EP3426709A1

EP3426709A1 - Two-component binder system for the polyurethane cold-box process

Info

Publication number: EP3426709A1
Application number: EP17712931.9A
Authority: EP
Inventors: Gérard LADÉGOURDIE; Nicolas Egeler; Jaime DÍAZ FERNÁNDEZ
Original assignee: Huettenes Albertus Chemische Werke GmbH
Current assignee: Huettenes Albertus Chemische Werke GmbH
Priority date: 2016-03-09
Filing date: 2017-03-08
Publication date: 2019-01-16
Also published as: EA201891751A1; DE102016203896A1; JP2019512396A; EA039022B1; JP7003049B2; US20190091758A1; KR20180124901A; BR112018067625A2; CN108699210B; CN108699210A; MX2018010789A; WO2017153474A1; KR102401072B1

Abstract

The invention relates to a two-component binder system for use in the polyurethane cold-box process, a mixture for curing by contact with a tertiary amine, a method for producing a feeder, a foundry mold or a foundry core, and feeders, foundry molds and foundry cores that can be produced by said method. The invention also relates to the use of a two-component binder system according to the invention or to a mixture according to the invention for binding a basic molding material or a mixture of basic molding materials in the polyurethane cold-box process.

Description

HÜTTENES-ALBERTUS Chemical Works Limited Liability Company Wiesenstraße 23, 40549 Düsseldorf

Two-component binder system for the polyurethane cold box process

The present application relates to a two-component binder system for use in the polyurethane cold-box process, a mixture for curing by contacting with a tertiary amine (wherein the term "tertiary amine" in the context of this application also includes mixtures of two or more tertiary amines ), a method for producing a feeder, a foundry mold or foundry core, and feeders, foundry molds and foundry cores that can be produced according to this method, and the use of a two-component binder system or a mixture according to the invention for bonding a molding base material or a mixture of molding base materials in the polyurethane cold box process.

In the production of feeders, foundry molds and foundry cores cold-curing two-component binder systems are often used to bond the mold base material with polyurethane formation. These binder systems consist of two components, a (usually dissolved in a solvent) polyol having at least two OH groups in the molecule (polyol component) and a (dissolved in a solvent or solvent-free) polyisocyanate having at least two isocyanate groups in the molecule (polyisocyanate -Component). The two components, which are separately added to a molding base to form a molding material mixture, react in the molded molding mixture in a polyaddition reaction to form a cured polyurethane binder. The curing takes place in the presence basic catalysts, preferably in the form of tertiary amines, which are introduced after forming the molding material mixture with a carrier gas in the mold.

The polyol component is usually a phenolic resin dissolved in a solvent, i. a condensation product of one or more (optionally substituted) phenols with one or more aldehydes (especially formaldehyde). The polyol component is therefore hereinafter referred to as phenolic resin component.

The polyisocyanate component used is a polyisocyanate having at least two isocyanate groups in the molecule in undissolved form or dissolved in a solvent. Preferred are aromatic polyisocyanates. In the case of a polyisocyanate component in the form of a solution, the concentration of the polyisocyanate is generally above 70%, based on the total weight of the polyisocyanate component.

To produce feeders, foundry cores and foundry molds by the polyurethane cold box process (also referred to as "urethane cold box process"), a molding material mixture is first prepared by mixing a granular molding base material with the two components of the above-described In this case, the proportions of the two components of the two-component binder system are preferably dimensioned such that, based on the number of OH groups, an excess of the NCO groups results Current bicomponent binder systems typically present an excess of NCO Up to 20%, based on the number of OH groups, of the total amount of binder (if appropriate, including the solvents and additives present in the binder components) in foundry cores and foundry molds is usually in the range of about 1% to 2%. based on the mass of Formgru used usually with feeders in the range of about 5% to 18% based on the other constituents of the feeder mass.

The molding material mixture is then molded. Thereafter, with short-term gassing with a tertiary amine (where the term "tertiary amine" also includes mixtures of two or more tertiary amines), the catalyst used is the curing of the molded molding material mixture in the range of 0.035% to 0.1 1%, in each case based on the mass of molding material used. Based on the mass of binder, the required amount of catalyst in the form of tertiary amine is typically 3% to 15%, depending on the type of used tertiary amine, then the feeder, the Foundry core or the foundry mold taken from the mold and used for casting of metal, for example in the engine casting.

