[go: up one dir, main page]

WO2007093176A2 - Morceaux de coke modifies pour fours de fusion de minerais - Google Patents

Morceaux de coke modifies pour fours de fusion de minerais Download PDF

Info

Publication number
WO2007093176A2
WO2007093176A2 PCT/DK2007/000069 DK2007000069W WO2007093176A2 WO 2007093176 A2 WO2007093176 A2 WO 2007093176A2 DK 2007000069 W DK2007000069 W DK 2007000069W WO 2007093176 A2 WO2007093176 A2 WO 2007093176A2
Authority
WO
WIPO (PCT)
Prior art keywords
carbon
coke
coke lump
lump
volatile
Prior art date
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.)
Ceased
Application number
PCT/DK2007/000069
Other languages
English (en)
Other versions
WO2007093176A3 (fr
Inventor
Leif Møller JENSEN
Svend Grove-Rasmussen
Peter Farkas Binderup Hansen
Mads GUDIK-SØRENSEN
Marianne Guldberg
Eva Ravn Nielsen
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Rockwool AS
Original Assignee
Rockwool International AS
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 Rockwool International AS filed Critical Rockwool International AS
Publication of WO2007093176A2 publication Critical patent/WO2007093176A2/fr
Publication of WO2007093176A3 publication Critical patent/WO2007093176A3/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/26—After-treatment of the shaped fuels, e.g. briquettes
    • C10L5/32—Coating
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/34—Other details of the shaped fuels, e.g. briquettes
    • C10L5/36—Shape
    • C10L5/366—Powders
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L9/00—Treating solid fuels to improve their combustion
    • C10L9/10—Treating solid fuels to improve their combustion by using additives

