WO2012175770A2 - Composition and method for producing mn tablets - Google Patents

Composition and method for producing mn tablets Download PDF

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Publication number
WO2012175770A2
WO2012175770A2 PCT/ES2012/070433 ES2012070433W WO2012175770A2 WO 2012175770 A2 WO2012175770 A2 WO 2012175770A2 ES 2012070433 W ES2012070433 W ES 2012070433W WO 2012175770 A2 WO2012175770 A2 WO 2012175770A2
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Prior art keywords
composition
organic polymer
tablets
composition according
water
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PCT/ES2012/070433
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Spanish (es)
French (fr)
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WO2012175770A3 (en
Inventor
Ricardo FERNÁNDEZ SERRANO
Gaspar GONZÁLEZ DONCEL
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Consejo Superior De Investigaciones Científicas (Csic)
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Publication of WO2012175770A2 publication Critical patent/WO2012175770A2/en
Publication of WO2012175770A3 publication Critical patent/WO2012175770A3/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/0006Adding metallic additives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/10Metallic powder containing lubricating or binding agents; Metallic powder containing organic material
    • B22F1/103Metallic powder containing lubricating or binding agents; Metallic powder containing organic material containing an organic binding agent comprising a mixture of, or obtained by reaction of, two or more components other than a solvent or a lubricating agent
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/24Binding; Briquetting ; Granulating
    • C22B1/242Binding; Briquetting ; Granulating with binders
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B47/00Obtaining manganese
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C1/00Making non-ferrous alloys
    • C22C1/04Making non-ferrous alloys by powder metallurgy
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C22/00Alloys based on manganese
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/02Compacting only
    • B22F2003/023Lubricant mixed with the metal powder
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/0056Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00 using cored wires
    • C21C2007/0062Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00 using cored wires with introduction of alloying or treating agents under a compacted form different from a wire, e.g. briquette, pellet

Definitions

  • the present invention relates to a mixture of additives in the preparation of compacted tablets of metals to add as alloys to a casting of another metal, mainly aluminum. More specifically, it refers to the use of a mixture of organic polymers that, mixed in the appropriate proportions, allows to obtain Mn powder tablets with good consistency, in terms of mechanical strength, and of easy dissolution in metal casting.
  • mother alloys with low alloying element contents typically less than 60%
  • these mother alloys commonly come from previous smelters, adding difficulty in controlling their composition.
  • This type of mother alloy has raised interest very recently (US2010313712) while alloys (in the form of splashes) with up to 93% Mn content, up to 5% in total Si and Fe, have been obtained, and The rest aluminum. Its high alloy content minimizes the melting furnace temperature drop and alloy recovery rates close to 100% are announced in periods of approximately 15 minutes.
  • the main disadvantage of these mother alloys remains their high cost.
  • the second is the significant risk of flammability as a result of the fine powders that are released from this type of tablets in a high temperature environment such as that of a foundry; f) Obtain dissolution rates fast enough to minimize casting times while achieving good homogeneity of the alloy in the casting.
  • the dissolution rates of conventional tablets (up to 85% Mn) are industrially acceptable.
  • the presence of small amounts of organic waxes used as lubricants accelerates the dissolution process of the tablets when aluminum is used as a binder (US6149710).
  • these waxes do not have the same binding power as aluminum and, in addition, should not be added in percentages greater than 5% since they increase the slag of the laundry, cause excess fumes, and introduce hydrogen and carbon into the alloy resulting;
  • the Mn being the main element
  • a concentration typically> 70% the use of a mixture of organic polymers with double function, binder and lubricant, for its manufacture is presented.
  • This mixture of polymers allows to obtain compact with a good mechanical resistance while reducing the loss of fine powders during handling.
  • the dissolution of manganese during casting is favored compared to compacts that use aluminum as a binder element and the cost is reduced, since the use of this element is minimized, even being avoided.
  • a composition for the manufacture of Mn tablets characterized in that it comprises: (a) Mn powder in a percentage between 70% and 99.5% by weight, and more preferably between 70% and 97% of the composition; (b) a first powder binder selected from at least one water insoluble organic polymer or at least one water soluble organic polymer, or a mixture of both, wherein said organic polymer is not a wax; and (c) a possible second powder binder preferably selected from aluminum, iron, or their respective alloys.
  • powder is understood as the product that remains of a solid after being reduced to very small parts, generally with a particle size between 1 and 1000 um.
  • a typical range of sizes is that indicated in Tables II and III of the detailed description of the invention.
  • the method of obtaining Mn tablets from the composition described above is object of the invention.
  • Said procedure is characterized in that it comprises compacting the different elements that they form the composition at room temperature (10 ° C-45 ° C).
  • the process may comprise a stage after compacting the heat treatment of the composition.
  • the object of the invention is the Mn tablets obtained from said process and their use in metal casting, preferably, in aluminum, iron, or their respective alloys.
  • Figure 1 shows an Mn tablet obtained from 146 g of Mn and 3.75 g of PEG 5000;
  • Figure 2 shows the evolution in time of the Mn content of the experimental casting broth according to Mn tablets with different composition, compacting the powders of the mixture at different loading levels and with subsequent heat treatment;
  • Figure 3 shows the mechanical resistance normalized by the height (mm) of the tested Mn tablets and in which the load axis was applied in the transverse direction.
  • the commercial tablet represented by squares, contains 80% Mn and 20% Al, and is 200 grams in weight. The rest of the tablets have been manufactured according to the present invention and contain 95% Mn.
  • the data represented by rhombuses correspond to a tablet with 5% PEG, weighing 80 grams, compacted at low load (25Tn) and without subsequent heat treatment.
  • the data represented by circles correspond to a tablet with 2.5% PEG and 2.5% PVA, 150 grams in weight and with a subsequent heat treatment of 100 ° C for 20 min.
  • the data represented by triangles correspond to a 5% PEG tablet, 80 grams of compacted weight at 45 tons and with a subsequent heat treatment of 65 ° C and 20 min.
  • the results obtained from the tablets of the present invention are superior to those obtained from the commercial tablet. This improvement is very significant, taking into account the percentage of Mn of the tablets (95%), higher than 80% of Mn of the commercial tablets.
  • the invention relates to the use of a mixture of organic polymers for the manufacture of tablets with a high manganese content (> 70%) by compaction at a temperature close to the environment (between 10 ° C and 45 ° C) of the mixture of organic polymers with manganese and optionally, with a metal selected from aluminum, iron, or its alloys. It is ruled out to replace one of the two polymers of the invention with a wax among which are: paraffin, microcrystalline wax, polyethylene or polypropylene waxes (which are similar to paraffin but with greater strength and flexibility), oxidized polyethylene waxes or carnauba This is because they give rise to softer tablets compared to polymer / polymer blends.
  • waxes containing phenolic or aromatic components are graphitized when the temperature is raised in a vacuum or in an inert gas atmosphere, contributing carbon to the laundry.
  • the organic polymer blend consists of a water insoluble polymer (Type A) and a water soluble polymer (Type B).
  • the Type A polymer may preferably consist of a polymer selected from a group consisting of polymers of vinyl alcohols, polyurethanes, polyamides, polyacrylates and polymethacrylates, as well as any combination thereof. More preferably, said polymer may consist of polyvinyl acetate (PVA), which has a good combination of properties and a low price compared to aluminum; polyvinylbutyral, for its clean combustion that minimizes carbon residues; or poly (oxymethylene).
  • PVA polyvinyl acetate
  • the Type A polymer may consist of Kollidon®, which comprises 8 parts (w / w) of PVA and 2 parts (w / w) of polyvinylpyrrolidone.
  • the weight percentage of said Type A polymer in the composition is between 0.05% and 5.0%.
  • the Type B polymer may preferably consist of a polymer selected from a group consisting of polyethylene glycol (PEG), polyethylene oxide, polyethylene, celluloses, copolymers of ethylene, polypropylene and propylene oxide, as well as any combination thereof.
  • PEG polyethylene glycol
  • polyethylene glycol is proposed for its good combination of properties and its low price compared to aluminum, as well as polyethylene for its low price.
  • Polyethylene oxide although it has good compatibility with Type A and Type B polymers and has good thermal decomposition properties, is much more expensive than polyethylene glycol.
  • the weight percentage of Type B polymer in the composition is preferably between 0.05% and 5.0%.
  • the molecular weight of the constituent polymers of the mixture is high.