The feeders, foundry cores or foundry molds already during the fumigation of a measurable strength (this is referred to as "initial strength" or "instantaneous strength"), which increases slowly after the end of fumigation to the final strength values. In practice, the highest possible initial strengths are desired so that the feeders, foundry cores or foundry molds can be removed as soon as possible after the fumigation of the mold and the mold is available again for a new operation available. Cold-curing two-component binder systems with polyurethane formation as described above are also used in the polyurethane no-bake process. Here, the curing takes place under the action of a liquid catalyst in the form of a solution of a tertiary amine, which is added to the molding material mixture.

Two-component binder system for use in the polyurethane cold box process are described, for example, in US Pat. No. 3,409,579, US Pat. No. 4,546,124, DE 10 2004 057 671, EP 0 771 599, EP 1 057 554 and DE 10 2010 051 567 and in the non-prepublished patent application PCT / EP2015 / 070,751th A two-component binder system for use in the polyurethane no-bake process is described, for example, in US Pat. No. 5,101,001. There is a continuing need in the foundry industry for more advanced two component binder systems for use in the polyurethane cold box process with improved processing characteristics, particularly with respect to the time during which the molding compound blended with the two binder components is formed into foundry molds prior to further processing or foundry cores can be stored despite the high reactivity of the binder system ("sand life"), and the initial strength of feeders, foundry cores or foundry molds.

This object is achieved by a two-component binder system for use in the polyurethane cold box process,

consisting of a phenolic resin component and a separate polyisocyanate component, wherein the phenolic resin component comprises an ortho-fused phenolic resole having etherified and / or unetherified terminal methylol groups and a solvent and optionally one or more additives

and

the polyisocyanate component comprises a polyisocyanate having at least two isocyanate groups per molecule and optionally a solvent and optionally one or more additives,

wherein in the polyisocyanate component the proportion of the mass of polyisocyanate is 90% or more, preferably 92% or more, more preferably 95% or more, particularly preferably 98% or more, in each case based on the total mass of the polyisocyanate component,

and wherein the stoichiometric ratio of isocyanate groups in the polyisocyanate component to hydroxy groups in the phenolic resin component is less than 1, 2, and preferably in the range of 0.5 to <1, particularly preferably in the range of 0, 7 to 0.95

in which

the phenolic resin component is free of compounds from the group of alkyl silicates and alkyl silicate oligomers

and based on the total mass of the phenolic resin component

the proportion of aromatic hydrocarbons is less than 39.43%, preferably less than 38%

and the proportion of rapeseed oil methyl ester is less than 39.43%, preferably less than 30%.

The term "hydrocarbons", according to its usual meaning in the field of chemistry, refers to organic compounds consisting only of carbon and hydrogen.

Preferably, based on the total mass of the phenolic resin component of the two-component binder according to the invention

the proportion of aromatic hydrocarbons is 35% or less, more preferably 30% or less, particularly preferably 25% or less,

and or the proportion of rapeseed oil methyl ester is 28% or less, more preferably 25% or less, particularly preferably 20% or less.

Surprisingly, it has been found that binder systems of the invention have a long sand life, and at the same time allow a high initial strength of feeders, foundry cores or foundry molds. Typically, binder systems that provide high initial reactivity of feeders, foundry cores, and foundry molds have a relatively short sand life due to their high reactivity, while relatively long sand life binder systems provide lower initial strength of feeders, foundry cores, and foundry shapes because of their lower reactivity.

In the two-component binder system according to the invention, the stoichiometric ratio of isocyanate groups in the polyisocyanate component to hydroxyl groups in the phenolic resin component is preferably in the range from 0.5 to 1.16, preferably in the range from 0.55 to 1, 1, more preferably in the range of 0.6 to 0.99, more preferably in the range of 0.7 to 0.95, particularly preferably in the range of 0.72 to 0.92, most preferably in the range of 0 , 75 to 0.9.

In the two-component binder system of the present invention, the phenolic resin component and the polyisocyanate component are separated from each other, i. they are in separate containers, because the above-described addition reaction (polyurethane formation) between the resole of the phenolic resin component and the polyisocyanate of the polyisocyanate component should occur only when both components are mixed in a molding material mixture with a molding material or a mixture of several molding materials and this molding material mixture was molded.

