EP2908968A2 - Mélanges de matière à mouler à base de liant inorganique et procédé de production de moules et de noyaux pour la coulée de métaux - Google Patents

Mélanges de matière à mouler à base de liant inorganique et procédé de production de moules et de noyaux pour la coulée de métaux

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Publication number
EP2908968A2
EP2908968A2 EP13811773.4A EP13811773A EP2908968A2 EP 2908968 A2 EP2908968 A2 EP 2908968A2 EP 13811773 A EP13811773 A EP 13811773A EP 2908968 A2 EP2908968 A2 EP 2908968A2
Authority
EP
European Patent Office
Prior art keywords
molding material
weight
material mixture
phosphate
molding
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.)
Granted
Application number
EP13811773.4A
Other languages
German (de)
English (en)
Other versions
EP2908968B1 (fr
Inventor
Dennis BARTELS
Heinz DETERS
Antoni Gieniec
Diether Koch
Hannes LINCKE
Martin Oberleiter
Oliver Schmidt
Carolin WALLENHORST
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.)
ASK Chemicals GmbH
Original Assignee
ASK Chemicals GmbH
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Filing date
Publication date
Application filed by ASK Chemicals GmbH filed Critical ASK Chemicals GmbH
Priority to EP21199894.3A priority Critical patent/EP3950168A1/fr
Priority to PL13811773T priority patent/PL2908968T3/pl
Publication of EP2908968A2 publication Critical patent/EP2908968A2/fr
Application granted granted Critical
Publication of EP2908968B1 publication Critical patent/EP2908968B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B22—CASTING; POWDER METALLURGY
    • B22C—FOUNDRY MOULDING
    • B22C1/00—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds
    • B22C1/16—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents
    • B22C1/18—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents of inorganic agents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B22—CASTING; POWDER METALLURGY
    • B22C—FOUNDRY MOULDING
    • B22C1/00—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds
    • B22C1/16—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents
    • B22C1/18—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents of inorganic agents
    • B22C1/181—Cements, oxides or clays
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B22—CASTING; POWDER METALLURGY
    • B22C—FOUNDRY MOULDING
    • B22C1/00—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds
    • B22C1/16—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents
    • B22C1/18—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents of inorganic agents
    • B22C1/186—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents of inorganic agents contaming ammonium or metal silicates, silica sols
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B22—CASTING; POWDER METALLURGY
    • B22C—FOUNDRY MOULDING
    • B22C9/00—Moulds or cores; Moulding processes
    • B22C9/02—Sand moulds or like moulds for shaped castings
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B22—CASTING; POWDER METALLURGY
    • B22C—FOUNDRY MOULDING
    • B22C9/00—Moulds or cores; Moulding processes
    • B22C9/12—Treating moulds or cores, e.g. drying, hardening

Definitions

  • the invention relates to molding material mixtures based on inorganic binders for the production of molds and cores for metal casting consisting of at least one refractory molding material, an inorganic binder and particulate amorphous silica as an additive. Furthermore, the invention relates to a process for the production of molds and cores using the molding material mixtures.
  • Molds essentially consist of molds and shapes and cores, which represent the negative forms of the casting to be produced. These cores and forms consist of a refractory material, such as quartz sand, and a suitable binder, which gives the mold after removal from the mold sufficient mechanical strength.
  • the refractory molding base material is preferably present in a free-flowing form, so that it can be filled into a suitable mold and compacted there.
  • the binder produces a firm cohesion between the particles of the molding base material, so that the casting mold obtains the required mechanical stability.
  • Molds form the outer wall of the casting during casting, cores are used to form cavities within the casting. It is not absolutely necessary that the forms and cores are made of the same material. Thus, e.g. In chill casting, the external shape of the castings with the help of metallic permanent molds. Also possible is a combination of molds and cores made from differently blended molding mixes and by different processes. If, in simplification, only forms are mentioned below, the statements apply to the same extent to cores based on the same molding material mixture and produced by the same process. For the production of molds both organic and inorganic binders can be used, the curing of which can be effected in each case by cold or hot processes.
  • Cold processes are those processes which are carried out essentially without heating the mold used for core production, generally at room temperature or at a temperature caused by a possible reaction.
  • the curing takes place, for example, by passing a gas through the molding material mixture to be cured, thereby triggering a chemical reaction.
  • hot processes the molding material mixture is heated to a sufficiently high temperature after molding, for example by the heated mold, to expel the solvent contained in the binder and / or to initiate a chemical reaction by which the binder is cured.