  • the molecular weight of the polymers used in the composition is preferably greater than 1000 g / mol, and more preferably, greater than 3000 g / mol.
  • the Type B polymer is PEG
  • the hydroxyl value decreases inversely proportional to the molecular weight .
  • the price of polyethylene glycol depends on the molecular weight.
  • PEG 5000-7000 has the best combination of hydroxyl value and price, so it is especially preferred in the present invention.
  • polyethylene glycol has a high oxidation index, so it decomposes into components of lower molecular weight without leaving residues around 200 ° C.
  • polyethylene glycol (PEG) of molecular weight greater than 4000 g / mol is especially preferred.
  • the described composition is constituted by the elements shown in Table I, where the preferred percentage by weight of each of said elements is also collected, so that the total sum of all of them in The composition is 100%.
  • said polymers may be present independently or in combination:
  • the main advantage of the invention is that the use of aluminum (or iron) as a binder can be completely eliminated and that the total amount of binders added to obtain the tablets can be reduced. For both reasons the cost of manufacturing tablets is reduced. In addition, the mechanical strength of the tablets improves several orders of magnitude and in parallel the dissolution times of the tablets in the broth are improved.
  • Example 1 Mix of 5% by weight of PEG in powder form, 10% by weight of aluminum in powder form and 85% by weight of electrolytic Mn from milling;
  • Example 2 Mix of 5% by weight of PEG with 95% of electrolytic Mn from milling;
  • Example 3 Mixture of 2.5% by weight of PVA + PEG with 97.5% by weight of electrolytic Mn from milling; Example 4. Measurement of the mechanical strength of the tablets obtained in examples 1 to 3.
  • Example 1. Mix of 5% by weight of PEG in powder form and 10% by weight of aluminum in powder form and 85% by weight of electrolytic Mn from milling. The powders described in Table IV were mixed in a turbot for 15 minutes at a rate of approximately 1 revolution per second to optimize the powder mixing process.
  • the granulometry of the Mn used in the procedure was that corresponding to Table II (b).
  • the granulometry of PEG powders was the one shown in Table III (b).
  • the aluminum used in the mixture was atomized aluminum powder with particle size between 100 ⁇ and 800 ⁇ .
  • the resulting mixture is poured minimizing the segregation of both components in the compaction tooling, with its inner surface lubricated with zinc stearate.
  • the powder mixture according to Tables II and III was compacted in a cold press at a temperature between 10 ° C and 45 ° C.
  • the tablet obtained was extracted by applying about 700 kg of pressure.
  • the resulting tablet had a diameter of 40 mm and a height of approximately 22 mm with a final weight of 75 grams.
  • the apparent density resulting from the process of Compaction was 2.7g / cm 3 .
  • Figure 2 shows the concentration of Mn measured by optical emission spectroscopy by spark, at different sample extraction times.
  • the recovery rate of Mn is 98%, obtaining this value in a time 2.4 times less than using only Al as the binding element.
  • Example 2 Mix of 5% by weight of PEG with 95% of electrolytic Mn from milling.
  • the powders described in Table V were mixed in a turbot for 15 minutes at a rate of approximately 1 revolution per second to optimize the powder mixing process.
  • Table V shows the intervals by weight of the different elements present in the composition: Table V. Intervals in percentage by weight of the elements comprising the composition
  • Figure 2 shows the concentration of Mn measured by optical emission spectroscopy by spark at different sample extraction times.
  • the recovery rate of Mn is 98%, obtaining this value in a time 2.4 times less than using only Al as the binding element.
  • Example 3 Mix of 2.5% by weight of PVA and PEG with 97.5% by weight of electrolytic Mn from milling.
  • the powders described in Table V were mixed in a turbot for 15 minutes at a rate of approximately 1 revolution per second to optimize the powder mixing process.
  • Figure 2 shows the concentration of Mn measured by optical emission spectroscopy by spark at different sample extraction times.
  • the recovery rate of Mn is 98%, obtaining this value in a time 2.4 times less than using only Al as the binding element.
  • Example 4. Measurement of the mechanical strength of the tablets obtained in examples 1 to 3.
  • the mechanical strength of the obtained tablets was studied by means of the so-called drop test in which the tablets were dropped in free fall from 740 mm high against a hard and rigid ground and the amount of throws needed is quantified so that the tablet loses a certain amount of material and breaks in an obvious way.
  • the results of this test are shown in Table VII.
  • Table VII shows the number of falls that each tablet has withstood in the drop test from 740 mm, together with the compaction conditions and subsequent heat treatment performed on each tablet. All tablets were compacted at 25 ° C and approximately 94 Tn. The result of number of falls in If it is less than 2, it is the average of performing the test on at least three tablets.

Abstract

The invention relates to a composition for manufacturing Mn tablets, characterized in that it includes: (a) between 70% and 99.5% by weight of Mn powder; (b) a first powder binder chosen from at least one organic polymer that is insoluble in water and at least one organic polymer that is soluble in water, or a mixture of the two, wherein said first binder is not a wax. The invention likewise relates to a method for producing said composition and to the use thereof as Mn tablets in the casting of metals.

Description

Composición y procedimiento de obtención de tabletas de Mn Sector de la Técnica  Composition and procedure for obtaining tablets from Mn Technical Sector
La presente invención se refiere a una mezcla de aditivos en la preparación de tabletas compactadas de metales para añadir como aleantes a una colada de otro metal, principalmente aluminio. Más concretamente se refiere al uso de una mezcla de polímeros orgánicos que mezclados en las proporciones adecuadas permite obtener tabletas de polvo de Mn con buena consistencia, en términos de resistencia mecánica, y de fácil disolución en coladas de metales.  The present invention relates to a mixture of additives in the preparation of compacted tablets of metals to add as alloys to a casting of another metal, mainly aluminum. More specifically, it refers to the use of a mixture of organic polymers that, mixed in the appropriate proportions, allows to obtain Mn powder tablets with good consistency, in terms of mechanical strength, and of easy dissolution in metal casting.
Estado de la Técnica State of the Art
En la industria de aleado de aleaciones de metales han existido tradicionalmente dos estrategias para realizar el proceso de aleado. Por un lado se han utilizado aleaciones madre con bajos contenidos de elemento aleante, típicamente menor del 60%. Entre las principales desventajas del uso de este tipo de aleaciones madre están: que añaden una gran cantidad de material frío a la colada, que el stock y el transporte de este producto supone unos costes importantes para la fundición y que el aluminio que se utiliza en dichas aleaciones proviene comúnmente de fundiciones previas, añadiendo dificultad en el control de la composición del mismo. Este tipo de aleaciones madre ha vuelto a suscitar interés muy recientemente (US2010313712 ) en tanto que se han obtenido aleaciones (en forma de salpicaduras) con hasta el 93% de contenido de Mn, hasta un 5% en total de Si y Fe, y el resto aluminio. Su alto contenido en aleante minimiza el descenso de temperatura del horno de fundición y se anuncian tasas de recuperación de aleante cercanas al 100% en periodos de aproximadamente 15 minutos. Sin embargo, la principal desventaja de estas aleaciones madre sigue siendo su elevado coste.  In the metal alloy alloy industry, there have traditionally been two strategies to carry out the alloy process. On the one hand, mother alloys with low alloying element contents, typically less than 60%, have been used. Among the main disadvantages of the use of this type of mother alloy are: that they add a large amount of cold material to the laundry, that the stock and transport of this product entails significant costs for the foundry and that the aluminum used in These alloys commonly come from previous smelters, adding difficulty in controlling their composition. This type of mother alloy has raised interest very recently (US2010313712) while alloys (in the form of splashes) with up to 93% Mn content, up to 5% in total Si and Fe, have been obtained, and The rest aluminum. Its high alloy content minimizes the melting furnace temperature drop and alloy recovery rates close to 100% are announced in periods of approximately 15 minutes. However, the main disadvantage of these mother alloys remains their high cost.
Por otro lado, en los años setenta del siglo XX comenzaron a aparecer en el mercado compactos de polvo del metal aleante en concentraciones típicas de alrededor del 70%. Esta estrategia reduce en gran medida los problemas derivados del uso de las aleaciones madre tradicionales. On the other hand, in the seventies of the twentieth century, compact alloys of metal powder began to appear on the market in typical concentrations of around 70%. This strategy greatly reduces the problems derived from the use of traditional mother alloys.