The phenolic resin component of the two-component binder system according to the invention contains a phenolic resin in the form of an ortho-condensed phenolic resole. "Ortho-fused phenolic resole" refers to a phenolic resin whose molecules have (a) methylene ether bridged ortho-linked aromatic rings formed from phenolic monomers and (b) ortho-positioned terminal (terminal) methylol groups "Phenolic monomers" includes both unsubstituted phenol and substituted phenols, for example cresols. The term "ortho-position" refers to the ortho-position with respect to the hydroxy group of the phenol It is not excluded that in the molecules of the present invention to be used ortho-fused phenolic resoles also linked by methylene aromatic rings (in addition to Methylene ether bridges linked aromatic rings (a)) and / or terminal hydrogen atoms in the ortho position (in addition to terminal methylol groups in ortho position (b)) are present. In the molecules of the orthocondensed phenolic resols to be used according to the invention, the ratio of methylene ether bridges to methyl bridges is at least 1, and the ratio of terminal (terminal) methylol groups in the ortho position to terminal hydrogen atoms in the ortho position is also at least 1. Such phenolic resins are also referred to as benzyl ether resins. They are obtainable by polycondensation of formaldehyde (optionally in the form of paraformaldehyde) and phenols in a molar ratio of greater than 1: 1 to 2: 1, preferably 1: 23: 1 to 1: 5: 1, catalyzed by divalent metal ions (preferably Zn ²⁺ ) in the weakly acidic medium.

The term "ortho-condensed phenolic resole", as used in the ordinary art, includes compounds as described in the textbook "Phenolic Resins: A Century of Progress" (published by: L. Pilato, published by Springer , Year of publication: 2010), in particular on page 477 of FIG. 18.22. The term likewise includes the "benzyl ether resins (ortho-phenolic resoles)" specified in VDG leaflet R 305 "Urethane cold box process" (February 1998) under 3.1.1. The term also includes the "phenol resins of the benzyl ether resin type" disclosed in EP 1 057 554 B1, see in particular paragraphs [0004] to [0006].

The ortho-condensed phenolic resole of the phenolic resin component to be used according to the invention has unetherified terminal methylol groups -CH ₂ OH and / or etherified terminal methylol groups -CH ₂ OR. In an etherified terminal methylol group, the hydrogen atom, which is bound to the oxygen atom in the unetherethered terminal methylol group -CH ₂ OH, is replaced by a radical R. In a first preferred alternative, R is an alkyl radical, ie the groups - CH ₂ OR are alkoxymethylene groups. Preference is given here to alkyl radicals having one to four carbon atoms, preferably from the group consisting of methyl, ethyl, propyl, n-butyl, i-butyl and tert-butyl. In a further preferred alternative, the radical R of the etherified terminal methylol group of the ortho-fused phenolic resole has the structure

-O-Si (OR1) _m (OR2) _n , where

R1 is selected from the group consisting of hydrogen and ethyl R 2 is a radical formed from an ortho-fused phenolic resole as described above,

Each of integers m and n is selected from the group consisting of 0, 1, 2 and 3 and m + n = 3. In this case, the ortho-fused phenolic resole of the phenolic resin component is a modified resole comprising ortho-fused phenolic resole units formed as described above which are substituted and / or linked by esters of orthosilicic acid. Such resins are preparable by reacting unreacted hydroxy groups (i.e., hydroxyl groups of the unetherified terminal methylol groups) of an ortho-fused phenolic resole with one or more esters of orthosilicic acid. Such modified resols and their preparation are described i.a. described in the patent application WO 2009/130335.

In the ortho-fused phenolic resole of the phenolic resin component of the two-component binder of the invention, the ratio of unetherified terminal methylol groups to etherified terminal methylol groups is preferably greater than 1, preferably greater than 2, more preferably greater than 4, and most preferably greater than 10. Preferably contain no etherified terminal methylol groups in the ortho-fused phenolic resole of the phenolic resin component.