  • organic binders Due to their technical properties, organic binders have currently been economically viable. the greater importance in the market. Regardless of their composition, however, they have the disadvantage that they decompose during the casting and thereby z. significant amounts of pollutants, e.g. Benzene, toluene and xylenes emit. In addition, the casting of organic binder usually leads to odor and smoke pollution. In some systems, undesirable emissions even occur during core manufacturing and / or storage. Although binder development has reduced emissions over the years, they can not be completely avoided with organic binders. For this reason, in recent years, the research and development work has again turned to the inorganic binder to further improve these and the product properties of the molds and cores thus produced.
  • pollutants e.g. Benzene, toluene and xylenes emit.
  • the casting of organic binder usually leads to odor and smoke pollution. In some systems, undesirable emissions even occur during core manufacturing and / or storage.
  • binder development has reduced emissions over the years, they
  • Inorganic binders have been known for a long time, especially those based on water glasses. They were widely used in the 1950s and 60s, but with the advent of modern organic binders, they quickly lost their importance. There are three different methods of curing the water glasses:
  • C0 2 curing eg in a hot box process or by microwave treatment.
  • C0 2 curing is described, for example, in GB 634817, hardening by means of hot air without C0 2 addition, for example in H. Polzin, W. Tilch and T. Kooyers, Foundry Practice 6/2006, p. 171.
  • a further development of C0 2 -curing by a subsequent flushing with air is disclosed in DE 102012103705.1.
  • the ester cure is e.g. from GB 1029057 known (so-called no-bake method).
  • the thermal curing of water glass is dealt with e.g. No. 4,226,277 and EP 1802409, wherein in the latter case particulate synthetic amorphous S1O2 is added to the molding material mixture to increase the strength.
  • binders are based on phosphates and / or a combination of silicates and phosphates, wherein the curing also takes place according to the abovementioned methods.
  • these include, for example, US 5,641, 015 (phosphate binder, thermal curing), US 6,139,619 (silicate / phosphate binder, thermal curing), US 2,895,838 (silicate / phosphate binder, C0 2 -Härtung) and US 6,299,677 (Silicate / phosphate binder, ester hardening).
  • 102012103705.1 it is proposed to add in each case amorphous silicon dioxide to the molding material mixtures.
  • the role of the S1O2 is to reduce the disintegration of the cores after thermal stress, e.g. after the casting, to improve.
  • EP 1802409 B1 and DE 102012103705.1 it is explained in detail that the addition of synthetic particulate amorphous S1O2 causes a significant increase in strength.
  • EP 2014392 B1 it is proposed to add to the molding material mixture, consisting of molding material, sodium hydroxide solution, binders based on alkali silicates and additives, a suspension of amorphous, spherical S1O2, the S1O2 being present in two particle size classifications. With this measure, a good flowability, high bending strength and a high curing rate should be obtained.
  • the object of the present invention is to further improve the properties of inorganic binders, in order to make them even more universally applicable and to make them an even better alternative to the currently dominant organic binders.
  • molding material mixtures which, because of further improved strengths and / or improved densification, make it possible to produce cores of complex geometry or, in the case of simpler core geometries, to reduce the amount of binder and / or shorten the curing times.
  • particulate amorphous Si0 2 as an additive, which was prepared by thermal decomposition of ZrSi0 4 to Zr0 2 and Si0 2 and substantially complete or partial removal of Zr0 2 , it is found that at identical addition amount and under identical reaction conditions surprisingly significantly improved strength and / or that the core weight is higher than when using the mentioned in EP 1802409 B1 particulate amorphous Si0 2 from other production processes.
  • Increasing the core weight with the same outer dimensions of the core leads to a reduction in gas permeability, which indicates a denser packing of the molding material particles.
  • the particulate amorphous Si0 2 prepared by the above method is also characterized by the term "artificially produced amorphous Si0 2. " The particulate amorphous Si0 2 can also be described cumulatively or alternatively by the following parameters.
  • the molding material mixture according to the invention comprises at least:
  • an inorganic binder preferably based on water glass, phosphate or a mixture of both,
  • an additive consisting of particulate amorphous SiO 2 , which is obtained by thermal decomposition of ZrSi0 4 to ZrO 2 and SiO 2 .
  • a molding material composition i.A.
  • the procedure is such that the refractory molding base material is initially charged and then the binder and the additive are added together or successively with stirring.
  • the binder is charged before the additive. It is stirred until a uniform distribution of the binder and the additive is ensured in the molding material.
  • the molding material mixture is then brought into the desired shape.
  • customary methods are used for the shaping.
  • the molding material mixture can be shot by means of a core shooting machine with the aid of compressed air into the mold.
  • Another possibility is to free-flow the molding material mixture from the mixer into the mold and to compact it there by shaking, stamping or pressing.
  • the curing of the molding material mixture takes place according to an embodiment of the invention after the hot-box process, ie it is cured by means of hot tools.