Desde la implantación a escala mundial del método de compactos de polvos como principal método de aleado de aleaciones de aluminio, el mercado ha presionado a los fabricantes para incrementar el contenido del Mn en sus productos. Este aumento supone, además, disminuir la dependencia del aluminio, que es un material caro y sujeto a cambios en su cotización. Since the worldwide implementation of the powder compact method as the main method of alloying aluminum alloys, the market has put pressure on manufacturers to increase the content of Mn in their products. This increase also means reducing dependence on aluminum, which is an expensive material and subject to changes in its price.
Obtener tabletas con alto o muy alto contenido en Mn supone, sin embargo, una serie de retos tecnológicos como pueden ser:  Obtaining tablets with high or very high Mn content, however, involves a series of technological challenges such as:
a) Conseguir mezclas homogéneas del metal aleante (Mn) con aluminio o con otro tipo de aglomerantes que presentan distintas densidades y granulometrias . Es bien conocido que la diferencia de densidades y/o granulometrias de dos tipos de polvos dificulta su mezcla homogénea puesto que los más ligeros y las partículas más pequeñas tienden a ir al fondo del recipiente de mezcla, deshomogeneizando la misma. Este problema es crítico cuando se trabaja con altas concentraciones de uno de los elementos de mezcla (>80%) ; b) Asegurar la fluidez de la mezcla de polvos desde los depósitos hasta las prensas donde se realizan los compactos. En concreto, el manejo de polvos y sus mezclas de manera eficiente a escala industrial exige su buen flujo a través de los distintos dispositivos, tolvas, conductos etc. de las plantas de producción. Es sabido que la presencia de polvos muy finos (<100 mieras de diámetro) incrementa sustancialmente la superficie de contacto entre partículas, lo que dificulta enormemente el flujo del polvo hacia las prensas de compactación;  a) Obtain homogeneous mixtures of the alloying metal (Mn) with aluminum or with other types of binders that have different densities and particle sizes. It is well known that the difference in densities and / or granulometries of two types of powders hinders their homogeneous mixing since the lighter ones and the smaller particles tend to go to the bottom of the mixing vessel, dehomogenizing it. This problem is critical when working with high concentrations of one of the mixing elements (> 80%); b) Ensure the fluidity of the powder mixture from the tanks to the presses where the compacts are made. Specifically, the handling of powders and their mixtures efficiently on an industrial scale requires their good flow through the different devices, hoppers, ducts etc. of the production plants. It is known that the presence of very fine powders (<100 microns in diameter) substantially increases the contact surface between particles, which greatly hinders the flow of the powder towards the compaction presses;
c) Minimizar el tiempo de compactación de la mezcla de polvos para incrementar la productividad. La mayor inversión de las empresas de fabricación de compactos de polvos se centra en el sistema de prensas. Por este motivo se busca minimizar su número. Para que los niveles de productividad de las fábricas sean competitivos, se tiende a reducir los tiempos de compactación de la mezcla de polvos hasta unos pocos segundos. Este factor condiciona la consistencia de los compactos obtenidos cuando se trabaja con bajas concentraciones de elemento aglomerante; c) Minimize the compaction time of the powder mixture to increase productivity. The largest investment of powder compact manufacturing companies is focused on the press system. For this reason, it seeks to minimize its number. For the productivity levels of the factories to be competitive, the compaction times of the powder mixture tend to be reduced to a few seconds. This factor determines the consistency of the compacts obtained when working with low concentrations of binder element;
d) Minimizar la degradación de las prensas y los punzones debidos al efecto abrasivo del Mn y otros metales similares; e) Obtener tabletas con suficiente consistencia, en términos de resistencia mecánica, para facilitar su manipulación y transporte. La consistencia mecánica de las tabletas de polvo disminuye con el contenido de elemento aglomerante, hecho que presenta dos inconvenientes. El primero es que la fragilidad de las tabletas aumenta. Por lo tanto se rompen fácilmente, lo que, además de complicar su manejo, dificulta el control de la cantidad de material aleante que se añade a las coladas. El segundo es el riesgo importante de inflamabilidad como consecuencia de los polvos finos que se desprenden de este tipo de tabletas en un ambiente de altas temperaturas como es el de una fundición; f) Obtener velocidades de disolución suficientemente rápidas para minimizar los tiempos de fundición al tiempo que se logra una buena homogeneidad del aleante en la colada. Las velocidades de disolución de las tabletas convencionales (hasta 85% de Mn) son aceptables industrialmente . Además, la presencia de pequeñas cantidades de ceras orgánicas empleadas como lubricantes acelera el proceso de disolución de las tabletas cuando se usa aluminio como aglomerante (US6149710) . Sin embargo, estas ceras no tienen el mismo poder aglomerante que el aluminio y además, no se deben añadir en porcentajes superiores al 5% puesto que incrementan la escoria de la colada, provocan un exceso de humos, e introducen hidrógeno y carbono en la aleación resultante;  d) Minimize the degradation of presses and punches due to the abrasive effect of Mn and other similar metals; e) Obtain tablets with sufficient consistency, in terms of mechanical strength, to facilitate handling and transport. The mechanical consistency of the powder tablets decreases with the content of the binder element, a fact that presents two drawbacks. The first is that the fragility of the tablets increases. Therefore they break easily, which, in addition to complicating its handling, makes it difficult to control the amount of alloying material that is added to the laundry. The second is the significant risk of flammability as a result of the fine powders that are released from this type of tablets in a high temperature environment such as that of a foundry; f) Obtain dissolution rates fast enough to minimize casting times while achieving good homogeneity of the alloy in the casting. The dissolution rates of conventional tablets (up to 85% Mn) are industrially acceptable. In addition, the presence of small amounts of organic waxes used as lubricants accelerates the dissolution process of the tablets when aluminum is used as a binder (US6149710). However, these waxes do not have the same binding power as aluminum and, in addition, should not be added in percentages greater than 5% since they increase the slag of the laundry, cause excess fumes, and introduce hydrogen and carbon into the alloy resulting;
g) Disminuir la contaminación. Para ello, hay que evitar el uso de materiales aglomerantes que sean nocivos tanto a nivel humano como medioambiental o que deterioren las propiedades de la aleación resultante final. En la actualidad, está extendido el uso de aluminio como material aglomerante y de materiales como: fluoruros, cloruros y carbonatos, que favorecen la disolución de las tabletas. Estos componentes, además de ser perjudiciales para el medio ambiente, han demostrado serlo también por las inclusiones que generan en las aleaciones obtenidas. g) Reduce pollution. For this, the use of binder materials that are harmful to both human and environmental levels or that deteriorate the properties of the final resulting alloy must be avoided. At present, the use of aluminum as a binder material and materials such as fluorides, chlorides and carbonates, which favor the dissolution of tablets, is widespread. These components, in addition to being harmful to the environment At the same time, they have also proven to be so because of the inclusions they generate in the alloys obtained.
Breve descripción de la invención Brief Description of the Invention
Con la finalidad de fabricar compactos de polvos siendo el Mn el principal elemento, en una concentración típicamente >70%, se presenta el uso de una mezcla de polímeros orgánicos con doble función, de aglomerante y lubricante, para su fabricación. Esta mezcla de polímeros permite obtener compactos con una buena resistencia mecánica al tiempo que reduce la pérdida de polvos finos durante su manipulación. Además, se favorece la disolución del manganeso durante la colada en comparación con los compactos que usan aluminio como elemento aglomerante y se reduce el coste, ya que se minimiza el uso de este elemento, llegando incluso a evitarse.  In order to manufacture powder compacts, the Mn being the main element, in a concentration typically> 70%, the use of a mixture of organic polymers with double function, binder and lubricant, for its manufacture is presented. This mixture of polymers allows to obtain compact with a good mechanical resistance while reducing the loss of fine powders during handling. In addition, the dissolution of manganese during casting is favored compared to compacts that use aluminum as a binder element and the cost is reduced, since the use of this element is minimized, even being avoided.
De este modo, es un primer objeto de esta invención una composición para la fabricación de tabletas de Mn caracterizada por que comprende: (a) polvo de Mn en un porcentaje comprendido entre un 70% y un 99.5% en peso, y más preferentemente entre un 70% y un 97% de la composición; (b) un primer aglomerante en polvo seleccionado entre al menos un polímero orgánico insoluble en agua o al menos un polímero orgánico soluble en agua, o una mezcla de ambos, donde dicho polímero orgánico no es una cera; y (c) un posible segundo aglomerante en polvo seleccionado preferentemente entre aluminio, hierro, o sus respectivas aleaciones .  Thus, it is a first object of this invention a composition for the manufacture of Mn tablets characterized in that it comprises: (a) Mn powder in a percentage between 70% and 99.5% by weight, and more preferably between 70% and 97% of the composition; (b) a first powder binder selected from at least one water insoluble organic polymer or at least one water soluble organic polymer, or a mixture of both, wherein said organic polymer is not a wax; and (c) a possible second powder binder preferably selected from aluminum, iron, or their respective alloys.