Conventionally, phenolic resins having etherified terminal methylol groups in the form of alkoxymethylene groups -CH ₂ -OR, in particular having R = ethoxy or methoxy as described in US Pat. No. 4,546,124, are preferably used in two-component binder systems for use in the polyurethane cold box process, since they Give foundry cores and foundry molds particularly high strength. Phenol resins with etherified methylol groups are also preferred in practice because they have a higher solubility in non-polar solvents such as aromatic hydrocarbons. Surprisingly, however, it has been found that the objects of the present invention are better achieved when using an ortho-fused phenolic resole containing predominantly or even exclusively unetherified methylol terminal groups (as defined above).

Preferably, the phenolic resin component component of the two-component binder according to the invention comprises an ortho-fused phenolic resole having unetherified terminal methylol groups and a solvent and optionally one or more additives. The proportion of the ortho-fused phenolic resole in the phenolic resin component is preferably in the range of 30% to 50%, preferably in the range of 40% to 45%, based on the total mass of the phenolic resin component.

The phenolic resin component of the two-component binder system of the invention comprises a solvent in which the above-described orthocondensed phenolic resole is dissolved. According to the invention, the solvent comprises the phenolic resin component

no compounds from the group of alkyl silicates and alkyl silicate oligomers and

Compounds from the group of aromatic hydrocarbons only in such an amount that based on the total mass of the phenolic resin component, the proportion of aromatic hydrocarbons is less than 39.43%, preferably less than 38%

and

Rapsölmethylester only in such an amount that based on the total mass of the phenolic resin component, the proportion of aromatic hydrocarbons is less than 39.43%, preferably less than 30%.

According to the invention, the solvent of the phenolic resin component preferably comprises one or more compounds selected from the group consisting of

Dialkyl esters of C ₃ .C ₆ -dicarboxylic acids,

saturated and unsaturated fatty acid alkyl esters, preferably vegetable oil alkyl esters, preferably from the group consisting of rapeseed oil methyl ester, tall oil methyl ester, tall oil butyl ester (CAS No. 67762-63-4), lauric acid, isopropyl laurate (isopropyl laurate, CAS No .: 10233-13-3), myristate isopropyl (Isopropylmyristat CAS No .: 1 10-27-0) and myristic isobutyl ester (isobutyl mystrate (CAS NO .: 25263-97-2)

Alkylene carbonates, preferably propylene carbonate,

Cycloalkanes

cyclic formals,

aromatic hydrocarbons from the groups consisting of alkylbenzenes, alkenylbenzenes, dialkylnaphthalenes, dialkenyl-naphthalenes Substances from the group consisting of cashew nut shell oil, components of cashew nut shell oil and derivatives of cashew nut shell oil, preferably cardol, cardanol and derivatives and oligomers of these compounds.

The dialkyl esters of C ₃ -C ₆ dicarboxylic acids are preferably dimethyl esters of C ₃ -C ₆ - dicarboxylic acids, particularly preferably from the group consisting of dimethyl adipate, dimethyl glutarate, dimethyl succinate and dimethyl malonate.

However, in the group of aromatic hydrocarbons, those selected from the group consisting of dialkyl-naphthalenes and dialkenyl-naphthalenes are not preferred because of the toxicity of such compounds.

Among the fatty acid alkyl esters, plant alkyl esters are preferred for their recovery from renewable resources. Preferred plant olalkyl esters are rapeseed oil methyl ester, tall oil methyl ester, tall oil butyl ester, methyl laurate, isopropyl laurate, isopropyl myristate and isobutyl myristate. Rape oil methyl ester is currently particularly preferred.

According to the invention, more preferably, the solvent comprises or consists of the phenolic resin component

one or more compounds from the group of dialkyl esters of C ₃ .C ₆ -dicarboxylic acids,

and

one or more compounds from the group of alkylbenzenes and alkenylbenzenes

and

one or more compounds from the group of saturated and unsaturated fatty acid alkyl esters, preferably from the group of Pflanzenolalkylester.

Most preferably, the solvent comprises or consists of the phenolic resin component

several compounds from the group of dialkyl esters of C ₃ .C ₆ dicarboxylic acids, and

several compounds from the group of alkylbenzenes and alkenylbenzenes and one or more vegetable oil alkyl esters from the group consisting of rapeseed oil methyl ester, tall oil methyl ester, tall oil butyl ester, methyl lauric acid, isopropyl acrylate, isopropyl myristate and

Myristinsäureisobutylester.

