WO2011070450A1 - The method of obtaining ternary chemical compounds based on iron oxide and manganese oxide - Google Patents

The method of obtaining ternary chemical compounds based on iron oxide and manganese oxide Download PDF

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WO2011070450A1
WO2011070450A1 PCT/IB2010/053297 IB2010053297W WO2011070450A1 WO 2011070450 A1 WO2011070450 A1 WO 2011070450A1 IB 2010053297 W IB2010053297 W IB 2010053297W WO 2011070450 A1 WO2011070450 A1 WO 2011070450A1
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temperature
chemical compounds
inert material
oxide
compounds based
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PCT/IB2010/053297
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French (fr)
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Ewelina Ksepko
Jan Figa
Marek ŚCIĄŻKO
Grzegorz ŁABOJKO
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Instytut Chemicznej Przeróbki Węgla
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Priority claimed from PL389853A external-priority patent/PL218481B1/en
Priority claimed from PL391770A external-priority patent/PL222499B1/en
Application filed by Instytut Chemicznej Przeróbki Węgla filed Critical Instytut Chemicznej Przeróbki Węgla
Priority to EP10751714.6A priority Critical patent/EP2509921B1/en
Publication of WO2011070450A1 publication Critical patent/WO2011070450A1/en

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    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00—Compounds of iron
    • C01G49/02—Oxides; Hydroxides
    • C01G49/06—Ferric oxide [Fe2O3]
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/16—Clays or other mineral silicates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/18—Carbon
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/002—Mixed oxides other than spinels, e.g. perovskite
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/889—Manganese, technetium or rhenium
    • B01J23/8892—Manganese
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61—Surface area
    • B01J35/618—Surface area more than 1000 m2/g
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • B01J37/0027—Powdering
    • B01J37/0036—Grinding
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G45/00—Compounds of manganese
    • C01G45/02—Oxides; Hydroxides
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2002/00—Crystal-structural characteristics
    • C01P2002/50—Solid solutions
    • C01P2002/52—Solid solutions containing elements as dopants
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2002/00—Crystal-structural characteristics
    • C01P2002/70—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
    • C01P2002/72—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2002/00—Crystal-structural characteristics
    • C01P2002/80—Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70
    • C01P2002/88—Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70 by thermal analysis data, e.g. TGA, DTA, DSC
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00—Particle morphology
    • C01P2004/60—Particles characterised by their size
    • C01P2004/61—Micrometer sized, i.e. from 1-100 micrometer
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00—Physical properties of inorganic compounds
    • C01P2006/12—Surface area
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00—Physical properties of inorganic compounds
    • C01P2006/80—Compositional purity
    • C01P2006/82—Compositional purity water content

Definitions

  • the subject of the invention consist of the method of obtaining ternary chemical compounds based on iron oxide and manganese oxide used in the processes of chemical oxygen transport in an oxide loop during fuels combustion or gasification described in Polish patent application No P-389853 and in an additional application No P-391770 supplemented by additional parameters of the method and additional substrates.
  • thermochemical coal conversion processes with simultaneous drastic reduction of their adverse environmental impact (including CO 2 and NO x emissions) makes that intensive research on the improvement of the existing and development of new processes directed inter alia at the oxygen combustion and gasification of fuels is carried out worldwide.
  • the use of a chemical looping is one of promising development directions for combustion and gasification processes, which allows achieving high conversion efficiencies and is economically attractive. In those processes a direct contact of the fuel with oxygen from the air is prevented.
  • the oxygen transport is carried out by means of a circulating solid oxygen carrier obtained based on metal oxides.
  • oxygen carriers including various compositions of copper, manganese, iron or nickel oxides used as active materials and aluminium oxide, titanium dioxide, zirconium dioxide used as an inert material. Inert materials are added at the amount from a few to a few dozen wt.% in relation to the active material, due to which the oxide carriers life is extended, inter alia via the reduction of their abrasion.
  • the chemical looping was initially used for the process of gaseous fuels combustion; later on it was expanded onto solid fuels combustion (including biomass and coal).
  • the invention is aimed at the method of obtaining ternary chemical compounds based on iron oxide and manganese oxide, useful for the process of oxygen transport in a chemical looping, of more favourable reactivity parameters and primarily of better oxygen transport capacity.
  • the input components are subject to at least two-stage calcination in an oxidising atmosphere
  • the inert material consists of sepiolite and/or ZrO2 and/or ⁇ 2 and/or AI2O3 and/or S1O2.