Definitions

  • the present invention relates to modified, and thereby improved, coke lumps useful as fuel in mineral melting furnaces, in particular for the production of stone wool.
  • the present invention also relates to the preparation of such modified coke lumps.
  • the production of stone wool and, e.g., metal smelting are important industrial processes.
  • the mineral melting in the production process for stone wool is typically conducted in a so-called cupola furnace in which the raw materials, e.g. coke and mineral materials such as rocks (e.g. of basalt, diabase, gabbro), briquettes (e.g. containing olivine, basalt, diabase, gabbro, slag, limestone, waste stone wool, etc.), are charged to the upper part of the furnace.
  • Air is blasted through a number of nozzles near the bottom of the cupola. Most of the coke combusts at a very high temperature in the lower region just above the nozzles.
  • the hot flue gas from the combustion containing carbon dioxide and water vapour flows up through the cupola and leaves the top at a significantly reduced temperature.
  • the upward flowing flue gas transfers its energy to the down flowing raw materials that melt and to the coke.
  • the raw materials melt in the region above the nozzles.
  • the melt runs to the bottom of the cupola furnace and is collected in a melt bath located below the nozzles.
  • the molten mineral material is found in the lower region of the furnace, and coke is predominantly found in a region just above the lower region.
  • a problem realised in conventional cupola furnaces is that a considerable amount of the fuel, i.e. in particular coke, is partly pyrolysed or gasified with carbon dioxide or water vapour in the furnace.
  • a significant fraction of the thermal energy is lost from the cupola furnace and a significant amount of potentially problematic CO (carbon monoxide) and H 2 (hydrogen) is formed.
  • One way of reducing the gasification of coke is by use of a less reactive coke (normally related to a larger density of the carbon and a lower porosity of the lump) or by use of larger lumps of coke.
  • a third alternative is by covering the coke surface with a solid surface layer as e.g. GB 1,409,971 disclosing a method of preparing a molten mineral mass in a coke-fired shaft furnace, wherein coke lumps are coated with a solid surface layer.
  • the present invention relates to coke lumps carrying an ablative coating.
  • the present invention provides a coke lump carrying an ablative coating of a composition comprising (i) one or more carbon material(s) and/or non-volatile carbon- forming material(s) and (ii) one or more non-volatile silicon material(s), preferably having a weight average particle size of at the most 500 ⁇ m.
  • Another main aspect of the present invention relates to coke lumps wherein a substantial portion of the pores comprises a non-volatile substance.
  • the present invention also provides a coke lump wherein a substantial portion of the pores comprises one or more (i) salt(s) and/or (ii) precursor compound(s), which leave a non-volatile substance when heated to a temperature in the range of 1200-2000 0 C in inert or reducing atmosphere.
  • Figure 1 illustrates a coke lump (1) coated with a surface coating (2), in particular an ablative coating.
  • FIG. 2 illustrates a coke lump (1) with an open pores system (3).
  • a pore (4) is filled with a solution of a salt and/or precursor compound (i.e. prior to heating to a temperature in the range of 1200-2000 0 C), whereas another pore (5) has a reduced diameter due to deposition of a non-volatile substance (e.g. a salt) resulting from heating of the salt or precursor compound to a temperature in the range of 1200-2000 0 C.
  • a non-volatile substance e.g. a salt
  • the present invention relates to modified coke lumps.
  • Coke represents solid carbonaceous fuels with a predominant part of the available energy present in the form of a solid, non-volatile, but reactive above 800 0 C.
  • Coke is typically a hard, dry carbon substance produced by heating coal to a high temperature in the absence of air.
  • the term "lump" reflects a block or a particle of material which will be held back by a grid or mesh having a spacing of 50 mm. Preferably, the block or particle will also be held back by a grid or mesh having a spacing of 90 mm. It should be understood that the before-mentioned definition relates to the modified coke lump.
  • the present invention provides a coke lump carrying an ablative coating of a composition
  • a composition comprising (i) one or more carbon material(s) and/or non-volatile carbon- forming material(s) and (ii) one or more non-volatile silicon material(s), preferably having a weight average particle size of at the most 500 ⁇ m.
  • the term "ablative coating" in connection with coke lumps is intended to mean a coating which, when the coke lump is subjected to a temperature exceeding 1200 0 C, is capable of removing the heat energy from the coke to reduce the reactivity of the coke towards e.g. CO 2 .
  • Ablation is a process in which heat energy is consumed by a material through melting, vaporization or thermal decomposition and then dissipated as the material vaporizes or erodes. These ablative materials may be chemically constructed or made from natural materials.
  • the ablative coating is present on the entire surface of the coke lump, however, in a cost efficient industrial process, it may not be possible to ensure that the entire surface of all (or just substantially all) of the coke lumps are fully covered.
  • the term "carrying an ablative coating" in connection with a coke lump refers to a situation where at least 80% of the surface of the coke lump is covered by the ablative coating. More particular, at least 90%, or even more preferable, the entire surface, of the surface of the coke lump is covered by the ablative coating.
  • the term "carrying an ablative coating” refers to a situation where at least 80% of the surface of 90% of the coke lumps in a population of coke lumps is covered by the ablative coating.
  • the present invention also relates to such a population of coke lumps.
  • the ablative coating of the coke lumps plays an important role and consists of a composition comprising of (i) one or more carbon material(s) and/or non-volatile carbon-forming material(s) and (ii) one or more non-volatile silicon material(s).
  • non-volatile is intended to mean the fraction of a material which does not (significantly) evaporate, decompose or in any other way disappear from the surface where deposited, as the material is heated to a temperature of 1200 0 C in an inert or reducing atmosphere at standard pressure (101.3 kPa; 1 atm.).
  • the ablative coating may comprise minor amounts of volatile materials, e.g. up to 15% by weight, due to the presence of water, solvents, volatiles in the commercial products corresponding to the carbon/carbon-forming and silicon materials.
  • the carbon/carbon-forming material(s) and the silicon material(s) will form the ablative coating when these materials are in intimate contact when heated.
  • the relative weight ratio between the carbon/carbon-forming material(s) and the silicon material(s) is not particularly critical when the coke lump is used as fuel in a mineral melting furnace, because excess of the carbon material(s) will be consumed as fuel in the furnace, and because excess of the silicon material(s) will form part of the mineral melt.