Preferred is in the phenolic resin component of the two-component binder system according to the invention

the total mass of compounds from the group of aromatic hydrocarbons 5% to 35%, preferably 10% to 30%, particularly preferably 15% to 25%

and or

the total mass of compounds from the group of dialkyl esters of C ₃ -C ₆ -dicarboxylic acids 5% to 35%, preferably 10% to 30%, particularly preferably 15% to 25%,

and or

the total mass of fatty acid alkyl esters 1% to 30%, preferably 5% to 25% and particularly preferably 10 to 20%

in each case based on the total mass of the phenolic resin component.

the total mass of compounds from the group of aromatic hydrocarbons 5% to 35%, preferably 10% to 30%, particularly preferably 15% to 25% and

the total mass of compounds from the group of dialkyl esters of C ₃ -C ₆ -dicarboxylic acids 5% to 35%, preferably 10% to 30%, particularly preferably 15% to 25%, in each case based on the total mass of the phenolic resin component and

in each case based on the total mass of the phenolic resin component. Preferably, the phenolic resin component of the two-component binder according to the invention at 20 ° C has a viscosity of at most 100 mPas, preferably of at most 50 mPas, each determined according to DIN 53019-1: 2008-09.

The phenolic resin component of the two-component binder according to the invention preferably contains less than 5%, preferably less than 1% of monomers selected from the group consisting of monomeric unsubstituted phenol and monomeric substituted phenols, based on the total mass of the phenolic resin component.

A low content of the phenolic resin component of the two-component binder of monomeric unsubstituted phenol and monomeric substituted phenols of the invention is desirable

the emissions of monomeric unsubstituted phenol and monomeric substituted phenols in the processing of the two-component binder of the invention, i. in the manufacture of an article from the group consisting of feeders, foundry molds and foundry cores according to the polyurethane cold box process

to reduce the emissions of monomeric unsubstituted phenol and monomeric substituted phenols as well as benzene during casting

to minimize the content of monomeric unsubstituted phenol and monomeric substituted phenols in used sand from used feeders, foundry molds and foundry cores (characterized by the phenol index) to reliably meet safety and environmental requirements for landfill disposal, or cost of completion of landfill safety and environmental requirements.

Typically, the content of monomeric unsubstituted phenol and monomeric substituted phenols in the phenolic resin components of conventional two component binders for use in the cold box process is on the order of 4% to 10% based on the total weight of the phenolic resin component the phenolic resin component of ortho-fused phenolic resole is typically 50% to 60%, preferably 52% to 55%, based on the total weight of the phenolic resin component.

A further reduction of the content of monomeric unsubstituted phenol and monomeric substituted phenols, for example by distillation, is difficult since ortho-fused resoles are sensitive to heat. Under the influence of heat, on the one hand terminal methylol groups of the molecules of ortho-fused resoles can undergo condensation reactions with one another, on the other hand, the methylene ether bridges can break open, so that formaldehyde is split off. Both processes lead to a change in the structure of the phenolic resin. Often an unwanted increase in molecular weight is observed here. As the number of methylene ether bridges decreases and the number of methylene bridges increases, a drop in reactivity is usually associated. By rapid distillation in the lowest possible vacuum (less than 1 kPa (10 mbar), preferably less than 0.5 kPa (5 mbar)) and at the lowest possible temperatures (less than 126 ° C, preferably less than 1 10 ° C. ) can be produced with contents of monomers from the group consisting of monomeric unsubstituted phenol and monomeric substituted phenols below 2% based on the mass of the resole ortho-fused resoles, said resoles meet the requirements of the cold-box process in terms of molecular weight and reactivity , This is surprising since the viscosity increases due to the removal of monomeric unsubstituted phenol and monomeric substituted phenols, which also act as solvents, which could further complicate the distillation.

The polyisocyanate present in the polyisocyanate component of the two-component binder system according to the invention having at least two isocyanate groups per molecule is preferably selected from the group consisting of diphenylmethane diisocyanate (methylene bis (phenyl isocyanate), MDI), polymethylene polyphenyl isocyanates (polymeric MDI) and their mixtures. If desired, polymeric MDI comprises molecules having more than two isocyanate groups per molecule.

Isocyanate compounds may also be used as the polyisocyanate for the polyisocyanate component with at least two isocyanate groups per molecule, which furthermore have at least one carbodiimide group per molecule. Such isocyanate compounds are also referred to as carbodiimide-modified isocyanate compounds and are used i.a. in DE 10 2010 051 567 A1.