  • X assumes values of 20, 30, 40, 60 wt.% and Y assumes values of 60, 50, 40, 20 wt.%.
  • inorganic heat-resistant minerals or their mixture is the inert material.
  • bentonite or sepiolite or any mixture of them is the inert material.
  • the input components consist of chemical compounds containing iron and/or manganese, from which iron and manganese oxides are obtained as a result of calcination in an oxidising atmosphere.
  • the basic merit of the invention is the fact that from metal oxides due to the mechanical mixing and calcination the oxide materials are obtained, which are oxygen carriers featuring better capacity of oxygen transport, more favourable parameters of reactivity with fuel (in the combustion/gasification reaction) and with oxygen from the air (at the stage of carrier regeneration).
  • the oxygen transport capacity was obtained at the amount of 4 - 20 wt.%, the material's attrition value from 0.6 to 5.4%, and the melting temperature in a reducing atmosphere above 1 100°C. This was achieved because of using two active components and one inert component, which are the basic components of the oxygen carrier.
  • the use of such system enabled primarily the obtaining of more perfect oxide materials by increasing their reactivity with fuel (in the combustion/gasification reaction) and increasing their life due to reducing their attrition and weakening their tendency to agglomerate.
  • thermochemical reactions in lower temperature ranges.
  • complex oxygen carriers feature a better reactivity.
  • the method of manufacturing acc. to the invention is simple in the practical application and gives repeatable results, enables obtaining oxygen carriers for chemical oxygen looping purposes with a possibility of free mixing of active and inert components of the input products, which is not ensured by other methods, e.g. impregnation, which in this respect are very limited by the amount of active component fed, frequently up to the amount of ca. 20 wt.%.
  • Fe 2 O 3 (purity > 99%), MnO 2 (purity > 90%), sepiolite, AI 2 O 3 (purity > 99.7%), ZrO2 (purity > 99%), SiO2 (purity > 99%), synthetic graphite.
  • the method of obtaining ternary chemical compounds consists in mixing 60 g of Fe2O3, 20 g of MnO2, 20 g of sepiolite and 10 g of graphite. The components were rubbed with distilled water till obtaining the grain size below 100 ⁇ . After drying the blend was calcined. The calcination was carried out during 24 hours at the temperature of 1050°C. Then obtained the blend was milled again and calcined at the temperature of 1050°C during 24 hours. As a result, a sample was obtained of composition 60 wt.% of Fe 2 O3, 20 wt.% of MnO 2 , 20 wt.% of sepiolite.
  • the oxygen carriers obtained in this way feature:
  • the fusion temperatures in a reducing atmosphere amounted to: sintering point 1 1 10°C, softening point 1350°C, melting temperature 1420°C, flow temperature 1500°C, low tendency to agglomerate, because 90% of the material produced was a fraction ⁇ 202 ⁇ ,
  • the method of obtaining ternary chemical compounds consists in mixing 60 g of Fe 2 O3, 20 g of MnO 2 , 20 g of ZrO 2 and 10 g of graphite. After the components mixing the blend was twice calcined during 24 hours, where the calcinations temperature amounted to 1050°C. As a result, a sample was obtained of chemical composition 60 wt.% of Fe 2 O 3 , 20 wt.% of MnO 2 , 20 wt.% of ZrO 2 .
  • X-ray powder patterns for a "fresh" oxygen carrier i.e. not subject to any processes and converted with fuel (methane) and then regenerated with oxygen from the air, prove a very good regeneration capacity of samples of oxygen carriers based on iron and manganese oxide.
  • the manufacture method specified guarantee that the conversion of substrates used ranges from 80 to 100%.
  • Fig. 1 gives results of cyclical thermogravimetric examinations for a sample of 60 wt.% of Fe 2 O3, 20 wt.% MnO 2 , 20 wt.% of sepiolite, carried out for the temperature of 800°C.
  • Table 1 presents the oxygen transport capacity versus the composition of selected binary and ternary oxygen carriers based on iron and manganese oxide.
  • abrasion granules 4 mm in diameter each, were prepared from the obtained preparations. They were pressed using a hydraulic press with a pressure of 1300 kg/cm 2 . The granules were then sintered at the temperature of 1050°C. Previously prepared granules were subject to attrition testing acc. to a modified procedure based on the standard EN 12915-2:2009.