A efectos de esta patente, se entiende por polvo el producto que queda de un sólido tras ser reducido a partes muy menudas, generalmente con un tamaño de partícula comprendido entre 1 y 1000 um. Un intervalo típico de tamaños es el que se indica en las Tablas II y III de la descripción detallada de la invención.  For the purposes of this patent, powder is understood as the product that remains of a solid after being reduced to very small parts, generally with a particle size between 1 and 1000 um. A typical range of sizes is that indicated in Tables II and III of the detailed description of the invention.
Asimismo, es objeto de la invención el procedimiento de obtención de tabletas de Mn a partir de la composición anteriormente descrita. Dicho procedimiento se caracteriza por que comprende compactar los distintos elementos que forman la composición a temperatura ambiente (10°C-45°C) .Likewise, the method of obtaining Mn tablets from the composition described above is object of the invention. Said procedure is characterized in that it comprises compacting the different elements that they form the composition at room temperature (10 ° C-45 ° C).
Además, si a la tableta formada por la mezcla (o no) de polímeros y el polvo de Mn, se le aplica un tratamiento térmico, posterior a la compactación, a una temperatura por encima de la temperatura de fusión de los polímeros, se consigue una gran unión entre los componentes de la tableta, mejorando de manera notable su resistencia mecánica y en menor medida su disolución en el caldo. Por tanto, en una realización preferida de la invención, el procedimiento puede comprender una etapa posterior a la compactación de tratamiento térmico de la composición. In addition, if a heat treatment, after compaction, is applied to the tablet formed by the mixture (or not) of polymers and Mn powder, at a temperature above the melting temperature of the polymers, it is achieved a great union between the components of the tablet, significantly improving its mechanical strength and to a lesser extent its dissolution in the broth. Therefore, in a preferred embodiment of the invention, the process may comprise a stage after compacting the heat treatment of the composition.
Finalmente, es objeto de la invención las tabletas de Mn obtenidas a partir de dicho procedimiento y su uso en coladas de metales, preferentemente, en coladas de aluminio, hierro, o sus respectivas aleaciones.  Finally, the object of the invention is the Mn tablets obtained from said process and their use in metal casting, preferably, in aluminum, iron, or their respective alloys.
Breve descripción de las figuras Brief description of the figures
La figura 1 muestra una tableta de Mn obtenida a partir de 146 g de Mn y 3.75 g de PEG 5000;  Figure 1 shows an Mn tablet obtained from 146 g of Mn and 3.75 g of PEG 5000;
La figura 2 muestra la evolución en el tiempo del contenido en Mn del caldo de coladas experimentales conforme a tabletas de Mn con distinta composición, realizando la compactación de los polvos de la mezcla a diferentes niveles de carga y con tratamiento térmico posterior;  Figure 2 shows the evolution in time of the Mn content of the experimental casting broth according to Mn tablets with different composition, compacting the powders of the mixture at different loading levels and with subsequent heat treatment;
En la figura 3 se ha representado la resistencia mecánica normalizada por la altura (mm) de las tabletas de Mn ensayadas y en las que se aplicó el eje de carga en la dirección transversal. La tableta comercial, representada por cuadrados, contiene 80% de Mn y 20% de Al, y tiene 200 gramos de peso. El resto de tabletas han sido fabricadas conforme a la presente invención y contienen un 95% de Mn. Los datos representados por rombos corresponden a una tableta con 5% PEG, de 80 gramos de peso, compactada a baja carga (25Tn) y sin tratamiento térmico posterior. Los datos representados por círculos corresponden a una tableta con 2.5% PEG y 2.5% PVA, de 150 gramos de peso y con un tratamiento térmico posterior de 100°C durante 20 min. Los datos representados por triángulos corresponden a una tableta con 5% PEG, de 80 gramos de peso compactada a 45 Tn y con un tratamiento térmico posterior de 65°C y 20 min. Como se observa en la figura, los resultados obtenidos a partir de las tabletas de la presente invención son superiores a los obtenidos a partir de la tableta comercial. Esta mejora es muy significativa, teniendo en cuenta el porcentaje de Mn de la tabletas (95%), superior al 80% de Mn de las tabletas comerciales . Figure 3 shows the mechanical resistance normalized by the height (mm) of the tested Mn tablets and in which the load axis was applied in the transverse direction. The commercial tablet, represented by squares, contains 80% Mn and 20% Al, and is 200 grams in weight. The rest of the tablets have been manufactured according to the present invention and contain 95% Mn. The data represented by rhombuses correspond to a tablet with 5% PEG, weighing 80 grams, compacted at low load (25Tn) and without subsequent heat treatment. The data represented by circles correspond to a tablet with 2.5% PEG and 2.5% PVA, 150 grams in weight and with a subsequent heat treatment of 100 ° C for 20 min. The data represented by triangles correspond to a 5% PEG tablet, 80 grams of compacted weight at 45 tons and with a subsequent heat treatment of 65 ° C and 20 min. As seen in the figure, the results obtained from the tablets of the present invention are superior to those obtained from the commercial tablet. This improvement is very significant, taking into account the percentage of Mn of the tablets (95%), higher than 80% of Mn of the commercial tablets.
Descripción detallada de la invención  Detailed description of the invention
La invención se refiere al uso de una mezcla de polímeros orgánicos para la fabricación de tabletas con un alto contenido de manganeso (>70%) mediante la compactación a una temperatura próxima a la ambiente (entre 10°C y 45°C) de la mezcla de polímeros orgánicos con el manganeso y opcionalmente, con un metal seleccionado entre aluminio, hierro, o sus aleaciones. Se descarta sustituir uno de los dos polímeros de la invención por una cera entre las que se encuentran: parafina, cera microcristalina, ceras de polietileno o polipropileno (que son similares a la parafina pero con mayor resistencia y flexibilidad) , ceras de polietileno oxidadas o carnauba. Esto es debido a que dan lugar a tabletas más blandas en comparación con las mezclas polímero/polímero. Además, las ceras que contienen componentes fenólicos o aromáticos se grafitizan cuando se eleva la temperatura en vacío o en atmósfera de gas inerte, aportando carbono a la colada.  The invention relates to the use of a mixture of organic polymers for the manufacture of tablets with a high manganese content (> 70%) by compaction at a temperature close to the environment (between 10 ° C and 45 ° C) of the mixture of organic polymers with manganese and optionally, with a metal selected from aluminum, iron, or its alloys. It is ruled out to replace one of the two polymers of the invention with a wax among which are: paraffin, microcrystalline wax, polyethylene or polypropylene waxes (which are similar to paraffin but with greater strength and flexibility), oxidized polyethylene waxes or carnauba This is because they give rise to softer tablets compared to polymer / polymer blends. In addition, waxes containing phenolic or aromatic components are graphitized when the temperature is raised in a vacuum or in an inert gas atmosphere, contributing carbon to the laundry.
La mezcla de polímeros orgánicos consiste en un polímero insoluble en agua (Tipo A) y en un polímero soluble en agua (Tipo B) .  The organic polymer blend consists of a water insoluble polymer (Type A) and a water soluble polymer (Type B).
El polímero Tipo A puede consistir preferentemente en un polímero seleccionado de un grupo que consiste en polímeros de alcoholes vinílicos, poliuretanos, poliamidas, poliacrilatos y polimetacrilatos , así como cualquiera de sus combinaciones. Más preferentemente, dicho polímero puede consistir en acetato de polivinilo (PVA) , el cual presenta una buena combinación de propiedades y un bajo precio en comparación con el aluminio; polivinilbutiral , por su limpia combustión que minimiza los residuos de carbono; o poli (oxi-metileno) . The Type A polymer may preferably consist of a polymer selected from a group consisting of polymers of vinyl alcohols, polyurethanes, polyamides, polyacrylates and polymethacrylates, as well as any combination thereof. More preferably, said polymer may consist of polyvinyl acetate (PVA), which has a good combination of properties and a low price compared to aluminum; polyvinylbutyral, for its clean combustion that minimizes carbon residues; or poly (oxymethylene).