In a preferred alternative, the polyisocyanate component of the two-component binder system according to the invention contains no polyisocyanate in the form of isocyanate compounds having at least two isocyanate groups per molecule, which furthermore have at least one carbodiimide group per molecule.

The polyisocyanate component of the two-component binder system of the invention comprises a solvent in which the above-described Polyisocyanate is dissolved with at least two isocyanate groups per molecule, or no solvent, so that the polyisocyanate contained in the polyisocyanate component is not dissolved.

For example, the solvent of the polyisocyanate component comprises one or more compounds selected from the group consisting of

Alkyl silicates and alkyl silicate oligomers,

Dialkyl esters of C ₃ -C ₆ dicarboxylic acids,

saturated and unsaturated fatty acid alkyl esters, preferably vegetable oil alkyl esters, preferably from the group consisting of rapeseed oil methyl ester, tall oil methyl ester, tall oil butyl ester, methyl lauric acid, isopropyl acrylate,

Isopropyl myristate and isobutyl myristate,

Alkylene carbonates, preferably propylene carbonate,

Cycloalkanes

cyclic formals,

aromatic hydrocarbons, e.g. from the group consisting of alkylbenzenes, alkenylbenzenes, dialkylnaphthalenes, dialkenylnaphthalenes.

In the group of aromatic hydrocarbons, those selected from the group consisting of dialkyl-naphthalenes and dialkenyl-naphthalenes are not preferred because of the toxicity of such compounds.

Among the fatty acid alkyl esters, vegetable oil alkyl esters are preferred for their recovery from renewable resources. Preferred vegetable oil alkyl esters are rapeseed oil methyl ester, tall oil methyl ester, tall oil butyl ester, methyl lauric acid, isopropyl laurate, isopropyl myristate and isobutyl myristate. Rape oil methyl ester is currently particularly preferred.

The solvent of the polyisocyanate component of the two-component binder according to the invention preferably does not comprise any compounds from the group consisting of alkyl silicates and alkyl silicate oligomers. The polyisocyanate component of the two-component binder according to the invention particularly preferably comprises no compounds from the group consisting of alkyl silicates and alkyl silicate oligomers.

The solvent of the polyisocyanate component preferably comprises one or more compounds selected from the group of the alkylene carbonates, more preferably propylene carbonate. The solvent of the polyisocyanate component particularly preferably consists of one or more alkylene carbonates, in particular propylene carbonate. Most preferably, the solvent of the polyisocyanate component consists of propylene carbonate.

The solvent present in the polyisocyanate component in a small amount (10% or less, preferably 8% or less, more preferably 5% or less, more preferably 2% or less, in each case based on the total weight of the polyisocyanate component) essentially serves to protect the polyisocyanate from moisture. The polyisocyanate component of the two-component binder system according to the invention preferably contains only such an amount of solvent as is necessary for the reliable protection of the polyisocyanate from moisture.

Preference is given to a two-component binder system according to the invention for use in the polyurethane cold box process, wherein the phenolic resin component and / or the polyisocyanate component comprises as additive one or more substances which are selected from the group consisting of

Silanes, e.g. Aminosilanes, epoxysilanes, mercaptosilanes and ureidosilanes and chlorosilanes,

Acid chlorides, e.g. Phosphoryl chloride, phthaloyl chloride and benzene phosphorous dichloride

Hydrofluoric acid,

- methanesulfonic acid

Phosphorus-oxygen acids

Additive mixture can be prepared by reacting a premix of (av) 1, 0 to 50.0 weight percent methanesulfonic acid

(bv) one or more esters of one or more phosphorus-oxygen acids, the total amount of said esters being in the range of

5.0 to 90.0 weight percent,

and (cv) one or more silanes selected from the group consisting of aminosilanes, epoxysilanes, mercaptosilanes and ureidosilanes, the total amount of said silanes being in the range of 5.0 to 90.0 percent by weight

wherein the weight percentages are based on the total amount of the components (av), (bv) and (cv) in the premix.