  • Graphs presented below in Fig. 1 , Fig. 2, Fig. 3, Fig. 4, Fig. 5 show appropriate results of examinations, of which: Fig. 1 - Results of cyclical thermogravimetric examinations 60 wt.% of Fe 2 0 3 , 20 wt.% of Mn0 2 , 20% wt.% of sepiolite, using syngas as the fuel,
  • Fig. 4 Results of cyclical thermogravimetric examinations 60 wt.% of Fe 2 O3, 20 wt.% of Mn0 2 , 20 wt.% of ZrO 2 , using "clean" syngas as the fuel— and contaminated with hydrogen sulphide— ,
  • the method of obtaining ternary chemical compounds consists in mixing 20 g of Fe 2 0 3l 60 g of Mn0 2 , 20 g of ZrO 2 , and 8 g of graphite. The components were rubbed with distilled water till obtaining the grain size below 100 ⁇ . After drying the blend was calcined. The calcination was carried out during 20 hours at the temperature of 850°C. Then the blend obtained was milled again with 8 g of graphite and calcined again at the temperature of 850°C during 20 hours. As a result, a sample was obtained of composition 20 wt.% of Fe 2 0 3 , 60 wt.% of MnO 2 , 20 wt.% of Zr0 2 .
  • the oxygen carriers obtained in this way feature:
  • the method of obtaining ternary chemical compounds consists in mixing 40 g of Fe 2 0 3 , 40 g of Mn0 2 , 20 g of AI 2 O 3 , and 9 g of graphite.
  • the components were rubbed with distilled water till obtaining the grain size below 100 pm.
  • After drying the blend was calcined. The calcination was carried out during 8 hours at the temperature of 800°C.
  • the blend obtained was milled again with 9 g of graphite and calcined at the temperature of 820°C during 8 hours.
  • the blend obtained was milled again with 9 g of graphite and calcined at the temperature of 820°C during 8 hours.
  • a sample was obtained of composition 40 wt.% of Fe 2 0 3 , 40 wt.% of Mn0 2 , 20 wt.% of Al 2 0 3 .
  • the oxygen carriers obtained in this way feature:
  • the method of obtaining ternary chemical compounds consists in mixing 20 g of Fe 2 O 3 , 60 g of MnO 2 , 20 g of ZrO 2 , and 8 g of graphite. The components were rubbed with distilled water till obtaining the grain size below 100 ⁇ . After drying the blend was calcined. The calcination was carried out during 20 hours at the temperature of 850°C. Then the blend obtained was milled again with 8 g of graphite and calcined again at the temperature of 850°C during 20 hours. As a result, a sample was obtained of composition 20 wt.% of Fe 2 O 3 , 60 wt.% of MnO 2 , 20 wt.% of ZrO 2 .
  • the oxygen carriers obtained in this way feature:
  • the method of obtaining ternary chemical compounds consists in mixing 40 g of Fe2O3, 40 g of MnO2, 20 g of AI2O3, and 9 g of graphite.
  • the components were rubbed with distilled water till obtaining the grain size below 100 ⁇ .
  • After drying the blend was calcined. The calcination was carried out during 8 hours at the temperature of 800°C.
  • the blend obtained was milled again with 9 g of graphite and calcined at the temperature of 820°C during 8 hours.
  • the blend obtained was milled again with 9 g of graphite and calcined at the temperature of 820°C during 8 hours.
  • a sample was obtained of composition 40 wt.% of Fe 2 O 3 , 40 wt.% of MnO 2 , 20 wt.% of AI 2 O 3 .
  • the oxygen carriers obtained in this way feature:

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Abstract

The method of obtaining ternary chemical compounds based on iron oxide and manganese oxide The subject of the invention consist of the method of obtaining ternary chemical compounds based on iron oxide and manganese oxide used in the processes of chemical oxygen transport in chemical looping during fuels combustion or gasification. The method of obtaining ternary chemical compounds based on iron oxide and manganese oxide, consisting in mixing the initial components, calcinating the mix at a high temperature, according to the invention is characterised in that powdered graphite at the amount of 1 to 2 wt.% in relation to the initial mix is added to the initial components in the form of Fe2O3 and MnO2 and an inert material, used in proportions resulting from a general chemical formula ∑(X Fe2O3 + Y MnO2 + Z inert material ) = 100 wt.%, where X and Y are within the ranges 1≤x≤99, 1≤y≤99 and the inert material is used at the amount supplementing to 100 wt.%, and the whole is subject to at least one-stage calcination in an oxidising atmosphere at a temperature of 600 –1500°C during 3 to 24 hours.