  • the hot tools preferably have a temperature of 100 to 300 ° C, more preferably of 120 ° C to 250 ° C.
  • a gas eg CO 2 or CO 2 enriched air
  • the above process (hot-box process) is preferably carried out in a core shooter.
  • the curing can also take place in that CO 2 , a CO 2 / gas mixture (eg with air) or CO 2 and a gas / gas mixture (eg air) successively (as described in detail in DE 102012103705) by the cold mold
  • the term "cold” means temperatures below 100 ° C., preferably below 50 ° C. and in particular at room temperature (eg 23 ° C.)
  • Guided gas or gas mixture may preferably be slightly heated, ie, up to a temperature of 120 ° C, preferably up to 100 ° C, particularly preferably up to 80 ° C.
  • molding base material materials customary for the production of casting molds can be used. Suitable examples are quartz, zircon or chrome ore sand, olivine, vermiculite, bauxite and chamotte. It is not necessary to use only new sands. In terms of resource conservation and to avoid landfill costs, it is even advantageous to have the highest possible proportion of regenerated
  • regenerates which are obtained by washing and subsequent drying. It is also possible to use regenerates obtained by purely mechanical treatment. In general, the regenerates can make up at least about 70% by weight of the molding base material, preferably at least about 80% by weight and more preferably at least about 90% by weight.
  • the average diameter of the molding base materials is generally between 1 001 and 600 ⁇ m, preferably between 120 ⁇ m and 550 ⁇ m, and particularly preferably between 150 ⁇ m and 500 ⁇ m.
  • the particle size can be determined, for example, by sieving according to DIN 66165 (part 2).
  • artificial molding materials can also be used as mold bases, in particular as an additive to the above molding materials but also as exclusive mold base material, such as glass beads, glass granules, the spherical ceramic mold bases known as "Cerabeads" or "Carboaccucast” or aluminum silicate microbeads (so-called ,
  • Such aluminum silicate microbubbles are marketed, for example, by Omega Minerals Germany GmbH, Norderstedt, under the name “Omega-Spheres.” Corresponding products are also available from PQ Corporation (USA) under the name “Extendospheres”.
  • the preferred proportion of the artificial molding base materials is at least about 3 wt.%, Particularly preferably at least about 5 wt.%, Particularly preferably at least about 10 wt.%, Preferably at least about 15 wt.%, Particularly preferably at least about 20% by weight, in each case based on the total amount of the refractory molding base material.
  • the molding material mixture according to the invention comprises an inorganic binder, e.g. on the basis of water glass.
  • an inorganic binder e.g. on the basis of water glass.
  • Conventional water glasses can be used as the water glass, as they have hitherto been used as binders in molding material mixtures.
  • These water glasses contain dissolved alkali silicates and can be prepared by dissolving glassy lithium, sodium and potassium silicates in water.
  • the water glasses preferably have a molar modulus Si0 2 / M 2 O in the range from 1.6 to 4.0, in particular from 2.0 to less than 3.5, where M is lithium, sodium or potassium.
  • the water glasses have a solids content in the range of 25 to 65 wt.%, Preferably from 30 to 60 wt.%. The solids content refers to the amount of Si0 2 and M 2 0 contained in the water glass.
  • the water glass-based binder between 0.5% by weight and 5% by weight of the water glass-based binder are used, preferably between 0.75% by weight and 4% by weight, particularly preferably between 1% by weight and 3, 5 wt.%, Each based on the molding material.
  • The% by weight refers to water glasses with a solids content as indicated above, i. includes the diluent.
  • the preferred phosphate glasses have a solubility in water of at least 200 g / L, preferably at least 800 g / L and contain between 30 and 80 mol% P 2 0 5 , between 20 and 70 mol% Li 2 0, Na 2 0 or K 2 0, between 0 and 30 mol% CaO, MgO or ZnO and between 0 and 15 mol% Al 2 0 3) Fe 2 0 3 or B 2 0 3 .
  • the particularly preferred composition is 58 to 72% by weight of P 2 O 5 , 28 to 42% by weight of Na 2 O and 0 to 16% by weight of CaO.
  • the phosphate anions are preferably present in the phosphate glasses as chains.
  • the phosphate glasses are usually used as about 15 to 65% strength by weight, preferably as about 25 to 60% strength by weight aqueous solutions.
  • the phosphate glass and the water can be added separately to the molding base material, with at least part of the phosphate glass dissolving in the water during the preparation of the molding material mixture.
  • Typical addition amounts of the phosphate glass solutions are from 0.5% by weight to 15% by weight, preferably from 0.75% by weight to 12% by weight, more preferably from 1% by weight to 10% by weight, based in each case on the molding base material ,
  • the term refers to phosphate glass solutions with a solids content as indicated above, ie includes the diluent.