For the latter additive, the proportion of water in a preferred variant is at most 0.1 percent by weight, the percentages by weight being based on the total amount of constituents (av), (bv) and (cv) in the premix. These additives essentially serve to extend the period of time during which the molding material mixture mixed with the two binder components can be stored prior to further processing into foundry molds or foundry cores despite the high reactivity of the binder system ("sand life") Additives that inhibit polyurethane formation Long sand lifetimes are needed so that a prepared batch of a molding material mixture does not become prematurely unusable The additives mentioned above are also known as "bench life extenders" and are known to the person skilled in the art from phosphoryl chloride POCl ₃ (CAS No. 10025-87-3), o-phthaloyl chloride (1,2-benzenedicarbonyl chloride, CAS No. 88-95-9) and benzene phosphorous dichloride (CAS No: 842-72-6) Other suitable additives are methanesulfonic acid and phosphorus-oxyacids, preferably from Gru ppe consisting of phosphinic acid, phosphonic acid, phosphoric acid, peroxophosphoric acid, hypodiphosphonic acid, diphosphonic acid, hypodiphosphoric acid, diphosphoric acid and peroxodiphosphoric acid. A preferred sand life-prolonging additive is an additive blend preparable by reacting a premix of the above components (av), (bv) and (cv) as described in patent application WO 2013/1 17256.

Inhibiting additives (except in the case of hydrofluoric acid) are usually added to the polyisocyanate component of the two-component binder system according to the invention. Their concentration is usually 0.01% to 2% based on the total weight of the polyisocyanate component. Hydrofluoric acid as an inhibiting additive is usually added to the phenolic resin component of the two-component binder system according to the invention. Further functions of the additives optionally contained in the phenol resin component and / or in the polyisocyanate component of the two-component binder system according to the invention are to facilitate the removal of hardened feeders, foundry cores and foundry molds from the mold and to increase the storage stability, in particular the Moisture resistance, manufactured feeders, foundry cores and foundry molds.

The skilled person, on the basis of his specialist knowledge, selects the additives in such a way that they are compatible with all constituents of the two-component binder system.

Another aspect of the present invention relates to a mixture for curing by contacting with a tertiary amine. This mixture according to the invention

(a) can be prepared by mixing the components of the two-component binder system according to the invention as defined above,

and or

(b)

an ortho-fused phenolic resole having etherified and / or unetherified terminal methylol groups,

a polyisocyanate having at least two isocyanate groups per molecule, a solvent and

optionally one or more additives

wherein in the mixture (both in case (a) and in case (b)) the stoichiometric ratio of isocyanate groups in the polyisocyanate component to hydroxy groups in the phenolic resin component is smaller than 1, 2, and preferably in the Range of 0.5 to <1, more preferably in the range of 0.7 to 0.95

in which

the mixture (both in case (a) and in case (b)) is free of compounds from the group of alkyl silicates and alkyl silicate oligomers

and based on the total mass of the mixture

the proportion of aromatic hydrocarbons is less than 27.6%, preferably less than 25% and

- The proportion of rapeseed oil methyl ester is less than 27.6%, preferably less than 25%. In the mixture according to the invention, the stoichiometric ratio of isocyanate groups in the polyisocyanate component to hydroxyl groups in the phenolic resin component is preferably in the range from 0.5 to 1.16, preferably in the range from 0.55 to 1.1, more preferably in the range from 0.6 to 0.99, more preferably in the range from 0.7 to 0.95, particularly preferably in the range from 0.72 to 0.92, very particularly preferably in the range from 0.75 to 0 , the ninth

Preferably, based on the total mass of the mixture according to the invention (as defined above)

the proportion of aromatic hydrocarbons is 22% or less, more preferably 20% or less, particularly preferably 15% or less,

and or

the proportion of rapeseed oil methyl ester is 22% or less, more preferably 20% or less, particularly preferably 15% or less.

Such a mixture according to the invention is useful for binding a masterbatch or mixture of masterbatch in the polyurethane cold box process (see below). The mixture according to the invention, in particular in its preferred embodiments, is characterized in that it gives adequate strength in feeders, foundry molds and foundry cores produced in the polyurethane cold box process with a low binder content and addition of a small amount of tertiary amine. Due to the small amounts of binder and tertiary amine, the emissions, especially of BTEX aromatics (benzene, toluene, ethylbenzene, xylene), and the odor burden are limited. Compared to the prior art smaller ratio of polyisocyanate in the polyisocyanate component to ortho-condensed phenolic resole with etherified and / or unetherified methylol groups in the phenolic resin component of the nitrogen content of the binder is reduced. In addition to the low binder content of the feeders, foundry molds and foundry cores according to the invention, this also limits the emission of odorous emissions by nitrogen-containing compounds and their decomposition products during casting, as well as a reduced risk of nitrogen-induced casting defects, e.g. pinhole error or comma error.