Description

The method of obtaining ternary chemical compounds based on iron oxide and manganese oxide
The subject of the invention consist of the method of obtaining ternary chemical compounds based on iron oxide and manganese oxide used in the processes of chemical oxygen transport in an oxide loop during fuels combustion or gasification described in Polish patent application No P-389853 and in an additional application No P-391770 supplemented by additional parameters of the method and additional substrates.
The necessity to improve the efficiency of thermochemical coal conversion processes with simultaneous drastic reduction of their adverse environmental impact (including CO2 and NOx emissions) makes that intensive research on the improvement of the existing and development of new processes directed inter alia at the oxygen combustion and gasification of fuels is carried out worldwide. The use of a chemical looping is one of promising development directions for combustion and gasification processes, which allows achieving high conversion efficiencies and is economically attractive. In those processes a direct contact of the fuel with oxygen from the air is prevented. The oxygen transport is carried out by means of a circulating solid oxygen carrier obtained based on metal oxides.
In chemical looping oxide methods of fuel combustion or gasification, nitrogen does not exists, both in the flue gas and in the gases generated as a result of conversion. In conventional methods of energy generation from fossil fuels it dilutes the flue gas or process gas produced, thereby increasing their volume. Many possible oxygen carriers are known, including various compositions of copper, manganese, iron or nickel oxides used as active materials and aluminium oxide, titanium dioxide, zirconium dioxide used as an inert material. Inert materials are added at the amount from a few to a few dozen wt.% in relation to the active material, due to which the oxide carriers life is extended, inter alia via the reduction of their abrasion.
The chemical looping was initially used for the process of gaseous fuels combustion; later on it was expanded onto solid fuels combustion (including biomass and coal).
The paper "Characterisation of oxygen carriers for chemical looping combustion" published during the Seventh International Conference in Vancouver, Canada in 2004 shows that the use of oxygen carriers consisting of one active and one inert component is known. While the known methods of oxygen carriers obtaining for a chemical looping is based on one-stage calcination process and not exceeding the period of 6 hours.
The invention is aimed at the method of obtaining ternary chemical compounds based on iron oxide and manganese oxide, useful for the process of oxygen transport in a chemical looping, of more favourable reactivity parameters and primarily of better oxygen transport capacity.
The method of obtaining ternary chemical compounds based on iron oxide and manganese oxide, consisting in mixing the initial components, calcinating the mix at a high temperature, acc. to the invention is characterised by the fact that powdered graphite at the amount of 1 to 25 wt.% in relation to the initial mix is added to the initial components in the form of Fe2O3 and MnO2 and an inert material, used in proportions resulting from a general chemical formula ∑ ( Fe203 + ΥΜΠ02 + Zinert material) = 00 wt.%, where X and Y are within the ranges 1 <x<99, 1 <y<99 and the inert material is used at the amount supplementing to 1 00 wt.%, and the whole is subject to at least one-stage calcination in an oxidising atmosphere at a temperature of 600 - 1 500°C during 3 to 24 hours. What is favourable, the input components are subject to at least two-stage calcination in an oxidising atmosphere at the temperature of 1050°C during 24 hours.
What is favourable, the inert material consists of sepiolite and/or ZrO2 and/or ΤΊΟ2 and/or AI2O3 and/or S1O2.
What is favourable, X assumes values of 20, 30, 40, 60 wt.% and Y assumes values of 60, 50, 40, 20 wt.%.
What is favourable, 10 wt.% of powdered graphite are added to the mix.
What is favourable, inorganic heat-resistant minerals or their mixture is the inert material.
What is favourable, bentonite or sepiolite or any mixture of them is the inert material.
What is favourable, 1 to 25 wt.% of powdered graphite or other carbon carriers are added to the mixture of oxides and inert materials.
What is favourable, up to 10 wt.% of powdered graphite or other carbon carriers are added to the mixture of oxides and inert materials.
What is favourable, once the process of high-temperature calcination is completed the process of controlled cooling at a temperature decrease rate from 1000°C/minute to 1 °C/minute is carried out.
What is favourable, the input components consist of chemical compounds containing iron and/or manganese, from which iron and manganese oxides are obtained as a result of calcination in an oxidising atmosphere.
The basic merit of the invention is the fact that from metal oxides due to the mechanical mixing and calcination the oxide materials are obtained, which are oxygen carriers featuring better capacity of oxygen transport, more favourable parameters of reactivity with fuel (in the combustion/gasification reaction) and with oxygen from the air (at the stage of carrier regeneration).
