WO2015003230A1 - Method for catalyzing the combustion of carbon-containing solid fuels - Google Patents

Method for catalyzing the combustion of carbon-containing solid fuels Download PDF

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Publication number
WO2015003230A1
WO2015003230A1 PCT/BG2014/000013 BG2014000013W WO2015003230A1 WO 2015003230 A1 WO2015003230 A1 WO 2015003230A1 BG 2014000013 W BG2014000013 W BG 2014000013W WO 2015003230 A1 WO2015003230 A1 WO 2015003230A1
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Prior art keywords
metals
salts
oxides
metalloids
carbon
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PCT/BG2014/000013
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French (fr)
Inventor
Hristo Atanasov Kovachki
Rumen Ivanov KUNEV
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Hristo Atanasov Kovachki
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Publication of WO2015003230A1 publication Critical patent/WO2015003230A1/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
    • C10L9/12Oxidation means, e.g. oxygen-generating 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • 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
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/04Raw material of mineral origin to be used; Pretreatment thereof

Definitions

  • the invention is based on the use of chemical methods for ameliorating the combustion of solid carbon-containing fuels.
  • the aim is to reduce the unburned residue after the combustion process and to increase the efficiency of the combustion installations.
  • This method focuses on reducing the unburned residue (carbon) in the use of solid carbon-containing raw materials.
  • the main reason for this is that generally the loss of power capacity due to unburned carbon is greater than as a result of unburned carbon monoxide.
  • the method for catalyzing the combustion of carbon-containing solid fuels consists in the addition of salts of transition metals, weak metals or metalloids or combination thereof to carbon-containing fuel, wherein processes proceed in the combustion chamber, leading to their decomposition to oxides.
  • the metal oxides formed react with the unburned carbon by oxidizing it. After their reduction the metals fall into the lower part of the combustion chamber where they are oxidized again by the air, creating centres of high temperature.
  • metals listed are significantly heavier than carbon and their oxides and after the reduction they fall into the lower part of the combustion chamber wherein they are oxidized again by the air, forming centres of high temperature, which facilitated the combustion of the unburned carbon particles falling with them.
  • the main reason for the use of metal salts rather than metal oxides as an additive to carbon-containing fuels is that when they are wet, they adhere on (impregnate) easier the fuel particles . This makes it possible all the above reactions to proceed on the contact surface of the fuel and to contribute to its maximum combustion.
  • salts of the transition metals are used: scandium (Sc), titanium (Ti), vanadium (V), chromium (Cr), manganese (Mn), iron (Fe), cobalt (Co), nickel (Ni), copper (Cu), zinc (Zn), yttrium (Y), zirconium (Zr), niobium (Nb), molybdenum (Mo), technetium (Tc), ruthenium (Ru), rhodium (Rh), palladium (Pd), silver (Ag), cadmium (Cd), lanthanides, hafnium (Hf), tantalum (Ta), tungsten (W), rhenium (Re), osmium (Os), iridium (Ir), platinum (Pt), gold (Au), mercury (Hg), actinides, as well as combinations of two or more salts of these metals.
  • salts of the following weak metals are added: aluminium (Al), gallium (Ga), germanium (Ge), indium (In), tin (Sn), antimony (Sb), thallium (TI), lead (Pb), bismuth (Bi), polonium (Po), as well as combinations of two or more salts of these metals.
  • salts of the metalloids are added: boron (B), silicon (Si), arsenic (As), tellurium (Te), as well as combinations of two or more salts of these metals.
  • combinations are also added of two or more salts of the above transition metals, weak metals and metalloids, as well as their oxides and combinations of two or more of their oxides.
  • salts, oxides and/or hydroxides of the alkaline earth metals are used: beryllium (Be), magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba), radium (Ra) and salts, oxides and/or hydroxides of the alkaline metals: lithium (Li), sodium (Na), potassium ( ), rubidium (Ru), francium (Fr), as well as combinations of salts, oxides and/or hydroxides of the said alkaline and alkaline earth metals.
  • Be beryllium
  • Mg magnesium
  • Ca calcium
  • Ba barium
  • Ra radium
  • salts, oxides and/or hydroxides of the alkaline metals lithium (Li), sodium (Na), potassium ( ), rubidium (Ru), francium (Fr), as well as combinations of salts, oxides and/or hydroxides of the said alkaline and alkaline earth metals.
  • the size of the particles in the catalyst mixture should be smaller or at most similar to the size of the particles of the carbon-containing fuel.
  • the aim is the desired effect to be obtained with minimal addition of catalyst.
  • Carbon-containing fuels include, but not only, fossil fuels (coal, oil shale, etc.), biomass (wood, grain stalks, wood processing waste, etc.), petrocoke, oil paste and other carbon-containing residues from petroleum refining.
  • the combustion of carbon-containing fuels includes power boilers for steam and electricity, boilers for heating power stations, waste incinerators, gasifiers and other combustion installations.
  • the catalyst used is a mixture of MnS0 4 , Fe 2 0 3 and AI 2 S0 4 .
  • catalyst without promoter is dosed in proportion 0.5%, 1% and 2% relative to the main fuel (coal).
  • 5 and 6 promoter is added to the catalyst (a mixture of Na 2 C0 3 and Ca(OH) 2 ). Its amount is 10% relative to the catalyst.
  • promoter enhances the catalytic effect, while maintaining the relationship between the catalyst and the decrease of the unburned part.