  • the composition comprises 10-90% by weight of the carbon or carbon-forming material(s) and 90-10% by weight of the silicon material(s), more particularly 20-80% by weight of the carbon or carbon-forming material(s) and 80-20% by weight of the silicon material(s).
  • One, two or more carbon/carbon-forming materials may be combined with one, two or more silicon materials.
  • the carbon or carbon-forming materials can be selected from a plethora of materials, but the carbon materials are typically selected from tar, granulated coke, coke powder and carbon powder, whereas the carbon-forming materials are typically selected from sugars, carbohydrate syrups, molasses, polyurethanes, and phenol urea formaldehyde.
  • the one or more carbon or carbon-forming material(s) are selected from the group consisting of tar, carbohydrate syrups, molasses, and phenol urea formaldehyde.
  • the silicon materials can also be selected from a wide range of materials, but are typically selected from the group consisting of silica, silica fumes, silicones, siloxanes (including polysiloxanes), and silicate rich oxides and minerals, in particular from silica and silica fumes.
  • the silicon materials should preferably have a weight average particle size of at the most 500 ⁇ m in order to ensure a suitable contact between the carbon/carbon-forming material and the silicon material.
  • the weight average particle size is at the most 250 ⁇ m, especially at the most 100 ⁇ m. It is also preferred that at least 5% by weight of the particles of the silicon material(s) have a particle size exceeding 2 mm.
  • the "weight average particle size" can be determined by available particle size measurements (e.g. laser diffraction) and corresponding trivial recalculation to identify the diameter at which an equal weight is present as larger and smaller particles. It is of course understood that particles so atypically large that removal of a few particles will significantly alter the weight average particle size are not included in this measurement.
  • composition may also comprise other constituents, e.g. up to 50% by weight of other materials, e.g. mineral materials, and binders, etc.
  • mineral materials e.g. mineral materials, and binders, etc.
  • such mineral materials preferably constitute 3-50% by weight, in particular 5-25% by weight.
  • Suitable examples of such mineral materials are those selected from the group consisting of bauxite, aludross, olivine, mullite, magnesia, lime, kaolin, dolomite, plastic clay, flyash and bentonite, although other similar, useful mineral materials may also be contemplated.
  • the thickness of the coating should be sufficient to suitably protect the inner coke lump.
  • average thickness of the ablative coating is typically in the range of 0.1-10 mm, such as in the range of 0.5-2.5 mm.
  • the average thickness can be determined by examining a number of cross sections by an element sensitive method of higher spatial resolution; e.g. EDX in a SEM.
  • compositions will be particularly useful as ablative coatings for coke lumps: (1) Tar with silica fumes or fine silica sand, and (2) molasses with silica fumes or fine silica sand.
  • the present invention also provides a process for the preparation of a coke lump carrying an ablative coating of a composition comprising (i) one or more carbon material(s) and/or nonvolatile carbon-forming material(s) and (i) one or more non-volatile silicon material(s) as defined above, said process comprising the steps of:
  • the coke lump is provided in such a way that it can be suitably sprayed.
  • the coke lump may be placed on a conveyer belt, or the like.
  • the coke may be held in a rotating drum-shaped grid to allow spraying of all surfaces.
  • a third option is placing the coke temporarily in a mesh cage suitable for dipping in said coating.
  • the coke lump is sprayed with or soaked in a coating composition comprising the one or more carbon or carbon-forming material(s) and the one or more silicon material(s).
  • the coating composition may either be the composition as such, but more preferably the coating composition comprises the carbon/carbon-forming material(s) and the silicon material(s) of the final composition in combination with volatiles (e.g. diluents, wetting agents), mineral materials, binders, etc.
  • the coating composition further comprises a binder.
  • binders are those selected from the group consisting of plastic clay, flyash, bentonite, (Na,AI)PO 4 , phosphate compounds, methyl cellulose, and other cellulose derivates.
  • the coating composition may further comprise 3-50% by weight (calculated on the basis of the non-volatiles) of mineral material(s).
  • the coke lump may be dried or cured, or charged directly into the top of a mineral melting furnace, e.g. a cupola.
  • the present invention also provides a coke lump wherein a substantial portion of the pores comprises one or more (i) salt(s) and/or (ii) precursor compound(s), which leave a nonvolatile substance when heated to a temperature in the range of 1200-2000 0 C in inert or reducing atmosphere.
  • the motivation for impregnation of pores relates to the well-known reaction rate of coke lump gasification.
  • the kinetics of coke gasification are limiting, i.e. the entire internal surface of the porous lump contributes to the reaction rate.
  • diffusional transport in pores of CO and CO 2 from and to the internal surface becomes limiting, and an increasing central volume of the coke lump is thus relatively inert to gasification; only the outer "shell" contributes significantly to the reaction rate.
  • only the outmost surface of the lump is reacting, as diffusion in pores prevents significant reaction inside the coke lump.
  • the term "substantial portion” is intended to mean at least 50% of the pores within a distance of 5 mm from the surface of the coke lump, in particular at least 70% of such pores, such as at least 80%, or at least 90%, of such pores.
  • the one or more salt(s) and/or precursor compound(s) are, when leaving a non-volatile substance (e.g. a salt, in particular the salt in non-decomposed form), believed to efficiently reduce the gas transport by diffusion, so that a lower gasification rate of the coke lump may be achieved (see, e.g., Figure 2).
  • a non-volatile substance e.g. a salt, in particular the salt in non-decomposed form
  • This effect is obtained either upon thermal conversion of the one or more precursor compound(s) at a temperature in the range of 1200-2000 0 C, whereby a suitable material, e.g. carbon, is deposited in the pores of the coke lump, or by simple deposition of a salt (with or without thermal decomposition/conversion) within the pores of the coke lump upon evaporation of the solvent for the salt.
  • inert or reducing atmosphere should be understood as not oxidizing relative to the deposited carbon at the temperatures being considered.
  • non-volatile is intended to mean the fraction of a material which does not significantly evaporate, decompose or in any other way disappear from the surface where deposited, as the material is heated to a temperature of 1200°C in an inert or reducing atmosphere at standard pressure (101.3 kPa; 1 atm.)
  • useful precursor compounds are those selected from the groups consisting of tar, polyurethanes, phenol urea formaldehyde, sugars, carbohydrate syrups, and molasses.
  • useful salts are those selected from the group consisting of Ca(MnO 4 ) 2 , Ca(NO 3 ) 2 , nitrates or chlorides of Al, Fe, Mg and Ca, and sodium silicate (water glass). Such salts will typically (which is also preferred) not undergo thermal decomposition/conversion upon heating to 1200 0 C.