Using the method acc. to the invention, the oxygen transport capacity was obtained at the amount of 4 - 20 wt.%, the material's attrition value from 0.6 to 5.4%, and the melting temperature in a reducing atmosphere above 1 100°C. This was achieved because of using two active components and one inert component, which are the basic components of the oxygen carrier. The use of such system enabled primarily the obtaining of more perfect oxide materials by increasing their reactivity with fuel (in the combustion/gasification reaction) and increasing their life due to reducing their attrition and weakening their tendency to agglomerate.
Moreover, they enable carrying out thermochemical reactions in lower temperature ranges. In general, complex oxygen carriers feature a better reactivity.
The method of manufacturing acc. to the invention is simple in the practical application and gives repeatable results, enables obtaining oxygen carriers for chemical oxygen looping purposes with a possibility of free mixing of active and inert components of the input products, which is not ensured by other methods, e.g. impregnation, which in this respect are very limited by the amount of active component fed, frequently up to the amount of ca. 20 wt.%.
Appropriate calcination (with adequately chosen calcination time and temperature) enables increasing the oxide product life due to reducing its abrasion and favourable weakening their tendency to agglomerate and increasing the homogeneity of the obtained product. Thereby this has a favourable impact on the costs of fuels combustion or gasification processes, which are reduced due to their increased reactivity and life.
In addition, the possibility to use inorganic heat-resistant minerals and chemical compounds containing iron and/or manganese results in the improvement to the economic efficiency.
The graphite addition to the blend caused that during calcination at the temperature of 1050°C in the air atmosphere it is subject to oxidation to carbon dioxide, which release results in an increase in: specific surface area, the conversion and the reaction rate.
In addition, the possibility to use inorganic heat-resistant minerals and chemical compounds containing iron and/or manganese results in the improvement to the economic efficiency. The selection of components' proportions is related to the obtaining of valuable, for a chemical oxide loop, oxides properties considering the reduction of their production costs.
The method acc. to the invention has been described in non-restrictive examples of implementation.
The following components have been used as raw materials to obtain oxygen carriers:
Fe2O3 (purity > 99%), MnO2 (purity > 90%), sepiolite, AI2O3 (purity > 99.7%), ZrO2 (purity > 99%), SiO2 (purity > 99%), synthetic graphite.
Example 1
The method of obtaining ternary chemical compounds consists in mixing 60 g of Fe2O3, 20 g of MnO2, 20 g of sepiolite and 10 g of graphite. The components were rubbed with distilled water till obtaining the grain size below 100 μιτι. After drying the blend was calcined. The calcination was carried out during 24 hours at the temperature of 1050°C. Then obtained the blend was milled again and calcined at the temperature of 1050°C during 24 hours. As a result, a sample was obtained of composition 60 wt.% of Fe2O3, 20 wt.% of MnO2, 20 wt.% of sepiolite.
The oxygen carriers obtained in this way feature:
high oxygen transport capacity of 18.75% (at the temperature of 800°C), specific surface area BET equal to 1 .307 m2/g,
low attrition 1 .2%,
good regeneration capacity (Fig. 1 , Fig. 5),
repeatability of results,
the fact that the optimum range of preparation work falls within the temperature range of 600 - 900°C,
high thermal resistance; the fusion temperatures in a reducing atmosphere amounted to: sintering point 1 1 10°C, softening point 1350°C, melting temperature 1420°C, flow temperature 1500°C, low tendency to agglomerate, because 90% of the material produced was a fraction < 202 μιτι,
a short oxidation and reduction time, where 90% of the fraction gets oxidised within 10.5 minutes, reduced within 24.4 minutes for "clean syngas" and was oxidised within 7.64 minutes and reduced within 14.79 minutes using syngas contaminated with hydrogen sulphide, actual density of 4.4 g/cm3,
100% ability for regeneration despite the syngas contamination with hydrogen sulphide,
100% ability of regeneration, after the reaction of methane combustion no problems with deactivation with carbon were observed.