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Catalysts (AREA)

Abstract

Method for catalyzing combustion processes, using a variety of carbon- containing raw materials by adding compounds of transition metals, weak metals or metalloids, promoted with compounds of alkaline and alkaline earth metals.

Description

METHOD FOR CATALYZING THE COMBUSTION OF
CARBON-CONTAINING SOLID FUELS
FIELD OF THE INVENTION
Combustion of carbon-containing substances in combustion installations.
BACKGROUND OF THE INVENTION
In the use of solid carbon-containing raw materials as fuels, the process providing the main quantity of energy is:
Cs + ½02 «— » CO9 + Qi [1 ]
CO + ¾02 <—► CO9 + Q.2 [2]
In the combustion there is always a residue of unburned carbon and carbon monoxide. The incomplete combustion of fuel and intermediate products is one of the important factors determining the coefficient of efficiency of the combustion installations.
The methods known for the optimization of combustion processes are based on the addition of various chemical compounds for ameliorating the combustion of carbon monoxide (equation [2]) in the area of the flame or in flue gases in order to obtain a higher energy yield and hence a higher coefficient of efficiency in the combustion installation.
TECHNICAL SUMMARY OF THE INVENTION
The invention is based on the use of chemical methods for ameliorating the combustion of solid carbon-containing fuels. The aim is to reduce the unburned residue after the combustion process and to increase the efficiency of the combustion installations.
This method focuses on reducing the unburned residue (carbon) in the use of solid carbon-containing raw materials. The main reason for this is that generally the loss of power capacity due to unburned carbon is greater than as a result of unburned carbon monoxide.
One of the reasons for the incomplete combustion of carbon is that it is impossible for the ignition temperature to reach some of the particles of the fuel fed into the combustion chamber.
The method for catalyzing the combustion of carbon-containing solid fuels, according to the invention, consists in the addition of salts of transition metals, weak metals or metalloids or combination thereof to carbon-containing fuel, wherein processes proceed in the combustion chamber, leading to their decomposition to oxides. The metal oxides formed react with the unburned carbon by oxidizing it. After their reduction the metals fall into the lower part of the combustion chamber where they are oxidized again by the air, creating centres of high temperature.
Upon the addition of salts of transition metals, weak metals or metalloids or combination thereof to carbon-containing fuel in the combustion chamber processes occur, leading to their decomposition to oxides, for example: nC03 → MnO + C02 [3]
FeC03 → FeO + C02 [4]
2CuS04 + C→ 2CuO + 2S02 + C02 [5]
CuS04 + CO→ CuO + S02 + C02 [63
The resulting metal oxides react with the unburned carbon by oxidizing it:
FeO + C <— Fe + CO + Qi [7]
FeO + CO <—► Fe + C02 + Q2 [8]
All metals listed are significantly heavier than carbon and their oxides and after the reduction they fall into the lower part of the combustion chamber wherein they are oxidized again by the air, forming centres of high temperature, which facilitated the combustion of the unburned carbon particles falling with them. The main reason for the use of metal salts rather than metal oxides as an additive to carbon-containing fuels is that when they are wet, they adhere on (impregnate) easier the fuel particles . This makes it possible all the above reactions to proceed on the contact surface of the fuel and to contribute to its maximum combustion.
For implementing the method according to the present invention salts of the transition metals are used: scandium (Sc), titanium (Ti), vanadium (V), chromium (Cr), manganese (Mn), iron (Fe), cobalt (Co), nickel (Ni), copper (Cu), zinc (Zn), yttrium (Y), zirconium (Zr), niobium (Nb), molybdenum (Mo), technetium (Tc), ruthenium (Ru), rhodium (Rh), palladium (Pd), silver (Ag), cadmium (Cd), lanthanides, hafnium (Hf), tantalum (Ta), tungsten (W), rhenium (Re), osmium (Os), iridium (Ir), platinum (Pt), gold (Au), mercury (Hg), actinides, as well as combinations of two or more salts of these metals.