  • the molding mixtures preferably furthermore contain hardeners which bring about the solidification of the mixtures, without the need for heat supply or for a gas to be passed through the mixture.
  • hardeners may be liquid or solid, organic or inorganic in nature.
  • Suitable organic hardeners are e.g. Esters of carbonic acid such as propylene carbonate, esters of monocarboxylic acids having 1 to 8 carbon atoms with mono-, di- or trifunctional alcohols such as ethylene glycol diacetate, glycerol mono-, di- and triacetic acid esters, and cyclic esters of carbonic acid such as propylene carbonate, esters of monocarboxylic acids having 1 to 8 carbon atoms with mono-, di- or trifunctional alcohols such as ethylene glycol diacetate, glycerol mono-, di- and triacetic acid esters, and cyclic esters of
  • Hydroxycarboxylic acids such as ⁇ -butyrolactone.
  • the esters can also be mixed with one another.
  • Suitable inorganic hardeners for waterglass-based binders are e.g. Phosphates such as Lithopix P26 (an aluminum phosphate of Fa.
  • the ratio of hardener to binder can vary depending on the desired property, eg processing time and / or breaking time of the molding material mixtures.
  • the proportion of hardener is greater than or equal to 5% by weight, preferably greater than or equal to 8% by weight, particularly preferably greater than or equal to 10% by weight, based in each case on the binder.
  • the upper limits are less than or equal to 25% by weight, based on the binder, preferably less than or equal to 20% by weight, more preferably less than or equal to 15% by weight.
  • the molding material mixtures contain a proportion of an artificially produced particulate amorphous SiO 2, which originates from the process of thermal decomposition of ZrSiO 4 to ZrO 2 and SiO 2 .
  • Corresponding products are, for example, supplied by the companies Possehl Erzharir GmbH, Doral Fused Materials Pty. Ltd., Cofermin Rohscher GmbH & Co. KG and TAM Ceramics LLC (ZrSi0 4 process).
  • FIG. 1 shows that there are more isolated particles in the SiO 2 according to the invention than in the comparison (FIG. 2). It can be seen in Fig. 2 also a stronger adhesion of individual balls to larger associations that can not be broken up into the primary particles.
  • the two figures indicate that the primary particles of the SiO 2 according to the invention have a broader particle size distribution than in the prior art, which may also contribute to the improved flowability.
  • the particle size was determined by means of dynamic light scattering on a Horiba LA 950, the scanning electron micrographs using an ultra-high resolution scanning electron microscope Nova NanoSem 230 from FEI, which was equipped with a Through The Lens Detector (TLD) for the SEM measurements were the samples dispersed in distilled water and then applied to a copper tape coated aluminum holder before the water was evaporated. In this way, details of the
  • the amorphous Si0 2 derived from the ZrSi0 process may still contain zirconium compounds, especially Zr0 2 .
  • the content of zirconium, calculated as Zr0 2 is usually below about 12% by weight, preferably below about 10% by weight, more preferably below about 8% by weight, and most preferably below about 5% by weight % and, on the other hand, greater than 0.01% by weight, greater than 0.1% by weight, or even greater than 0.2% by weight.
  • Fe 2 0 3 , Al 2 0 3 , P 2 0 5 , Hf0 2 , Ti0 2 , CaO, Na 2 0 and K 2 0 with a total content of less than about 8 wt.%, Preferably less than approx 5% by weight and more preferably less than about 3% by weight.
  • the water content of the particulate amorphous SiO 2 used according to the invention is less than 10% by weight, preferably less than 5% by weight and particularly preferably less than 2% by weight.
  • the amorphous Si0 2 is used as a pourable dry powder.
  • the powder is pourable and pourable under its own weight.
  • the average particle size of the particulate amorphous Si0 2 preferably moves between 0.05 ⁇ and 10 ⁇ , in particular between 0.1 [im and 5 [m and more preferably between 0.1 ⁇ im and 2 ⁇ , wherein by means of primary particles with diameters REM were found between about 0.01 ⁇ im and about 5 ⁇ .
  • the determination was carried out with the aid of dynamic light scattering on a Horiba LA 950.
  • the particulate amorphous silica has an average particle size of preferably less than 300 ⁇ m, preferably less than 200 ⁇ m, particularly preferably less than 100 ⁇ m.
  • the particle size can be determined by sieve analysis.
  • the sieve residue of the particulate amorphous S1O2 when passing through a 125 mesh sieve (120 mesh) is preferably not more than 10 wt%, more preferably not more than 5 wt%, and most preferably not more than 2 wt%. ,
  • the sieve residue is determined according to the machine screen method described in DIN 66165 (Part 2), wherein additionally a chain ring is used as screen aid.