Example 2
The method of obtaining ternary chemical compounds consists in mixing 60 g of Fe2O3, 20 g of MnO2, 20 g of ZrO2 and 10 g of graphite. After the components mixing the blend was twice calcined during 24 hours, where the calcinations temperature amounted to 1050°C. As a result, a sample was obtained of chemical composition 60 wt.% of Fe2O3, 20 wt.% of MnO2, 20 wt.% of ZrO2. The oxygen carriers obtained feature:
high oxygen transport capacity of 18.99% (at the temperature of 800°C), specific surface area BET equal to 0.771 m2/g,
a short oxidation and reduction time, where 90% of the fraction gets oxidised within 9.9 minutes, reduced within 16.6 minutes for "clean syngas" and within was oxidised 7.64 minutes and reduced within 12.3 minutes using syngas contaminated with hydrogen sulphide, good regeneration capacity (Fig. 2),
100% capacity for regeneration despite the syngas contamination with hydrogen sulphide,
100% capacity of regeneration, after the reaction of methane combustion no problems with deactivation with carbon were observed, high thermal resistance; where the fusion temperatures in a reducing atmosphere amounted to: sintering point 1 100°C, softening point 1520°C, melting temperature 1530°C, flow temperature 1540°C,
low attrition 1 .4 %,
the scope of the compound use is optimal in the temperature range of 600 - 900°C,
low tendency to agglomerate, where 90% of the blend was a fraction < 98.2 μηη ,
actual density of 5.2 g/cm3,
repeatability of results.
X-ray powder patterns for a "fresh" oxygen carrier, i.e. not subject to any processes and converted with fuel (methane) and then regenerated with oxygen from the air, prove a very good regeneration capacity of samples of oxygen carriers based on iron and manganese oxide.
These advantages have been confirmed by product analyses, including investigations of: X-ray diffraction on powder samples (XRD), thermogravimetry coupled with a quadrupole mass spectrometer (TG-QMS), fusion temperatures, abrasion, grain size distribution, actual density, specific area using the BET method.
The manufacture method specified guarantee that the conversion of substrates used ranges from 80 to 100%.
The oxygen transport capacity is defined as the difference between the oxidised and reduced mass of the solid oxygen carrier Δ = mox - mre (wt.%). In practice this means the amount of oxygen transferred from the oxygen carrier to the fuel.
To determine the oxygen transport capacity of the obtained solid oxygen carriers based on transition metals, cyclical examinations were carried out in oxidising (synthetic air) and reducing (syngas consisting of 36% CO, 27% H2, 12% CO2, 25% He, and 38% CO, 30.8% H2, 13% CO2, 17.8% He, 4042 ppm H2S and 3% CH /Ar) conditions by means of the coupled TG-QMS technique using a TA Model 2050 thermobalance and a Netzsch STA 409 PC Luxx thermobalance coupled with an Aeolos QMS 403C quadrupole mass spectrometer, where the mass spectrometry has been used to control substrates and to identify the waste gases.
The process of chemical looping was simulated this way using a thermogravimetric analysis.
For example, Fig. 1 gives results of cyclical thermogravimetric examinations for a sample of 60 wt.% of Fe2O3, 20 wt.% MnO2, 20 wt.% of sepiolite, carried out for the temperature of 800°C.
Table 1 presents the oxygen transport capacity versus the composition of selected binary and ternary oxygen carriers based on iron and manganese oxide.
Table 1. Oxygen transport capacity versus the chemical composition
Oxygen carrier Oxygen transport Oxygen transport capacity * (wt.%) capacity ** (wt.%)
60% Fe2O3, 20% MnO2, 20% 18.75 17.92 sepiolite
60% Fe2O3, 20% MnO2, 20% ZrO2 18.99 18.99
60% Fe2O3, 40% ZrO2 x 17.66
60% MnO2, 40% ZrO2 x 4,36
* at 800°C for the fuel in the form of syngas
** at 800°C for the fuel in the form of syngas contaminated with H2S
To determine the abrasion granules, 4 mm in diameter each, were prepared from the obtained preparations. They were pressed using a hydraulic press with a pressure of 1300 kg/cm2. The granules were then sintered at the temperature of 1050°C. Previously prepared granules were subject to attrition testing acc. to a modified procedure based on the standard EN 12915-2:2009.
Graphs presented below in Fig. 1 , Fig. 2, Fig. 3, Fig. 4, Fig. 5 show appropriate results of examinations, of which: Fig. 1 - Results of cyclical thermogravimetric examinations 60 wt.% of Fe203, 20 wt.% of Mn02, 20% wt.% of sepiolite, using syngas as the fuel,
Fig. 2 - Results of cyclical thermogravimetric examinations 60 wt.% of Fe2O3, 20 wt.% of Mn02, 20 wt.% of ZrO2, using syngas as the fuel,
Fig. 3 - Degree of oxidation (regeneration) versus time,
Fig. 4 - Results of cyclical thermogravimetric examinations 60 wt.% of Fe2O3, 20 wt.% of Mn02, 20 wt.% of ZrO2, using "clean" syngas as the fuel— and contaminated with hydrogen sulphide— ,
Fig. 5 - X-ray powder patterns for the oxygen carrier containing 60 wt.% of Fe203, 20 wt.% of Mn02, 20% wt.% of sepiolite, not subjected to any processes and after its regeneration.