En una realización preferida de la invención, el polímero Tipo A puede consistir en Kollidon©, el cual comprende 8 partes (p/p) de PVA y 2 partes (p/p) de polivinilpirrolidona .  In a preferred embodiment of the invention, the Type A polymer may consist of Kollidon®, which comprises 8 parts (w / w) of PVA and 2 parts (w / w) of polyvinylpyrrolidone.
De manera preferida, el porcentaje en peso de dicho polímero Tipo A en la composición se encuentra comprendido entre un 0.05% y un 5.0%.  Preferably, the weight percentage of said Type A polymer in the composition is between 0.05% and 5.0%.
El polímero del Tipo B puede consistir preferentemente en un polímero seleccionado de un grupo que consiste en polietilenglicol (PEG) , óxido de polietileno, polietileno, celulosas, copolímeros de etileno, polipropileno y óxido de propileno, así como cualquiera de sus combinaciones.  The Type B polymer may preferably consist of a polymer selected from a group consisting of polyethylene glycol (PEG), polyethylene oxide, polyethylene, celluloses, copolymers of ethylene, polypropylene and propylene oxide, as well as any combination thereof.
Preferentemente, se propone el uso del polietilenglicol por su buena combinación de propiedades y su bajo precio en comparación con el aluminio, así como el polietileno por su bajo precio. El óxido de polietileno, si bien presenta una buena compatibilidad con polímeros del Tipo A y del Tipo B y tiene buenas propiedades de descomposición térmica, es mucho más caro que el polietilenglicol.  Preferably, the use of polyethylene glycol is proposed for its good combination of properties and its low price compared to aluminum, as well as polyethylene for its low price. Polyethylene oxide, although it has good compatibility with Type A and Type B polymers and has good thermal decomposition properties, is much more expensive than polyethylene glycol.
De la misma manera que el polímero Tipo A, el porcentaje en peso del polímero Tipo B en la composición se encuentra comprendido preferentemente entre un 0.05% y un 5.0%.  In the same way as Type A polymer, the weight percentage of Type B polymer in the composition is preferably between 0.05% and 5.0%.
Una característica adicional, de gran importancia para la invención, es que el peso molecular de los polímeros constituyentes de la mezcla sea elevado. De este modo, de manera preferida, el peso molecular de los polímeros empleados en la composición es preferentemente superior a 1000 g/mol, y más preferentemente, superior a 3000 g/mol . En una realización preferida de la invención en la que el polímero Tipo B sea PEG, a la hora de seleccionar el peso molar del PEG empleado en la composición, será necesario tener en cuenta que el valor de hidroxilo disminuye de manera inversamente proporcional al peso molecular. Además, el precio del polietilenglicol depende del peso molecular. An additional feature, of great importance for the invention, is that the molecular weight of the constituent polymers of the mixture is high. Thus, preferably, the molecular weight of the polymers used in the composition is preferably greater than 1000 g / mol, and more preferably, greater than 3000 g / mol. In a preferred embodiment of the invention in which the Type B polymer is PEG, when selecting the molar weight of the PEG used in the composition, it will be necessary to take into account that the hydroxyl value decreases inversely proportional to the molecular weight . In addition, the price of polyethylene glycol depends on the molecular weight.
El PEG 5000-7000 presenta la mejor combinación de valor de hidroxilo y de precio, por lo que es especialmente preferido en la presente invención. Además, el polietilenglicol tiene un índice de oxidación alto, por lo que se descompone en componentes de peso molecular menor sin dejar residuos alrededor de los 200°C. De este modo, entre los polímeros del Tipo B, es especialmente preferido el polietilenglicol (PEG) de peso molecular superior a 4000 g/mol . PEG 5000-7000 has the best combination of hydroxyl value and price, so it is especially preferred in the present invention. In addition, polyethylene glycol has a high oxidation index, so it decomposes into components of lower molecular weight without leaving residues around 200 ° C. Thus, among the polymers of Type B, polyethylene glycol (PEG) of molecular weight greater than 4000 g / mol is especially preferred.
En una realización preferida de la invención, la composición descrita está constituida por los elementos que se muestran en la tabla I, donde se recoge asimismo el porcentaje en peso preferido de cada uno de dichos elementos, de modo que la suma total de todos ellos en la composición es el 100%. En relación al polímero del Tipo A y al polímero del Tipo B, dichos polímeros pueden estar presentes de manera independiente o en combinación:  In a preferred embodiment of the invention, the described composition is constituted by the elements shown in Table I, where the preferred percentage by weight of each of said elements is also collected, so that the total sum of all of them in The composition is 100%. In relation to the Type A polymer and the Type B polymer, said polymers may be present independently or in combination:
Tabla I. Intervalos en porcentaje en peso de los elementos que comprenden la composición Table I. Intervals in percentage by weight of the elements comprising the composition
Figure imgf000010_0001
Figure imgf000010_0001
Un aspecto de vital importancia para conseguir una buena unión aglomerante-Mn es que sus granulometrías sean complementarias. Esto requiere que las partículas de la mezcla de polímeros rellenen eficientemente los huecos existentes entre las partículas de Mn. De esta manera, se disminuirá la presencia de uniones débiles de la tableta [R. Fernández, G. González-Doncel, R. Antolín, T. Posada y G. Borge, Alton T. Tabereaux TMS (The Minerals, Metals & Materials Society) , 2004, pp. 769-773] . En el caso del Mn, el cual proviene tradicionalmente de molturación de piezas de mayor tamaño obtenidas por electrólisis, se dispone típicamente de granulometrías como la descrita en la tabla 11(a) : One aspect of vital importance to achieve a good binding agglomerant-Mn is that its granulometries are complementary. This requires that the particles of the polymer mixture efficiently fill the gaps between the Mn particles. In this way, the presence of weak tablet joints will be reduced [R. Fernández, G. González-Doncel, R. Antolín, T. Posada and G. Borge, Alton T. Tabereaux TMS (The Minerals, Metals & Materials Society), 2004, pp. 769-773]. In the case of Mn, which traditionally comes from grinding larger pieces obtained by electrolysis, granulometries are typically available as described in Table 11 (a):
Tabla II (a) . Granulometría típica de los polvos de Mn Table II (a). Typical granulometry of Mn powders
Tamaño partícula ( m) Porcentaje (%)  Particle size (m) Percentage (%)
< 50 0 - 20 50 - 150 5 - 25<50 0 - 20 50 - 150 5 - 25
150 - 350 30 - 60 150 - 350 30 - 60
> 350 15 - 35  > 350 15 - 35
De manera particular, un ejemplo de la granulometria de los polvos de Mn puede ser la que se muestra en la siguiente tabla II (b) : In particular, an example of the granulometry of Mn powders may be that shown in the following table II (b):
Tabla II (b) . Granulometria típica de los polvos de Mn  Table II (b). Typical granulometry of Mn powders
Figure imgf000011_0001
Figure imgf000011_0001
Es decir, de manera cualitativa, tras el proceso de molienda se obtienen partículas de Mn de menos de 1 mm, y se procura minimizar la fracción de finos (partículas cuyo tamaño es <100μπι) para favorecer el flujo del polvo a través de los distintos dispositivos del proceso de fabricación industrial. Conocidos estos datos, es posible calcular la granulometria ideal de la mezcla de polímeros con finalidad aglomerante. Para ello, hay que tener en cuenta que los huecos que quedan entre las partículas esféricas del metal son del orden del diámetro promedio de las partículas dividido por tres. Por lo tanto, conocida la distribución de tamaños de partida del Mn es necesario disponer de una mezcla de polímeros que presente una distribución de tamaños similar a la del Mn, en porcentaje de aparición, pero dividiendo cada tamaño por tres. La granulometria de los polvos de la mezcla de polímeros utilizada conforme a dicho criterio para la presente invención se encuentra descrita en la Tabla III (a) : That is, qualitatively, after the grinding process, particles of Mn of less than 1 mm are obtained, and the fraction of fines (particles whose size is <100μπι) is minimized to favor the flow of dust through the different Industrial manufacturing process devices. Once these data are known, it is possible to calculate the ideal particle size of the polymer mixture with binder purpose. For this, it must be taken into account that the gaps that remain between the spherical particles of the metal are of the order of the average diameter of the particles divided by three. Therefore, it is known that the distribution of starting sizes of Mn is necessary to have a mixture of polymers that has a size distribution similar to that of Mn, in percentage of appearance, but dividing each size by three. The granulometry of the powders of the polymer mixture used according to said criteria for the present invention is described in Table III (a):
Tabla III (a) . Granulometria general de los polvos de PEG  Table III (a). General granulometry of PEG powders
Figure imgf000011_0002
Figure imgf000011_0002
De manera particular, dicha granulometria puede igual a la que se muestra en la tabla III (b) : In particular, said granulometry can same as shown in table III (b):
Tabla III (b) . Granulometria particular de los polvos de PEG Table III (b). Particular particle size of PEG powders
Figure imgf000012_0001
En el proceso de mezcla de polvos existe una alta probabilidad de segregación debido a la diferencia de densidades entre los constituyentes de la mezcla, puesto que la densidad de los polímeros es de aproximadamente 1 g/cm3, mientras que la del Mn es de 7.5 g/cm3. Sin embargo, este efecto se reduce de manera importante porque los polímeros descritos son extremadamente dúctiles por encima de 25°C. De esta manera, la segregación se reduce cuando el proceso de mezcla se realiza a escala industrial, con una masa de polvo en las mezcladoras típicamente superior a los 100 kg. En estos casos, el Mn queda impregnado por los polímeros por efecto del rozamiento entre partículas durante la mezcla. A pesar de este hecho, es deseable trabajar con granulometrías de aglomerante finas que permita una distribución homogénea del aglomerante en la mezcla de polvos como la descrita en la Tabla II. Adicionalmente, se mejora la fluidez de la mezcla al utilizar polímeros por sus características lubricantes, especialmente la del polietilenglicol , con un peso molecular superior a 6000 g/mol.