  • the residue of particulate amorphous SiO 2 used in accordance with the invention passes through a sieve with a mesh size of 45 ⁇ m (325 mesh) not more than about 10% by weight, more preferably not more than about 5% by weight and very particularly preferably not more than about 2% by weight (sieving according to DIN ISO 3310).
  • a sieve with a mesh size of 45 ⁇ m (325 mesh) not more than about 10% by weight, more preferably not more than about 5% by weight and very particularly preferably not more than about 2% by weight (sieving according to DIN ISO 3310).
  • the ratio of primary particles (non-agglomerated, non-fused and unmelted particles) to the secondary particles (agglomerated, fused and / or fused particles including particles which (clearly) have no spherical shape) of the particulate amorphous SiO 2 can be determined. These images were taken using a Nova NanoSem 230 ultrahigh-scanning electron microscope from FEI equipped with a Through The Lens
  • the ratio of the primary particles to the secondary particles of the particulate amorphous S1O2 is advantageously and independently characterized as follows: a) The particles are more than 20%, preferably more than 40%, more preferably more than 60% and most preferably more than 80%, based on the total number of particles, in the form of essentially spherical primary particles, in each case in particular with the above limits in the form of spherical primary particles with diameters less than 4 pm, and more preferably less than 2 m.
  • the particles are more than 20% by volume, preferably more than 40% by volume, more preferably more than 60% by volume and most preferably more than 80% by volume, based on the cumulative volume of the particles, in the form of substantially spherical primary particles, in each case in particular with the above limit values in the form of spherical primary particles with diameters of less than 4 ⁇ m, and particularly preferably less than 2 m.
  • the calculation of the respective volumes of the individual particles as well as the cumulative volume of all particles was carried out under the assumption of a spherical symmetry present in each case for individual particles and with the aid of the diameter determined for each particle by means of SEM images.
  • the particles are more than 20 area%, preferably more than 40linin%, more preferably more than 60 area% and most preferably more than 80 area%, based on the cumulative area of the particles, in Form of substantially spherical primary particles, in each case in particular with the above limit values in the form of spherical primary particles with diameters smaller than 4 ⁇ m, and particularly preferably smaller than 2 ⁇ m.
  • the percentage detection is based on a statistical analysis of a plurality of SEM images, as shown for example in Figure 1 and Figure 2, wherein agglomeration / adhesion / fusion is / are classified as such only if the respective contours of individual adjacent spherical (intermeshing) primary particles are no longer recognizable.
  • the classification is carried out as a primary particle, even if the view does not allow an actual classification due to the two-dimensionality of the images.
  • the area only the visible particle areas are evaluated and contribute to the total.
  • Suitable particulate amorphous SiO 2 used according to the invention has a BET of less than or equal to 35 m 2 / g, preferably less than or equal to 20 m 2 / g, particularly preferably less than or equal to 17 m 2 / g and particularly preferably less than or equal to 15 m 2 / g.
  • the lower limits are greater than or equal to 1 m 2 / g, preferably greater than or equal to 2 m 2 / g, particularly preferably greater than or equal to 3 m 2 / g and particularly preferably greater than or equal to 4 m 2 / g.
  • the particulate amorphous SiO 2 are used, preferably between 0.1% by weight and 1.8% by weight and more preferably between 0.1% by weight and 1, 5 wt.%, Each based on the molding material.
  • the ratio of inorganic binder to particulate amorphous S1O2 used according to the invention can be varied within wide limits. This offers the possibility of determining the initial strengths of the cores, i. the strength immediately after removal from the mold to vary greatly without significantly affecting the ultimate strengths. This is of great interest especially in light metal casting. On the one hand, high initial strengths are desired in order to be able to easily transport the cores after their production or to assemble them into complete core packages, on the other hand, the final strengths should not be too high to avoid difficulties in core decay after casting.
  • the particulate amorphous SiO 2 is preferably present in a proportion of from 2% by weight to 60% by weight, more preferably from 3% by weight to 55% by weight. and most preferably from 4% to 50% by weight.
  • the artificially produced (particulate) amorphous S1O2 corresponds to the particulate amorphous SiO 2 according to terminology and others of the claims and is used in particular as a powder, in particular with a water content of less than 5% by weight, preferably less than 3% by weight, in particular less than 2% by weight. , (Water content determined by Karl Fischer).
  • the ignition loss (at 400 ° C.) is preferably less than 6, less than 5 or even less than 4% by weight.
  • the addition of the particulate amorphous Si0 2 used according to the invention can be carried out both before and after or mixed together with the binder addition directly to the refractory material.
  • the particulate amorphous Si0 2 used according to the invention is added directly to the refractory material in dry and in powder form after the binder addition.