Example 3
The method of obtaining ternary chemical compounds consists in mixing 20 g of Fe203l 60 g of Mn02, 20 g of ZrO2, and 8 g of graphite. The components were rubbed with distilled water till obtaining the grain size below 100 μιη. After drying the blend was calcined. The calcination was carried out during 20 hours at the temperature of 850°C. Then the blend obtained was milled again with 8 g of graphite and calcined again at the temperature of 850°C during 20 hours. As a result, a sample was obtained of composition 20 wt.% of Fe203, 60 wt.% of MnO2, 20 wt.% of Zr02.
The oxygen carriers obtained in this way feature:
high oxygen transport capacity of 6.5% (at the temperature of 800°C), specific area BET equal to 1.355 m2/g,
low abrasion 1.0 %,
good capacity of regeneration,
repeatability of results, the fact that the optimum range of preparation work falls within the temperature range of 600 - 1500°C,
high thermal resistance; the melting temperature in a reducing atmosphere amounted to: 1520°C,
low tendency to agglomerate, because 90% of the material produced was a fraction < 65 pm,
a short oxidation and reduction time, where 90% of the fraction gets oxidised within 6.05 minutes, reduced within 10.8 minutes for "clean syngas" and was oxidised within 1.56 minutes and reduced within 6.85 minutes using syngas contaminated with hydrogen sulphide,
97% capacity for regeneration despite the syngas contamination with hydrogen sulphide,
100% capacity of regeneration, after the reaction of methane combustion no problems with deactivation with carbon black were observed.
Example 4
The method of obtaining ternary chemical compounds consists in mixing 40 g of Fe203, 40 g of Mn02, 20 g of AI2O3, and 9 g of graphite. The components were rubbed with distilled water till obtaining the grain size below 100 pm. After drying the blend was calcined. The calcination was carried out during 8 hours at the temperature of 800°C. Next the blend obtained was milled again with 9 g of graphite and calcined at the temperature of 820°C during 8 hours. Then the blend obtained was milled again with 9 g of graphite and calcined at the temperature of 820°C during 8 hours. As a result, a sample was obtained of composition 40 wt.% of Fe203, 40 wt.% of Mn02, 20 wt.% of Al203.
The oxygen carriers obtained in this way feature:
high oxygen transport capacity of 13.2% (at the temperature of 800°C), specific area BET equal to 1.355 m2/g,
low attrition 0.7 %,
good capacity of regeneration,
repeatability of results, the fact that the optimum range of preparation work falls within the temperature range of 600 - 1500°C,
high thermal resistance; the melting temperature in a reducing atmosphere amounted to: 1640°C,
low tendency to agglomerate, because 90% of the material produced was a fraction < 103 pm,
a short oxidation and reduction time, where 90% of the fraction gets oxidised within 12.7 minutes, reduced within 13.3 minutes for "clean syngas" and was oxidised within 3.2 minutes and reduced within 8.14 minutes using syngas contaminated with hydrogen sulphide,
98% capacity for regeneration despite the syngas contamination with hydrogen sulphide,
100% capacity of regeneration, after the reaction of methane combustion no problems with deactivation with carbon were observed.
Figure imgf000012_0001
Example 3
The method of obtaining ternary chemical compounds consists in mixing 20 g of Fe2O3, 60 g of MnO2, 20 g of ZrO2, and 8 g of graphite. The components were rubbed with distilled water till obtaining the grain size below 100 μιτι. After drying the blend was calcined. The calcination was carried out during 20 hours at the temperature of 850°C. Then the blend obtained was milled again with 8 g of graphite and calcined again at the temperature of 850°C during 20 hours. As a result, a sample was obtained of composition 20 wt.% of Fe2O3, 60 wt.% of MnO2, 20 wt.% of ZrO2.