For implementing the method according to the present invention salts of the following weak metals are added: aluminium (Al), gallium (Ga), germanium (Ge), indium (In), tin (Sn), antimony (Sb), thallium (TI), lead (Pb), bismuth (Bi), polonium (Po), as well as combinations of two or more salts of these metals.
For implementing the method according to the present invention salts of the metalloids are added: boron (B), silicon (Si), arsenic (As), tellurium (Te), as well as combinations of two or more salts of these metals.
According to the invention, combinations are also added of two or more salts of the above transition metals, weak metals and metalloids, as well as their oxides and combinations of two or more of their oxides.
In experiments carried out with various combinations of the above mentioned metal salts with the addition of salts of alkaline and alkaline earth metals, better results are observed than without them. This is probably due to the fact that the salts and the oxides of alkaline and alkaline earth metals have lower melting points in comparison with the others. Therefore they act as an adhesive between the particles of the fuel and the salts of the transition metals, weak metals or metalloids in the combustion zone, where the water is already evaporated. This prolongs the retention time of all additives to the fuel particles in the chamber and results in more complete combustion of carbon. In this way the alkaline and alkaline earth metals act as promoters.
For implementing the method according to the invention when using promoters to the additives, salts, oxides and/or hydroxides of the alkaline earth metals are used: beryllium (Be), magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba), radium (Ra) and salts, oxides and/or hydroxides of the alkaline metals: lithium (Li), sodium (Na), potassium ( ), rubidium (Ru), francium (Fr), as well as combinations of salts, oxides and/or hydroxides of the said alkaline and alkaline earth metals.
The use of promoters allows in addition to the salts of the transition metals, weak metals and metalloids, their oxides to be also used. Thereby adverse side effects on the equipment will be avoided, resulting from the formation of halides when using such salts. In this case reactions 3 to 6 are skipped and only the reduction reactions proceed:
MexOy + (y-x)C→ xMeO + (y-x)CO + Q3 [9]
MeO + C <— > Me + CO + Q4 [10] and oxidation to metal oxides:
Me + 02 <— > 2MeO + Q5 [1 1]
Here the heats of reactions 9 and 10 are with sign plus and minus depending on the metal oxide used.
The size of the particles in the catalyst mixture should be smaller or at most similar to the size of the particles of the carbon-containing fuel. The aim is the desired effect to be obtained with minimal addition of catalyst.
Carbon-containing fuels include, but not only, fossil fuels (coal, oil shale, etc.), biomass (wood, grain stalks, wood processing waste, etc.), petrocoke, oil paste and other carbon-containing residues from petroleum refining.
The combustion of carbon-containing fuels includes power boilers for steam and electricity, boilers for heating power stations, waste incinerators, gasifiers and other combustion installations.
EMBODIMENTS
In the Tables attached below the summarized results are shown from tests in two power boilers with different carbon content in the solid residue - ash and slag. The catalyst used is a mixture of MnS04, Fe203 and AI2S04. In both Tables in experiments 1 , 2 and 3 catalyst without promoter is dosed in proportion 0.5%, 1% and 2% relative to the main fuel (coal). In experiments 4, 5 and 6 promoter is added to the catalyst (a mixture of Na2C03 and Ca(OH)2). Its amount is 10% relative to the catalyst.
In Table 1 , where the amount of carbon in the solid waste is higher, certain correlation is observed between the dose of the catalyst and the decrease of the unburned portion. More serious is the decrease at dosages 0.5% and 1 %. This means that at higher doses of catalyst its distribution on the surface of the fuel particles is uneven and it does not bring the required effect. In this case a dose higher than 2% is not necessary. Of course the concrete ratio will depend on the compounds used and the ratio thereof.
The addition of promoter enhances the catalytic effect, while maintaining the relationship between the catalyst and the decrease of the unburned part.
In Table 2 the same relationships are observed, but on a smaller scale, as the boiler itself operates with smaller loss of carbon in the ash and slag.