  • the one or more salt(s) and/or precursor compound(s) are preferably selected from the groups consisting of tar, polyurethanes, and phenol urea formaldehyde, sugars, carbohydrate syrups, molasses, Ca(MnO 4 ) 2 , Ca(NO 3 ) 2 , nitrates or chlorides of Al, Fe, Mg and Ca, and sodium silicate (water glass).
  • precursor compounds such as sugars and carbohydrate syrups with high carbon content as well as salts such as Ca(MnO 4 ) 2 , Ca(NO 3 ) 2 and water glass are expected to be advantageous.
  • the portion of the pores of particular concern is pores within a distance of 5 mm from the surface of the coke lump. More particular, pores within a distance of 10 mm, especially pores within a distance of 20 mm, from the surface of the coke lump are considered and filled with the salt(s) and/or precursor compound(s).
  • the present invention also provides a process for the preparation of a coke lump wherein a substantial portion of the pores comprises one or more (i) salt(s) and/or (ii) precursor compound(s) as defined above, said process comprising the steps of:
  • step (ii) optionally establishing a lower pressure around the coke lump to facilitate impregnation by re-establishing the ambient pressure after step (iii)
  • Water is a suitable and useful solvent or dispersing agent for the solution or dispersion used in step (iii).
  • the solution or dispersion preferably comprises a wetting agent, e.g. a surfactant lowering the surface tension of water and/or enhancing penetration of water into the coke porosity.
  • a wetting agent e.g. a surfactant lowering the surface tension of water and/or enhancing penetration of water into the coke porosity.
  • the salts and/or precursor compounds may be applied to the coke lump in the form of a solution or a dispersion, preferably a colloidal dispersion.
  • the salts are, however, preferably applied in the form of a solution in order to facilitate a suitable penetration into the pores of the coke lump.
  • the coke lump may be dried or cured, or charged directly into the top of a mineral melting furnace, e.g. a cupola.
  • the present application also provides a coke lump on which at least 80%, more particular at least 90%, or even more preferable the entire surface, of the surface is coated with a composition comprising one or more substances which remain essentially on the surface of the coke lump at temperatures above 120O 0 C, more particular above 1300 0 C, and especially above 1500°C.
  • the composition include (i) a high melting particle material and optionally (ii) a lower melting material, the higher melting material being selected from the group of silica, bauxite, aludross, calcined bauxite, olivine, mullite, magnesia, lime, dolomite, kaolin, aluminium phosphate, sodium-aluminium phosphate, anorthosite, iron oxide and iron, and the optional lower melting material being selected from the group of bentonite, flyash, clay, cements, Portland cement, phosphates, crushed glass, crushed glass cullets or recycle glass, crushed stone wool fibres or glass wool fibres and sodium silicates (water glass).
  • any subselection of the aforementioned materials may be applied.
  • the present invention also provides a process for the preparation of a coke lump as defined above, said process comprising the steps of:
  • the suspension preferably comprises a wetting agent, in particular a surfactant lowering the surface tension of water.
  • the suspension may preferably further comprise a viscosity modifying agent, e.g. selected from the group consisting of plastic clay, flyash, bentonite, methyl cellulose and other cellulose derivates.
  • a viscosity modifying agent e.g. selected from the group consisting of plastic clay, flyash, bentonite, methyl cellulose and other cellulose derivates.
  • the high melting particle material may in particular be selected among the substances silica, silica fumes, aludross, bauxite and olivine, the optional lower melting may in particular be selected among the substances Portland cement, clay and crushed stone wool fibres.
  • the viscosity modifying additive may in particular be a cellulose derivate.
  • intumescent paints Another type of surface coating is so-called intumescent paints. After spraying or soaking, the coke lump may be dried or cured, or charged directly into the top of a mineral melting furnace, e.g. a cupola.
  • the surface of coke may be provided with an ablative coating.
  • An ablative coating may be prepared, e.g., as a combination of silica and carbon.
  • Silicate may be applied in the form of sand, silica fumes or other fine particles rich in silica.
  • Carbon may be applied in the form of tar, sugar, molasses or other organic polymers or compounds with a substantial content of non-volatile carbon. Silicone or siloxane may be applied to provide one or both components by decomposition or partial combustion.
  • the ablative coating may be applied in the form of a suspension or solution or liquid, by methods such as e.g. dipping or spraying or passing a lacquer-blanket of the fluid.
  • the pore structure in a coke lump may be partially blocked by application of a salt or a non- volatile substance.
  • the non-volatile substance may be present in the form of an organic or inorganic material which has been left upon heating of a precursor compound to 1200 0 C.
  • the salt or precursor compound may be dissolved, molten or in other way liquefied, or as a gel or dispersion of particles with a predominant diameter which allows for a significant level of penetration into the porous structure of the selected coke.
  • a wetting agent may be applied to ensure sufficient penetration into the porous structure of the coke.
  • the medium for e.g. dissolution is preferentially water but other media may be used, e.g. organic solvents or fuels. Examples of salts and precursor compounds are given in Table 1.
  • Table 1 Examples of salts and precursor compounds which may be applied to reduce activity of coke.
  • the one or more salts and/or precursor compounds may be applied by methods such as e.g. dipping or spraying or passing a lacquer-blanket of the fluid.
  • the applied fluid may or may not form a continuous film on the surface of the coke after impregnation.
  • the salts and/or precursor compounds may dry, decompose, crystallise or otherwise react before or during the passing down through the cupola to leave a non-volatile substance above 1200 0 C.
  • a coke lump may be provided with a surface coating by application of a suspension.
  • the suspension may contain one or more high-melting oxides or minerals, one or more lower melting oxides or minerals or glasses as well as one or more viscosity regulating additives, or any subselection of the aforementioned materials.
  • a binder serving to increase the adhesion of the dry coating on the coke may be used. Examples are given in Table 2.
  • the particle sizes must be selected to match the application process. Materials are preferably suspended in water or a water-based liquid system, but organic based systems may be applied. Another specific example is use of so called intumescent paints.
  • Table 2 Examples of coating materials and combinations of these which may be applied to reduce activity of coke.
  • Coke lumps are coated by methods such as e.g. dipping or spraying or passing a lacquer- blanket of the suspension.
  • the coating dries before or during the passing down through the cupola.