Figure imgf000012_0001
In the powder mixing process there is a high probability of segregation due to the difference in densities between the constituents of the mixture, since the density of the polymers is approximately 1 g / cm 3 , while that of Mn is 7.5 g / cm 3 . However, this effect is significantly reduced because the polymers described are extremely ductile above 25 ° C. In this way, segregation is reduced when the mixing process is carried out on an industrial scale, with a mass of powder in the mixers typically exceeding 100 kg. In these cases, the Mn is impregnated by the polymers due to the friction between particles during mixing. Despite this fact, it is desirable to work with fine binder granulometries that allow a homogeneous distribution of the binder in the powder mixture as described in Table II. Additionally, the fluidity of the mixture is improved by using polymers for their lubricating characteristics, especially that of polyethylene glycol, with a molecular weight greater than 6000 g / mol.
Un aspecto a considerar en paralelo es que esta fracción de polvo fino suele oxidarse con facilidad en contacto con la atmósfera. Por este motivo es deseable utilizar polímeros que presenten grupos polares (solubles en agua) que tienen una fuerte interacción con materiales cerámicos u óxidos. Típicamente, la unión entre el polímero y el metal (o el óxido de metal) se incrementa con el peso molecular del polímero utilizado.  One aspect to consider in parallel is that this fraction of fine dust usually oxidizes easily in contact with the atmosphere. For this reason it is desirable to use polymers that have polar groups (soluble in water) that have a strong interaction with ceramic materials or oxides. Typically, the bond between the polymer and the metal (or the metal oxide) increases with the molecular weight of the polymer used.
Tras la consolidación de los componentes de la tableta (manganeso, polímero insoluble en agua y/o polímero soluble en agua, y opcionalmente aluminio) , mediante compactación en una prensa a temperatura ambiente (entre 10°C y 45°C) , es beneficioso para mejorar la consistencia mecánica y la disolución de las tabletas en el caldo de la colada, llevar a cabo un tratamiento térmico de la tableta consolidada. Este tratamiento consiste en mantener la tableta a una temperatura por encima del punto de fusión del polímero con menor punto de fusión durante un tiempo concreto, por ejemplo 20 minutos. También es beneficioso para la consistencia mecánica y la disolución de las tabletas en el caldo de la colada realizar dicho tratamiento térmico, durante un tiempo similar, a una temperatura por encima del punto de fusión del polímero con mayor punto de fusión. After consolidation of the tablet components (manganese, water insoluble polymer and / or water soluble polymer, and optionally aluminum), by compaction in A press at room temperature (between 10 ° C and 45 ° C), is beneficial to improve the mechanical consistency and dissolution of the tablets in the broth of the laundry, carry out a heat treatment of the consolidated tablet. This treatment consists in keeping the tablet at a temperature above the melting point of the polymer with the lowest melting point for a specific time, for example 20 minutes. It is also beneficial for the mechanical consistency and dissolution of the tablets in the broth of the laundry to perform said heat treatment, for a similar time, at a temperature above the melting point of the polymer with the highest melting point.
La principal ventaja de la invención es que se puede eliminar completamente el uso de aluminio (o de hierro) como aglomerante y que se puede reducir la cantidad total de aglomerantes que se añaden para obtener las tabletas. Por ambos motivos se reduce el coste de fabricación de tabletas. Además, la resistencia mecánica de las tabletas mejora varios órdenes de magnitud y paralelamente se mejoran los tiempos de disolución de las tabletas en el caldo.  The main advantage of the invention is that the use of aluminum (or iron) as a binder can be completely eliminated and that the total amount of binders added to obtain the tablets can be reduced. For both reasons the cost of manufacturing tablets is reduced. In addition, the mechanical strength of the tablets improves several orders of magnitude and in parallel the dissolution times of the tablets in the broth are improved.
A continuación, se presentan una serie de ejemplos de realizaciones particulares y no limitativas de la invención, los cuales permiten demostrar las ventajas señaladas. Ejemplos de realización de la invención  Next, a series of examples of particular and non-limiting embodiments of the invention are presented, which allow demonstrating the advantages indicated. Examples of embodiment of the invention
Ejemplo 1. Mezcla de 5% en peso de PEG en forma de polvo, un 10% en peso de aluminio en forma de polvo y un 85% en peso de Mn electrolítico proveniente de molturacion;  Example 1. Mix of 5% by weight of PEG in powder form, 10% by weight of aluminum in powder form and 85% by weight of electrolytic Mn from milling;
· Ejemplo 2. Mezcla de 5% en peso de PEG con 95% de Mn electrolítico proveniente de molturacion;  · Example 2. Mix of 5% by weight of PEG with 95% of electrolytic Mn from milling;
• Ejemplo 3. Mezcla de 2,5% en peso de PVA+PEG con 97,5% en peso de Mn electrolítico proveniente de molturacion; Ejemplo 4. Medida de la resistencia mecánica de las tabletas obtenidas en los ejemplos 1 a 3. Ejemplo 1. Mezcla de 5% en peso de PEG en forma de polvo y un 10% en peso de aluminio en forma de polvo y un 85% en peso de Mn electrolítico proveniente de molturacion. Los polvos descritos en la tabla IV se mezclaron en una túrbula durante 15 minutos a una velocidad de aproximadamente 1 revolución por segundo para optimizar el proceso de mezclado de los polvos. • Example 3. Mixture of 2.5% by weight of PVA + PEG with 97.5% by weight of electrolytic Mn from milling; Example 4. Measurement of the mechanical strength of the tablets obtained in examples 1 to 3. Example 1. Mix of 5% by weight of PEG in powder form and 10% by weight of aluminum in powder form and 85% by weight of electrolytic Mn from milling. The powders described in Table IV were mixed in a turbot for 15 minutes at a rate of approximately 1 revolution per second to optimize the powder mixing process.
En este ejemplo se llevó a cabo la preparación de tabletas de Mn a partir de una composición particular de acuerdo al objeto de la presente invención. En la tabla IV se recogen los intervalos en peso de los distintos elementos presentes en la composición:  In this example, the preparation of Mn tablets from a particular composition according to the object of the present invention was carried out. Table IV shows the intervals by weight of the different elements present in the composition:
Tabla IV. Intervalos en porcentaje en peso de los elementos que comprenden la composición  Table IV Intervals in percentage by weight of the elements that comprise the composition
Figure imgf000014_0001
Figure imgf000014_0001
La granulometría del Mn empleado en el procedimiento fue la correspondiente a la tabla II (b) . Por otra parte, la granulometría de los polvos de PEG fue la que se muestra en la tabla III (b) . The granulometry of the Mn used in the procedure was that corresponding to Table II (b). On the other hand, the granulometry of PEG powders was the one shown in Table III (b).