  • a premix of Si0 2 is first prepared with an aqueous alkali solution, such as sodium hydroxide, and optionally the binder or a part of the binder and then added to the refractory molding material.
  • aqueous alkali solution such as sodium hydroxide
  • the binder or binder fraction which may still be present and which is not used for the premix can be added to the molding base material before or after the addition of the premix or together with it.
  • a non-inventive synthetic particulate amorphous Si0 2 in addition to the particulate amorphous Si0 2, a non-inventive synthetic particulate amorphous Si0 2 according to EP 1802409 B1, for example in a ratio of 1 to less than 1 are used.
  • inventive and non-inventive Si0 2 may be advantageous if the effect of the particulate amorphous Si0 2 is to be "attenuated.”
  • the additions of inventive and non-inventive amorphous Si0 2 to the molding material can be the strengths and / or the In the case of an inorganic binder on the basis of water glass, the molding material mixture according to the invention may comprise a phosphorus-containing compound in a further embodiment
  • Such an addition is preferred for very thin-walled sections of a casting mold and in particular for cores, since in this way the This is especially important when the molten metal encounters an oblique surface during casting and there is a strong erosion due to the high metallostatic pressure exerts effect or can lead to deformations in particular thin-walled sections of the mold.
  • Suitable phosphorus compounds do not or not significantly affect the processing time of the novel molding material mixtures.
  • An example of this is sodium hexametaphosphate. Further suitable representatives as well as their added amounts are described in detail in WO 2008/046653 and this is to that extent also made a disclosure of the present property rights.
  • the molding material mixture according to the invention contains a proportion of platelet-shaped lubricants, in particular graphite or M0S 2 .
  • the amount of added platelet-shaped lubricant, in particular graphite is preferably 0.05 wt.% To 1 wt.% Based on the molding material.
  • the platelet-shaped lubricant it is also possible to use surface-active substances, in particular surfactants, which likewise further improve the flowability of the molding material mixture according to the invention.
  • the molding material mixture according to the invention may also comprise further additives.
  • release agents can be added which facilitate the detachment of the cores from the mold.
  • Suitable release agents are, for example, calcium stearate, fatty acid esters, waxes, natural resins or special alkyd resins. If these release agents are soluble in the binder and do not separate from it even after prolonged storage, especially at low temperatures, they may already be present in the binder component, but they may also form part of the additive or as a separate component of the molding material mixture be added.
  • organic additives may be added. Suitable organic additives are for example phenol-formaldehyde resins such as novolacs, epoxy resins such as
  • Bisphenol A epoxy resins bisphenol F epoxy resins or epoxidized novolacs
  • polyols such as polyethylene or polypropylene glycols, glycerol or polyglycerol, polyolefins such as polyethylene or polypropylene, copolymers of olefins such as ethylene and / or propylene with others
  • Comonomers such as vinyl acetate or styrene and / or diene monomers such as butadiene, polyamides such as polyamide-6, polyamide-12 or polyamide-6,6, natural resins such as gum rosin, fatty acid esters such as cetyl palmitate, fatty acid amides such as
  • Ethylenediaminebisstearamide metal soaps such as stearates or oleates of divalent or trivalent metals and carbohydrates such as dextrins.
  • Carbohydrates, especially dextrins are particularly suitable.
  • Suitable carbohydrates are described in WO 2008/046651 A1.
  • the organic additives can be used both as a pure substance, as well as in admixture with various other organic and / or inorganic compounds.
  • the organic additives are preferably used in an amount of from 0.01% by weight to 1.5% by weight, more preferably from 0.05% by weight to 1.3% by weight and most preferably from 0.1% by weight to 1 % By weight added, in each case based on the molding material.
  • the molding material mixture according to the invention therefore contains a proportion of at least one silane.
  • Suitable silanes are, for example, aminosilanes, epoxysilanes, mercaptosilanes,
  • Suitable silanes are ⁇ -(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N
  • the silanes mentioned, in particular the aminosilanes can also
  • silane based on the binder
  • a suitable additives are alkali metal siliconates, for example potassium methyl siliconate, of which about 0.5% by weight to about 15% by weight, preferably about 1% by weight to about 10% by weight and particularly preferably about 1% by weight. can be used up to about 5 wt.% Based on the binder.
  • the molding material mixture comprises an organic additive, then it can be added per se at any point in time during the preparation of the molding material mixture.
  • the addition can be carried out in bulk or in the form of a solution
  • Water-soluble organic additives can be used in the form of an aqueous solution. If the organic additives are soluble in the binder and are stable in storage for several months without decomposition, they can also be dissolved in the binder and thus added together with the molding material. Water-insoluble additives may be used in the form of a dispersion or a paste. The dispersions or pastes preferably contain water as the liquid medium.