The oxygen carriers obtained in this way feature:
high oxygen transport capacity of 6.5% (at the temperature of 800°C), specific area BET equal to 1 .355 m2/g,
low abrasion 1 .0 %,
good capacity of regeneration,
repeatability of results,
the fact that the optimum range of preparation work falls within the temperature range of 600 - 1500°C,
high thermal resistance; the melting temperature in a reducing atmosphere amounted to: 1520°C,
low tendency to agglomerate, because 90% of the material produced was a fraction < 65 μιτι,
a short oxidation and reduction time, where 90% of the fraction gets oxidised within 6.05 minutes, reduced within 10.8 minutes for "clean syngas" and was oxidised within 1 .56 minutes and reduced within 6.85 minutes using syngas contaminated with hydrogen sulphide,
97% capacity for regeneration despite the syngas contamination with hydrogen sulphide,
100% capacity of regeneration, after the reaction of methane combustion no problems with deactivation with carbon black were observed. Example 4
The method of obtaining ternary chemical compounds consists in mixing 40 g of Fe2O3, 40 g of MnO2, 20 g of AI2O3, and 9 g of graphite. The components were rubbed with distilled water till obtaining the grain size below 100 μιτι. After drying the blend was calcined. The calcination was carried out during 8 hours at the temperature of 800°C. Next the blend obtained was milled again with 9 g of graphite and calcined at the temperature of 820°C during 8 hours. Then the blend obtained was milled again with 9 g of graphite and calcined at the temperature of 820°C during 8 hours. As a result, a sample was obtained of composition 40 wt.% of Fe2O3, 40 wt.% of MnO2, 20 wt.% of AI2O3.
The oxygen carriers obtained in this way feature:
high oxygen transport capacity of 13.2% (at the temperature of 800°C), specific area BET equal to 1 .355 m2/g,
low attrition 0.7 %,
good capacity of regeneration,
repeatability of results,
the fact that the optimum range of preparation work falls within the temperature range of 600 - 1500°C,
high thermal resistance; the melting temperature in a reducing atmosphere amounted to: 1640°C,
low tendency to agglomerate, because 90% of the material produced was a fraction < 103 m,
a short oxidation and reduction time, where 90% of the fraction gets oxidised within 12.7 minutes, reduced within 13.3 minutes for "clean syngas" and was oxidised within 3.2 minutes and reduced within 8.14 minutes using syngas contaminated with hydrogen sulphide,
98% capacity for regeneration despite the syngas contamination with hydrogen sulphide,
100% capacity of regeneration, after the reaction of methane combustion no problems with deactivation with carbon were observed.

Claims

The method of obtaining ternary chemical compounds based on iron oxide and manganese oxide Claims
1 . The method of obtaining ternary chemical compounds based on iron oxide and manganese oxide, consisting in mixing the initial components, calcinating the blend at a high temperature, is characterised in that powdered graphite at the amount of 1 to 25 wt.% in relation to the initial blend is added to the initial components in the form of Fe2O3 and MnO2 and an inert material, used in proportions resulting from a general chemical formula∑ ( Fe203 + ΜΠ02 + Zinert material) = 00 wt.%, where X and Y are within the ranges 1 <x<99, 1 <y<99 and the inert material is used at the amount supplementing to 1 00 wt.%, and the whole is subject to at least one-stage calcination in an oxidising atmosphere at a temperature of 600 - 1 500°C during 3 to 24 hours.
2. The method according to claim 1 is characterised in that the input components are subject to at least two-stage calcination in an oxidising atmosphere at the temperature of 1 050°C during 24 hours.
3. The method according to claim 1 and 2 is characterised in that the inert material consists of sepiolite and/or ZrO2 and/or T1O2 and/or AI2O3 and/or S1O2.
4. The method according to claim 1 and 2 is characterised in that X assumes values of 20, 30, 40, 60 wt.% and Y assumes values of 60, 50, 40, 20 wt.%.
5. The method according to claim 1 is characterised in that 1 0 wt.% of powdered graphite are added to the mix.
6. The method according to claim 1 is characterised in that inorganic heat- resistant minerals or their mixture is the inert material .
7. The method according to claim 6 is characterised in that bentonite or sepiolite or any mixture of them is the inert material.
8. The method according to claim 1 and 6 is characterised in that 1 to 25 wt.% of powdered graphite or other carbon carriers are added to the mixture of oxides and inert materials.
9. The method according to claim 1 and 7 is characterised in that up to 10 wt.% of powdered graphite or other carbon carriers are added to the mixture of oxides and inert materials.
10. The method according to claim 1 and 2 is characterised in that once the process of high-temperature calcination is completed the process of controlled cooling at a temperature decrease rate from 1000°C/minute to 1 °C/minute is carried out.
1 1 . The method according to claim 1 is characterised in that the input components consist of chemical compounds containing iron and/or manganese, from which iron and manganese oxides are obtained as a result of calcination in an oxidising atmosphere.
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