Por otra parte, el aluminio empleado en la mezcla fue aluminio atomizado en polvo con tamaño de partícula entre 100 μπι y 800 μπι. La mezcla resultante se vierte minimizando la segregación de ambos componentes en el utillaje de compactación, con su superficie interior lubricada con estearato de zinc.  On the other hand, the aluminum used in the mixture was atomized aluminum powder with particle size between 100 μπι and 800 μπι. The resulting mixture is poured minimizing the segregation of both components in the compaction tooling, with its inner surface lubricated with zinc stearate.
La mezcla de polvos de acuerdo a las tablas II y III fue compactada en una prensa en frío a una de temperatura entre 10°C y 45°C.  The powder mixture according to Tables II and III was compacted in a cold press at a temperature between 10 ° C and 45 ° C.
Posteriormente, se extrajo la tableta obtenida mediante la aplicación de alrededor de 700 kg de presión.  Subsequently, the tablet obtained was extracted by applying about 700 kg of pressure.
La tableta resultante tuvo un diámetro de 40 mm y una altura de aproximadamente 22 mm con un peso final de 75 gramos. La densidad aparente resultante del proceso de compactación fue de 2.7g/cm3. The resulting tablet had a diameter of 40 mm and a height of approximately 22 mm with a final weight of 75 grams. The apparent density resulting from the process of Compaction was 2.7g / cm 3 .
La resistencia mecánica de las tabletas obtenidas se estudió mediante un ensayo de caída libre desde aproximadamente 1 metro de altura. Los resultados de este ensayo se recogen en la tabla VII.  The mechanical strength of the obtained tablets was studied by a free fall test from approximately 1 meter in height. The results of this test are shown in Table VII.
Para estudiar la velocidad de disolución de las tabletas resultantes se realizó una colada con 5kg de aluminio de 99.99% de pureza a una temperatura de 740°C utilizando un horno de resistencias y un crisol de arena y grafito .  In order to study the dissolution rate of the resulting tablets, a wash with 5kg of 99.99% pure aluminum at a temperature of 740 ° C was carried out using a resistance furnace and a sand and graphite crucible.
En la figura 2 se representa la concentración de Mn medido mediante espectroscopia de emisión óptica por chispa, a distintos tiempos de extracción de muestra. La tasa de recuperación de Mn es del 98% obteniéndose este valor en un tiempo 2.4 veces menor que usando únicamente Al como elemento ligante.  Figure 2 shows the concentration of Mn measured by optical emission spectroscopy by spark, at different sample extraction times. The recovery rate of Mn is 98%, obtaining this value in a time 2.4 times less than using only Al as the binding element.
Ejemplo 2. Mezcla de 5% en peso de PEG con 95% de Mn electrolítico proveniente de molturacion. Example 2. Mix of 5% by weight of PEG with 95% of electrolytic Mn from milling.
Los polvos descritos en la tabla V se mezclaron en una túrbula durante 15 minutos a una velocidad de aproximadamente 1 revolución por segundo para optimizar el proceso de mezclado de polvos.  The powders described in Table V were mixed in a turbot for 15 minutes at a rate of approximately 1 revolution per second to optimize the powder mixing process.
En este ejemplo, se llevó a cabo la preparación de tabletas de Mn a partir de una composición particular de acuerdo al objeto de la presente invención. En la tabla V, se recogen los intervalos en peso de los distintos elementos presentes en la composición: Tabla V. Intervalos en porcentaje en peso de los elementos que comprenden la composición  In this example, the preparation of Mn tablets from a particular composition according to the object of the present invention was carried out. Table V shows the intervals by weight of the different elements present in the composition: Table V. Intervals in percentage by weight of the elements comprising the composition
Figure imgf000015_0001
Figure imgf000015_0001
La granulometría del Mn empleado en el procedimiento fue la correspondiente a la tabla II (b) . Por otra parte, la granulometria de los polvos de PEG fue la que se muestra en la tabla III (b) : The granulometry of the Mn used in the procedure was the one corresponding to table II (b). On the other hand, the granulometry of PEG powders was that shown in Table III (b):
La resistencia mecánica de las tabletas obtenidas se estudió mediante un ensayo de caída libre desde aproximadamente 740 milímetros de altura. Los resultados de este ensayo se recogen en la tabla VII.  The mechanical strength of the obtained tablets was studied by a free fall test from approximately 740 millimeters in height. The results of this test are shown in Table VII.
Para estudiar la velocidad de disolución de las tabletas resultantes se realizó una colada con 5kg de aluminio de 99,99% de pureza a una temperatura de 740°C utilizando un horno de resistencias y un crisol de arena y grafito .  To study the dissolution rate of the resulting tablets, a wash with 5kg of 99.99% pure aluminum at a temperature of 740 ° C was carried out using a resistance furnace and a sand and graphite crucible.
En la figura 2 se representa la concentración de Mn medido mediante espectroscopia de emisión óptica por chispa a distintos tiempos de extracción de muestra. La tasa de recuperación de Mn es del 98% obteniéndose este valor en un tiempo 2.4 veces menor que usando únicamente Al como elemento ligante. Ejemplo 3. Mezcla de 2,5% en peso de PVA y PEG con 97,5% en peso de Mn electrolítico proveniente de molturacion.  Figure 2 shows the concentration of Mn measured by optical emission spectroscopy by spark at different sample extraction times. The recovery rate of Mn is 98%, obtaining this value in a time 2.4 times less than using only Al as the binding element. Example 3. Mix of 2.5% by weight of PVA and PEG with 97.5% by weight of electrolytic Mn from milling.
Los polvos descritos en la tabla V se mezclaron en una túrbula durante 15 minutos a una velocidad de aproximadamente 1 revolución por segundo para optimizar el proceso de mezclado de polvos.  The powders described in Table V were mixed in a turbot for 15 minutes at a rate of approximately 1 revolution per second to optimize the powder mixing process.
En este ejemplo, se llevó a cabo la preparación de tabletas de Mn a partir de una composición particular de acuerdo al objeto de la presente invención. En la tabla VI, se recogen los intervalos en peso de los distintos elementos presentes en la composición:  In this example, the preparation of Mn tablets from a particular composition according to the object of the present invention was carried out. Table VI shows the intervals by weight of the different elements present in the composition:
Tabla VI. Intervalos en porcentaje en peso de los elementos que comprenden la composición Table VI Intervals in percentage by weight of the elements that comprise the composition
Elemento Intervalo de composición (%) Element Composition interval (%)
Manganeso 97.5 Manganese 97.5
Polvos de polietilenglicol  Polyethylene glycol powders
(PEG) de peso molecular 1.25  (PEG) of molecular weight 1.25
superior a 5000 g/mol Polvos de acetato de greater than 5000 g / mol Acetate Powders
polivinilo (PVA) de peso  polyvinyl (PVA) weight
1.25  1.25
molecular superior a 5000  molecular greater than 5000
g/mol  g / mol
La granulometria del Mn empleado en el procedimiento fue la correspondiente a la tabla II (b) . Finalmente, el PVA fue molturado hasta obtener polvos de PVA con un tamaño de partícula comprendido entre ΙΟΟμπι y 800μπι. Por otra parte, la granulometria de los polvos de PEG fue la que se muestra en la tabla III (b) . The granulometry of the Mn used in the procedure was that corresponding to Table II (b). Finally, the PVA was ground to obtain PVA powders with a particle size between ΙΟΟμπι and 800μπι. On the other hand, the granulometry of PEG powders was that shown in Table III (b).
Para estudiar la velocidad de disolución de las tabletas resultantes se realizó una colada con 5kg de aluminio 99,9% de pureza a una temperatura de 740°C utilizando un horno de resistencias y un crisol de arena y grafito .  To study the dissolution rate of the resulting tablets, a wash with 5kg of 99.9% pure aluminum at a temperature of 740 ° C was carried out using a resistance furnace and a sand and graphite crucible.
En la figura 2 se representa la concentración de Mn medido mediante espectroscopia de emisión óptica por chispa a distintos tiempos de extracción de muestra. La tasa de recuperación de Mn es del 98% obteniéndose este valor en un tiempo 2.4 veces menor que usando únicamente Al como elemento ligante. Ejemplo 4. Medida de la resistencia mecánica de las tabletas obtenidas en los ejemplos 1 a 3.  Figure 2 shows the concentration of Mn measured by optical emission spectroscopy by spark at different sample extraction times. The recovery rate of Mn is 98%, obtaining this value in a time 2.4 times less than using only Al as the binding element. Example 4. Measurement of the mechanical strength of the tablets obtained in examples 1 to 3.