Landscapes

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

Abstract

La présente invention concerne des morceaux de coke modifiés en tant que combustible dans des fours de fusion de minerais (cubilots), pour la production de laine de roche, ainsi que leur préparation. Le morceau de coke peut comporter un enduit ablatif constitué d'un matériau de carbone ou d'un matériau formant un carbone non-volatile et d'un matériau à base de silicium non-volatile; ou une partie substantielle des pores d'un morceau de coke peut comprendre des sels ou un ou plusieurs composés précurseurs, qui libèrent une substance non-volatile lorsqu'ils sont chauffés à une température dans la plage de 1200 à 20000 °C sous une atmosphère inerte ou réductrice; ou le morceau de coke peut comprendre un enduit de silice, de scorie d'aluminium, de bauxite, de bauxite calcinée, d'olivine, de mullite, de magnésie, de chaux, de dolomite, de kaolin, de phosphate d'aluminium, de phosphate d'aluminium de sodium, d'anorthosite, d'oxyde de fer et de fer, de cendre volante, d'argile, de ciments, de ciment de Portland, de phosphates, de verre écrasé, de déchets de verre écrasé ou de verre recyclé, de fibres de laine de roche écrasées ou de fibres de laine de verre et de silicates de sodium.
PCT/DK2007/000069 2006-02-16 2007-02-09 Morceaux de coke modifies pour fours de fusion de minerais Ceased WO2007093176A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP06075346.4 2006-02-16
EP06075346A EP1820839A1 (fr) 2006-02-16 2006-02-16 Coke en blocs modifié pour fours à fusion minérale