Claims

PATENT CLAIMS
1 . A method for catalyzing the combustion of carbon-containing solid fuel characterized in that to the carbon-containing fuel salts of transition metals, weak metals or metalloids are added or combination thereof and in the combustion chamber processes proceed, leading to their decomposition to oxides, the obtained metal oxides react with the unburned carbon by oxidizing it. After their reduction the metals fall into the lower part of the combustion chamber where they are oxidized again by the air, creating centres of high temperature, which facilitated the combustion of the unburned carbon particles falling with them.
2. A method according to claim 1 characterized in that salts, oxides and/or hydroxides are added of transition metals, weak metals or metalloids or combination thereof as promoters.
3. A method according to claims 1 and 2 characterized in that when promoters are used, besides salts of transition metals, weak metals or metalloids their oxides are also used, wherein the reactions of reduction and oxidation of the metal oxides proceed only.
4 A method according to claims 1 , 2 and 3 characterized in that salts of the transition metals are added: scandium (Sc), titanium (Ti), vanadium (V), chromium (Cr), manganese (Mn), iron (Fe), cobalt (Co), nickel (Ni), copper (Cu), zinc (Zn), yttrium (Y), zirconium (Zr), niobium (Nb), molybdenum (Mo), technetium (Tc), ruthenium (Ru), rhodium (Rh), palladium (Pd), silver (Ag), cadmium (Cd), lanthanides, hafnium (Hf), tantalum (Ta), tungsten (W), rhenium (Re), osmium (Os), iridium (Ir), platinum (Pt), gold (Au), mercury (Hg), actinides, as well as combinations of two or more salts of these metals.
5. A method according to claims 1 , 2 and 3 characterized in that salts of the weak metals are added: aluminium (Al), gallium (Ga), germanium (Ge), indium (In), tin (Sn), antimony (Sb), thallium (TI), lead (Pb), bismuth (Bi), polonium (Po), as well as combinations of two or more salts of these metals.
6. A method according to claims 1 , 2 and 3 characterized in that salts of the metalloids are added: boron (B), silicon (Si), arsenic (As), tellurium (Te), as well as combinations of two or more salts of these metals.
7. A method according to claims 1 , 2 and 3 characterized in that combinations of two or more salts are added of the transition metals, weak metals or metalloids, specified in claims 4, 5 and 6.
8. A method according to claims 1 , 2 and 3 characterized in that an oxide or combination of two or more oxides of the transition metals, the weak metals and the metalloids, specified in claims 5, 6 and 7.
9. A method according to claims 1 , 2 and 3 characterized in that salts, oxides and/or hydroxides of the alkaline earth metals are used: beryllium (Be), magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba), radium ( a) as promoters to the additives specified in claims 4, 5, 6, 7 and 8.
10. A method according to claims 1 , 2 and 3 characterized in that salts, oxides and/or hydroxides of the alkaline metals are used: lithium (Li), sodium (Na), potassium (K), rubidium (Ru), francium (Fr) as promoters to the additives specified in claims 4, 5, 6, 7 and 8.
PCT/BG2014/000013 2013-07-12 2014-03-25 Method for catalyzing the combustion of carbon-containing solid fuels WO2015003230A1 (en)

