tiene alto contenido de hierro y/o calcio, reduciendo la tendencia a la formacion de escorias sobre superficies de intercambio térmico y cambiando la naturaleza de la escoria para su más fácil remocion. El proceso incluye quemar un carbon formador de escoria, que tiene alto contenido de hierro y/o calcio, con un exceso total de oxígeno; mover los gases de combustion resultantes a través del equipo de intercambio térmico bajo condiciones las cuales causan el enfriamiento de la escoria formada quemando el combustible; y con anterioridad al contacto con dicho equipo de intercambio térmico, introducir trihidroxido de aluminio acuoso en cantidades y con tamanos de gota y concentraciones eficaces para disminuir la velocidad de ensuciamiento, y preferentemente, aumentar la fragilidad de la escoria resultante. Deseablemente, el reactivo de trihidroxido de aluminio es introducido en la forma de un líquido acuoso y se emplea dinámica computacional de fluidos para determinar las velocidades de flujo y seleccionar las velocidades de introduccion de reactivo, punto(s) de introduccion de reactivo, concentracion de reactivo, tamano de gota del reactivo y/o momento del reactivo, En un aspecto preferido, la velocidad de alimentacion será de hasta aproximadamente 2,72 kg (6 libras) de ATH por tonelada y preferentemente con hasta aproximadamente 0,90 kg (2 libras) de Mg(OH)2 por tonelada de carbon. También se proporciona un proceso para la limpieza y mantenimiento del estado limpio de una cámara de combustion. Reivindicacion 9: Un proceso de limpieza y mantenimiento de una caldera caracterizado porque comprende un régimen de dosificacion inicial de entre aproximadamente 1,36 y 2,72 kg (3 y 6 libras) de ATH por tonelada de carbon y aproximadamente 0,45 a 0,90 kg (1 a 2 libras) de Mg(OH)2 por tonelada de carbon durante un tiempo suficiente para reducir la escoria, seguido por una reduccion de la dosificacion de entre aproximadamente 10 a aproximadamente 50% de los valores iniciales para mantener la cámara de combustion limpia y funcionando de manera eficaz.A process is described that increases the performance of a combustion chamber fed with carbon that has a high content of iron and / or calcium, reducing the tendency to slag formation on heat exchange surfaces and changing the nature of the slag for further easy removal The process includes burning a slag-forming carbon, which is high in iron and / or calcium, with a total excess of oxygen; move the resulting combustion gases through the heat exchange equipment under conditions which cause the slag formed to burn by burning the fuel; and prior to contact with said thermal exchange equipment, introduce aqueous aluminum trihydroxide in amounts and with effective drop sizes and concentrations to decrease the fouling rate, and preferably, increase the fragility of the resulting slag. Desirably, the aluminum trihydroxide reagent is introduced in the form of an aqueous liquid and computational fluid dynamics is used to determine flow rates and select reagent introduction rates, reagent introduction point (s), concentration of reagent, reagent drop size and / or reagent time, In a preferred aspect, the feed rate will be up to about 2.72 kg (6 pounds) of ATH per ton and preferably with up to about 0.90 kg (2 pounds) of Mg (OH) 2 per ton of carbon. A process for cleaning and maintaining the clean state of a combustion chamber is also provided. Claim 9: A cleaning and maintenance process of a boiler characterized in that it comprises an initial dosing regime of between approximately 1.36 and 2.72 kg (3 and 6 pounds) of ATH per ton of carbon and approximately 0.45 to 0 , 90 kg (1 to 2 pounds) of Mg (OH) 2 per ton of carbon for a time sufficient to reduce slag, followed by a dosage reduction of between about 10 to about 50% of the initial values to maintain combustion chamber clean and working efficiently.

ARP090102634A 2008-07-11 2009-07-13 PROCESS TO REDUCE THE COHESIVITY AND / OR ADHERENCE OF ESCORIA IN A CHAMBER OF COMBUSTION AND PROCESS OF CLEANING AND MAINTENANCE OF A BOILER. AR072502A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US8000408P 2008-07-11 2008-07-11

Publications (1)

Publication Number Publication Date
AR072502A1 true AR072502A1 (en) 2010-09-01

Family

ID=41507460

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP090102634A AR072502A1 (en) 2008-07-11 2009-07-13 PROCESS TO REDUCE THE COHESIVITY AND / OR ADHERENCE OF ESCORIA IN A CHAMBER OF COMBUSTION AND PROCESS OF CLEANING AND MAINTENANCE OF A BOILER.

Country Status (18)

Country Link
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)
TW (1) TWI482852B (en)
WO (1) WO2010006325A1 (en)

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Publication number Priority date Publication date Assignee Title
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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Also Published As

Publication number Publication date
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
EP2318489B1 (en) 2015-09-02
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
CA2729959A1 (en) 2010-01-14
AU2009268391A1 (en) 2010-01-14
US20100006014A1 (en) 2010-01-14
CN102089413B (en) 2013-12-18

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Legal Events

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FG Grant, registration
FD Application declared void or lapsed, e.g., due to non-payment of fee