Publications (2)

Publication Number Publication Date
WO2007093176A2 true WO2007093176A2 (fr) 2007-08-23
WO2007093176A3 WO2007093176A3 (fr) 2008-03-20

Family

ID=36691361

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/DK2007/000069 Ceased WO2007093176A2 (fr) 2006-02-16 2007-02-09 Morceaux de coke modifies pour fours de fusion de minerais

Country Status (2)

Country Link
EP (1) EP1820839A1 (fr)
WO (1) WO2007093176A2 (fr)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB0802260D0 (en) * 2008-02-07 2008-03-12 Internat Innovative Technologi Fuel enrichment process
CN103013617A (zh) * 2013-01-08 2013-04-03 华北电力大学 一种工业废渣锅炉抗结焦剂及其使用方法
CN112537963B (zh) * 2019-09-20 2022-09-09 本钢板材股份有限公司 一种用于铁水罐罐沿渣清理的喷涂方法
CN110684580B (zh) * 2019-11-14 2021-02-26 安徽省宗正农业科技开发有限公司 一种复合高能生物质燃料棒的制备方法
CN114317061B (zh) * 2021-11-16 2023-01-24 华阳新材料科技集团有限公司 一种精煤制取超低灰分煤的化学提纯方法

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3711318A (en) * 1971-01-28 1973-01-16 Fmc Corp Method of controlling ultrafines from reactive form coke
SE348710B (fr) * 1972-01-11 1972-09-11 Rockwool Ab
US5578239A (en) * 1992-04-29 1996-11-26 Benetech, Inc. Methods for treating coke and coal and products produced thereby

Also Published As

Publication number Publication date
WO2007093176A3 (fr) 2008-03-20
EP1820839A1 (fr) 2007-08-22

Similar Documents

Publication Publication Date Title
CN103930385B (zh) 可浇注耐火组合物
CN1029735C (zh) 形成多孔耐火材料体的方法及其在此方法中使用的组合物
CN1076382C (zh) 用于高温耐火材料的表面处理剂以及用其进行处理的方法
WO2007093176A2 (fr) Morceaux de coke modifies pour fours de fusion de minerais
JPS62270469A (ja) 耐火物塊体を形成する方法およびかかる塊体を形成するための粒子の混合物
JPH0825004A (ja) 可動モールド式連続鋳造機のモールド用コーティング剤
US4298391A (en) Hot repair gun refractory mix for a lining refractory
CN119177559B (zh) 一种低粉尘的保温覆盖剂及其制备方法
JP6955519B2 (ja) 低生体内持続性繊維を含有する耐火被覆材及びその製造方法
ES2373765T3 (es) Mezcla seca para el tratamiento de sustratos refractarios y procedimiento que la emplea.
JP3238385B2 (ja) ライニング材
JP4125980B2 (ja) コークス炉用珪石れんがとその製造方法
JP2989790B2 (ja) コークス炉
KR101041528B1 (ko) 코크오븐 탄화실 내화물 표면 코팅제
KR102062107B1 (ko) 내열성 기지에 발생되는 크랙의 치유 및 방염이 가능한 도포제 및 상기 도포제를 이용한 도포방법
CN100544857C (zh) 处理金属熔体的方法
FR2537024A1 (fr) Plaques thermo-isolantes refractaires et procede pour la coulee continue d'acier
WO2004080915A1 (fr) Matieres coulables en ciment refractaire
CN100427242C (zh) 干式中间罐涂布材料及其施工方法
CN110642604A (zh) 铸造用钢包防渣涂抹料及其制备方法
RU2239758C1 (ru) Способ горячего ремонта огнеупорной футеровки тепловых агрегатов методом керамической наплавки и керамическая наплавленная масса
CN121017487A (zh) 一种Mn13高耐磨钢专用保护渣
CN107312554A (zh) 一种焦炉装煤孔用自动浇浆料
JPS6030721B2 (ja) 溶銑予備処理用容器の内張材処理方法
RU1784660C (ru) Способ получени защитного покрыти на металлической поверхности, контактирующей с расплавленным цветным металлом

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application
NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 07702487

Country of ref document: EP

Kind code of ref document: A2