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BG111535A BG66821B1 (en) 2013-07-12 2013-07-12 Method for catalyzing the combustion of carbon-containing solid fuels

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105219477A (en) * 2015-11-10 2016-01-06 内蒙古科技大学 A kind of fluidized bed preparation method for material of area load rare earth oxide catalyst
CN105238489A (en) * 2015-10-15 2016-01-13 阳开金 Powdery coal-saving combustion improver and preparation method thereof
CN106190426A (en) * 2016-08-12 2016-12-07 安徽昌信生物质能源有限公司 A kind of auxiliary agent added in biomass fuel
CN106190403A (en) * 2016-08-12 2016-12-07 安徽昌信生物质能源有限公司 A kind of low-carbon environment-friendly biomass fuel and preparation method
CN106244280A (en) * 2016-08-12 2016-12-21 安徽昌信生物质能源有限公司 A kind of biomass fuel and preparation method
CN111548836A (en) * 2020-05-11 2020-08-18 朱彬苇 Preparation method of autocatalytic high-calorific-value biomass granular fuel
CN114736725A (en) * 2021-01-08 2022-07-12 西安近代化学研究所 Boron-based solid fuel capable of regulating and controlling energy release and preparation method thereof

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CH202497A (en) * 1936-02-18 1939-01-31 Benjamin Toustou Jean Process for improving solid fuels.
WO2003080541A1 (en) * 2002-03-22 2003-10-02 Csir Exothermic combustible products
US20070180760A1 (en) * 2006-02-09 2007-08-09 Headwaters Nanokinetix, Inc. Crystalline nanocatalysts for improving combustion properties of fuels and fuel compositions incorporating such catalysts
US20090199459A1 (en) * 2008-02-13 2009-08-13 Taylor David W Form of coal particles
US20120311924A1 (en) * 2001-01-10 2012-12-13 Richardson Melvin A Methods of improving combustion of solid fuels

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH202497A (en) * 1936-02-18 1939-01-31 Benjamin Toustou Jean Process for improving solid fuels.
US20120311924A1 (en) * 2001-01-10 2012-12-13 Richardson Melvin A Methods of improving combustion of solid fuels
WO2003080541A1 (en) * 2002-03-22 2003-10-02 Csir Exothermic combustible products
US20070180760A1 (en) * 2006-02-09 2007-08-09 Headwaters Nanokinetix, Inc. Crystalline nanocatalysts for improving combustion properties of fuels and fuel compositions incorporating such catalysts
US20090199459A1 (en) * 2008-02-13 2009-08-13 Taylor David W Form of coal particles

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105238489A (en) * 2015-10-15 2016-01-13 阳开金 Powdery coal-saving combustion improver and preparation method thereof
CN105219477A (en) * 2015-11-10 2016-01-06 内蒙古科技大学 A kind of fluidized bed preparation method for material of area load rare earth oxide catalyst
CN105219477B (en) * 2015-11-10 2018-02-16 内蒙古科技大学 A kind of fluidized bed preparation method for material of area load rare earth oxide catalyst
CN106190426A (en) * 2016-08-12 2016-12-07 安徽昌信生物质能源有限公司 A kind of auxiliary agent added in biomass fuel
CN106190403A (en) * 2016-08-12 2016-12-07 安徽昌信生物质能源有限公司 A kind of low-carbon environment-friendly biomass fuel and preparation method
CN106244280A (en) * 2016-08-12 2016-12-21 安徽昌信生物质能源有限公司 A kind of biomass fuel and preparation method
CN111548836A (en) * 2020-05-11 2020-08-18 朱彬苇 Preparation method of autocatalytic high-calorific-value biomass granular fuel
CN111548836B (en) * 2020-05-11 2021-06-04 上海积鼎信息科技有限公司 Preparation method of autocatalytic high-calorific-value biomass granular fuel
CN114736725A (en) * 2021-01-08 2022-07-12 西安近代化学研究所 Boron-based solid fuel capable of regulating and controlling energy release and preparation method thereof
CN114736725B (en) * 2021-01-08 2023-07-18 西安近代化学研究所 Boron-based solid fuel capable of regulating and controlling energy release and preparation method thereof

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