La resistencia mecánica de las tabletas obtenidas se estudió mediante el denominado ensayo de caída (drop test) en el que se han dejado caer las tabletas en caída libre desde 740 mm de altura contra un suelo duro y rígido y se cuantifica la cantidad de lanzamientos necesaria para que la tableta pierda una cantidad de material determinada y se rompa de manera evidente. Los resultados de este ensayo se recogen en la tabla VII. En esta tabla VII se muestra el número de caídas que ha resistido cada tableta en el test de caída desde 740 mm, junto con las condiciones de compactación y tratamiento térmico posterior realizado a cada tableta. Todas las tabletas fueron compactadas a 25°C y 94 Tn aproximadamente. El resultado de número de caídas en el caso de que sea menor de 2, es el promedio de realizar el test en al menos tres tabletas. The mechanical strength of the obtained tablets was studied by means of the so-called drop test in which the tablets were dropped in free fall from 740 mm high against a hard and rigid ground and the amount of throws needed is quantified so that the tablet loses a certain amount of material and breaks in an obvious way. The results of this test are shown in Table VII. Table VII shows the number of falls that each tablet has withstood in the drop test from 740 mm, together with the compaction conditions and subsequent heat treatment performed on each tablet. All tablets were compacted at 25 ° C and approximately 94 Tn. The result of number of falls in If it is less than 2, it is the average of performing the test on at least three tablets.
Tabla VII. Resultados del ensayo de caída Table VII Fall test results
Figure imgf000018_0001
Figure imgf000018_0001
*Estas tabletas no se rompieron incluso tras repetido intentos de caida libre desde una altura de unos dos metros  * These tablets did not break even after repeated attempts at free fall from a height of about two meters

Claims

Reivindicaciones Claims
1. Composición para la fabricación de tabletas de Mn caracterizada por que comprende: 1. Composition for the manufacture of Mn tablets characterized by comprising:
(a) polvo de Mn en un porcentaje comprendido entre un 70% y un 99.5% en peso de la composición;  (a) Mn powder in a percentage comprised between 70% and 99.5% by weight of the composition;
(b) un primer aglomerante en polvo seleccionado entre al menos un polímero orgánico insoluble en agua o al menos un polímero orgánico soluble en agua, o una mezcla de ambos, donde dicho primer aglomerante no es una cera.  (b) a first powder binder selected from at least one water insoluble organic polymer or at least one water soluble organic polymer, or a mixture of both, wherein said first binder is not a wax.
2. Composición, de acuerdo a la reivindicación 1, donde el primer aglomerante se encuentra comprendido entre un 0,05% y un 5% en peso de la composición. 2. Composition according to claim 1, wherein the first binder is between 0.05% and 5% by weight of the composition.
3. Composición, de acuerdo a la reivindicación 1 ó 2, caracterizada por que comprende un segundo aglomerante en polvo seleccionado entre aluminio, hierro, o cualquiera de sus aleaciones. 3. Composition according to claim 1 or 2, characterized in that it comprises a second powder binder selected from aluminum, iron, or any of its alloys.
4. Composición, de acuerdo a la reivindicación 3, donde el segundo aglomerante se encuentra en un porcentaje inferior al 30% en peso de la composición. 4. Composition according to claim 3, wherein the second binder is in a percentage less than 30% by weight of the composition.
5. Composición, de acuerdo a una cualquiera de las reivindicaciones 1 a 4, donde el polímero orgánico insoluble en agua es seleccionado de un grupo que consiste en polímeros de alcoholes vinílicos, poliuretanos , poliamidas, poliacrilatos y polimetacrilatos , así como cualquiera de sus combinaciones. 5. Composition according to any one of claims 1 to 4, wherein the water-insoluble organic polymer is selected from a group consisting of polymers of vinyl alcohols, polyurethanes, polyamides, polyacrylates and polymethacrylates, as well as any combination thereof .
6. Composición, de acuerdo a la reivindicación 5, donde el polímero orgánico insoluble en agua es seleccionado de un grupo que consiste en acetato de polivinilo o PVA, polivinil butiral y polioximetileno, así como cualquiera de sus combinaciones. 6. Composition according to claim 5, wherein the water-insoluble organic polymer is selected from a group consisting of polyvinyl acetate or PVA, polyvinyl butyral and polyoxymethylene, as well as any combination thereof.
7. Composición, de acuerdo a la reivindicación 6, donde el polímero orgánico insoluble en agua comprende 8 partes (p/p) de PVA y 2 partes (p/p) de polivinilpirrolidona . 7. Composition according to claim 6, wherein the water-insoluble organic polymer comprises 8 parts (w / w) of PVA and 2 parts (w / w) of polyvinylpyrrolidone.
8. Composición, de acuerdo a una cualquiera de las reivindicaciones 1 a 7, donde el polímero orgánico insoluble en agua es un polímero con un peso molecular por encima de 1000 g/mol. 8. Composition according to any one of claims 1 to 7, wherein the water insoluble organic polymer is a polymer with a molecular weight above 1000 g / mol.
9. Composición, de acuerdo a una cualquiera de las reivindicaciones 1 a 8, donde el polímero orgánico soluble en agua es seleccionado de un grupo que consiste en polietilenglicol , óxido de polietileno, polietileno, copolímeros de etileno, polipropileno y óxido de propileno, así como cualquiera de sus combinaciones. 9. Composition according to any one of claims 1 to 8, wherein the water soluble organic polymer is selected from a group consisting of polyethylene glycol, polyethylene oxide, polyethylene, copolymers of ethylene, polypropylene and propylene oxide, as well Like any of your combinations.
10. Composición, de acuerdo a la reivindicación 9, donde el polímero orgánico soluble en agua es un polímero con un peso molecular por encima de 1000 g/mol. 10. Composition according to claim 9, wherein the water-soluble organic polymer is a polymer with a molecular weight above 1000 g / mol.
11. Procedimiento de obtención de tabletas de Mn a partir de una composición de acuerdo a una cualquiera de las reivindicaciones 1 a 10, caracterizado porque comprende la compactación de los elementos que componen dicha composición a temperatura ambiente. 11. Method of obtaining Mn tablets from a composition according to any one of claims 1 to 10, characterized in that it comprises compacting the elements that comprise said composition at room temperature.
12. Procedimiento, de acuerdo a la reivindicación 11, caracterizado por que comprende una etapa, posterior a la compactación, de tratamiento térmico a una temperatura por encima de la temperatura de fusión de al menos un polímero orgánico insoluble en agua o de al menos un polímero orgánico soluble en agua. 12. A method according to claim 11, characterized in that it comprises a stage, after compaction, of heat treatment at a temperature above the melting temperature of at least one water-insoluble organic polymer or at least one water soluble organic polymer.
13. Tableta de Mn obtenida a partir de un procedimiento de acuerdo a la reivindicación 11 o 12. 13. Mn tablet obtained from a method according to claim 11 or 12.
14. Uso de una tableta según la reivindicación 13 como elemento aleante en la colada de metales. 14. Use of a tablet according to claim 13 as an alloying element in metal casting.
PCT/ES2012/070433 2011-06-20 2012-06-08 Composition and method for producing mn tablets WO2012175770A2 (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2361925A (en) * 1942-07-04 1944-11-07 Minerals And Metals Corp Preparation of manganese products
AU5164073A (en) * 1972-02-02 1974-08-01 Foseco International Limited Bonded compositions
US4362559A (en) * 1981-03-09 1982-12-07 American Cyanamid Company Method of introducing addition agents into a metallurgical operation
US5951737A (en) * 1998-06-16 1999-09-14 National Research Council Of Canada Lubricated aluminum powder compositions
EP1045040A1 (en) * 1999-04-15 2000-10-18 Bostlan, S.A. Additive for adding one or more metals into aluminium alloys

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2361925A (en) * 1942-07-04 1944-11-07 Minerals And Metals Corp Preparation of manganese products
AU5164073A (en) * 1972-02-02 1974-08-01 Foseco International Limited Bonded compositions
US4362559A (en) * 1981-03-09 1982-12-07 American Cyanamid Company Method of introducing addition agents into a metallurgical operation
US5951737A (en) * 1998-06-16 1999-09-14 National Research Council Of Canada Lubricated aluminum powder compositions
EP1045040A1 (en) * 1999-04-15 2000-10-18 Bostlan, S.A. Additive for adding one or more metals into aluminium alloys

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