  • the molding material mixture contains silanes and / or alkali metal siliconates, they are usually added in the form that they are incorporated into the binder in advance. However, they can also be added to the molding material as a separate component.
  • Inorganic additives can also have a positive influence on the properties of the molding material mixtures according to the invention.
  • the carbonates mentioned in AFS Transactions, Vol. 88, pp 601-608 (1980) or Vol 89, pp 47-54 (1981) the moisture resistance of the cores during storage
  • Alkali borates as constituents of water glass binders are disclosed, for example, in EP 0111398.
  • Suitable inorganic additives for improving the casting surface based on BaSO 4 are described in DE 102012104934.3 and can be added to the molding material mixture as a complete or at least partial replacement of the organic additives mentioned above. Further details such as the respective amounts added are described in detail in DE 102012104934.3 and this is also made to the extent of disclosure of the present property rights.
  • the cores produced from these molding material mixtures show good disintegration after the casting, in particular in aluminum casting.
  • the use of the cores produced from the molding mixtures according to the invention is not limited to light metal casting.
  • the molds are generally suitable for casting metals. Such metals include, for example, non-ferrous metals such as brass or bronze, and ferrous metals.
  • FIG. 1 scanning electron microscope image of the particulate amorphous SiO 2 used according to the invention .
  • Fig. 2 Scanning electron microscope photograph of an amorphous non-inventive amorphous SiO 2 produced in the production of silicon / ferrosilicon
  • Quartz sand was poured into the bowl of a mixer from Hobart (model HSM 10). With stirring, the binder was then added and each intensively mixed with the sand for 1 minute.
  • the sand used, the type of binder and the respective amounts added are listed in Table 1.
  • Microsilica 971 U (Eikern AS, production process: production of silicon / ferrosilicon)
  • Microsilica white GHL DL 971 W (production process: see d)
  • Microsilica POS BW 90 LD (Possehl Erzrac GmbH, production process: production of
  • the molding material mixtures were introduced from the supply container into the mold by means of compressed air (5 bar).
  • the residence time in the hot mold for curing the mixtures was 35 seconds.
  • hot air (2 bar, 100 ° C on entering the tool) was passed through the mold during the last 20 seconds.
  • the mold was opened and the test bars removed.
  • the test specimens are used to determine the core weights using this method.
  • the flexural strengths were determined according to the following scheme:
  • the molding material mixtures were analogously 1.1.1. produced. Their compositions are listed in Tab. 3.
  • inlet channel cores were produced, which are larger and have a more complex geometry than the Georg Fischer bolts (FIG ).
  • the molding material mixtures were transferred to the storage bunker of a core shooting machine L 6.5 of Röperwerk-G manmaschinen GmbH, Viersen, DE, whose mold had been heated to 180.degree. C., and from there into the mold by means of compressed air.
  • the pressures used are listed in Tab. 4.
  • the residence time in the hot mold for curing the mixtures was 35 seconds.
  • hot air (2 bar, 150 ° C entering the tool) was passed through the mold during the last 20 seconds. The mold was opened and the test bars removed.
  • Tab.4 confirms the improved flowability of the molding material mixtures according to the invention over the prior art on the basis of a foundry practice. The positive effect is independent of the type of sand and the shooting pressure.
  • Part of a 2.1.1. prepared molding material mixture was transferred to the storage chamber of a core shooter H1 Röperwerk-G manmaschinen GmbH, Viersen, DE. The remainder of the molding compound mixture was stored in a carefully sealed vessel until the core shooter was refilled to prevent it from drying out and to prevent premature reaction with the CO 2 present in the air.
  • the molding material mixtures were shot by means of compressed air (4 bar) in a non-tempered mold provided with two engravings for round cores with a diameter of 50 mm and 50 mm in height.
  • compressed air 4 bar
  • a non-tempered mold provided with two engravings for round cores with a diameter of 50 mm and 50 mm in height.
  • C0 2 was first for 6 seconds with a CO 2 -FIUSS of 2 L / min. and then for 45 seconds compressed air at a pressure of 4 bar passed through the filled with the molding material molding tool.
  • the temperatures of both gases were about 23 ° C when entering the mold.
  • CO 2 was at a CO 2 -FIUSS of 4 L / min. passed through the filled with the molding material molding tool.
  • the temperature of the CO 2 was when entering the mold at about 23 °.
  • Tab. 7 shows the fumigation times with CO 2 .
  • Table 8 shows the fumigation times with air.
  • test specimens were removed from the mold and their compressive strengths were determined immediately after removal with a Zwick universal testing machine (Model Z 010), ie a maximum of 15 seconds.
  • compressive strengths of the test specimens were tested after 24 hours, in some cases even after 3 and 6 days of storage in a climatic chamber. With the help of a climatic cabinet (company Rubarth Apparate GmbH) consistent storage conditions could be guaranteed. Unless otherwise stated, a temperature of 23 ° C and a relative humidity of 50% was set. The values given in the tables are averages of 8 cores each.
  • the core weights were determined 24 hours after removal from the core box. The weighing was carried out on a laboratory balance with an accuracy of 0.1 g.
  • Quartz sand from Quarzwerke Frechen GmbH was filled into the bowl of a mixer from Hobart (model HSM 10). With stirring, the hardener and then the binder were then added first and each intensively mixed with the sand for 1 minute.
  • composition of the molding mixtures used to produce the test specimens is listed in Tab. 10 in parts by weight (GT).
  • Cuboid test bars with the dimensions 220 mm x 22.36 mm x 22.36 mm (so-called Georg Fischer bars) were produced for testing the molding material mixtures.
  • the molding mixture prepared by hand was introduced by hand into an 8-cavity mold and compacted by pressing with a hand plate.
  • the processing time (VZ) ie the time within which a molding material mixture can easily be densified, was determined visually. One can recognize the exceeding of the processing time by the fact that a molding material mixture no longer flows freely, but rolls off like a lump.
  • the processing times of the individual mixtures are given in Tab. 10.
  • AZ Ausschalzeitzeit
  • AZ the time after which a molding material has solidified so that it can be removed from the mold, a second part of the respective mixture by hand in a round shape of 100 mm in height and 100 mm diameter was filled and also compacted with a hand plate.
  • Microsilica 971 U (Eikern SA, production process: production of silicon / ferrosilicon)
  • test bars were placed in a Georg Fischer Strength Tester equipped with a 3-point bender, and the force was measured which resulted in breakage of the test bars.
  • the flexural strengths were determined according to the following scheme:
  • Table 11 shows the positive effects of the particulate amorphous S1O 2 used with respect to strengths and core weight during cold hardening

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  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Mold Materials And Core Materials (AREA)

Abstract

La présente invention concerne des mélanges de matière à mouler à base de liant inorganique permettant de produire des moules et des noyaux pour la coulée de métaux, lesquels mélanges sont composés d'au moins une matière de base à mouler réfractaire, d'un liant inorganique et de dioxyde de silicium amorphe en tant qu'additif. L'invention concerne également un procédé de production de moules et de noyaux mettant en oeuvre lesdits mélanges de matière à mouler.
EP13811773.4A 2012-10-19 2013-10-18 Mélanges de matière à mouler à base de liant inorganique et procédé de production de moules et de noyaux pour la coulée de métaux Active EP2908968B1 (fr)

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PL13811773T PL2908968T3 (pl) 2012-10-19 2013-10-18 Mieszaniny materiału formierskiego na bazie spoiw nieorganicznych oraz sposób wytwarzania form i rdzeni do odlewania metali

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DE102012020509.0A DE102012020509A1 (de) 2012-10-19 2012-10-19 Formstoffmischungen auf der Basis anorganischer Bindemittel und Verfahren zur Herstellung von Formen und Kerne für den Metallguss
PCT/DE2013/000610 WO2014059967A2 (fr) 2012-10-19 2013-10-18 Mélanges de matière à mouler à base de liant inorganique et procédé de production de moules et de noyaux pour la coulée de métaux

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EP21199894.3A Division EP3950168A1 (fr) 2012-10-19 2013-10-18 Melanges de matière à mouler à base de liant inorganique et procédé de production de moules et de noyaux pour la coulee de métaux

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Also Published As

Publication number Publication date
EP2908968B1 (fr) 2021-11-24
KR20150074109A (ko) 2015-07-01
ES2906237T3 (es) 2022-04-13
RU2650219C2 (ru) 2018-04-11
RU2015118399A (ru) 2016-12-10
EP3950168A1 (fr) 2022-02-09
ZA201502169B (en) 2016-01-27
CN104736270A (zh) 2015-06-24
WO2014059967A3 (fr) 2014-07-17
PL2908968T3 (pl) 2022-04-19
CN104736270B (zh) 2018-10-09
BR112015008549B1 (pt) 2019-11-19
HUE058306T2 (hu) 2022-07-28
JP6397415B2 (ja) 2018-09-26
BR112015008549A2 (pt) 2017-07-04
DE102012020509A1 (de) 2014-06-12
JP2015532209A (ja) 2015-11-09
US10092946B2 (en) 2018-10-09
MX2015004904A (es) 2015-07-21
WO2014059967A2 (fr) 2014-04-24
MX371009B (es) 2020-01-13
US20150246387A1 (en) 2015-09-03
KR102104999B1 (ko) 2020-06-01

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