Variant (a) of the mixture according to the invention as described above is preferably preparable by mixing the components of one of the above-described preferred two-component binder systems according to the invention. For variant (b) of the mixture according to the invention as described above, the above statements apply with regard to preferably used ortho-fused phenolic resoles, polyisocyanates, solvents, additives and mixing ratios.

A further aspect of the present invention relates to a mixture as defined above, further comprising a molding base material or a mixture of several molding base materials, wherein the ratio of the total mass of molding base materials to the total mass of other components of the mixture in the range of 100: 2 to 100: 0.4, preferably from 100: 1, 5 to 100: 0.6. The other constituents of the mixture comprise all constituents of the mixture which are not molding materials, in particular all components of the two-component binder according to the invention, i. ortho-fused phenolic resole, polyisocyanate, solvent and optionally additives as defined above. Such a mixture according to the invention can be used as a molding material mixture for producing a foundry mold or a foundry core according to the polyurethane-cold-box process. This mixture according to the invention, especially in its preferred embodiments, is characterized in that produced foundry molds and foundry cores have sufficient strength at a low binder content and with a small amount of tertiary amine necessary for curing. Due to the small amounts of binder and tertiary amine, the emissions, in particular of BTEX aromatics, and the odor pollution are limited. Compared to the prior art smaller ratio of polyisocyanate in the polyisocyanate component to ortho-condensed phenolic resole with etherified and / or unetherified methylol groups in the phenolic resin component of the nitrogen content of the binder is reduced. In addition to the low binder content of the feeders, foundry molds and foundry cores according to the invention, this results in a limitation of the odorous emissions of nitrogen-containing compounds and their decomposition products during casting as well as a reduced risk of casting errors caused by nitrogen, such as e.g. pinhole error or comma error.

Suitable mold bases are all customary mold bases used for the production of feeders, foundry molds and foundry cores, for example quartz sand and special sands. The term special sand includes natural mineral sands as well as sintered and melted products, which are produced in granular form or transformed into granular form by crushing, grinding and classifying processes, or inorganic mineral sands formed by other physicochemical processes, which are used as molding bases be used with foundry usual binders for the production of feeders, cores and molds. Special sands include

Aluminum silicates in the form of natural minerals or mineral mixtures such as J-sand and Kerphalite KF,

Aluminum silicates in the form of technical sintered ceramics such as e.g. Chamotte and cerabeads,

natural heavy minerals such as R-sand, chromite sand and zircon sand,

technical oxide ceramics such as M-sand and bauxite sand,

and non-oxide technical ceramics such as silicon carbide.

A molding material mixture according to the invention which is suitable for producing a feeder according to the polyurethane cold box process, i. a feeder mass according to the invention

(i) a mixture according to the invention which

or

(b) an ortho-fused phenolic resole having etherified and / or unetherified terminal methylol groups,

optionally comprising one or more additives

wherein in the mixture (both in case (a) and in case (b)) the stoichiometric ratio of isocyanate groups in the polyisocyanate component to hydroxy groups in the phenol resin component is smaller than 1, 2, and is preferably in the range of 0.5 to <1, more preferably in the range of 0.7 to 0.95

wherein the mixture (both in case (a) and in case (b)) is free of compounds from the group of alkyl silicates and alkyl silicate oligomers.

and based on the total mass of the mixture

the proportion of aromatic hydrocarbons is less than 27.6%, preferably less than 25% and the proportion of rapeseed oil methyl ester is less than 27.6%, preferably less than 25%.

(ii) conventional feeder components,

wherein in the feed mass, the ratio of the total mass of the usual feed constituents to the total mass of the mixture according to the invention in the range of 100: 18 to 100: 5. The feeder components comprise refractory granular fillers, optionally insulating fillers such as hollow microspheres, optionally fiber material, and in the case of exothermic feeders an oxidizable metal and an oxidizing agent for the oxidizable metal. The preparation of feeders by the polyurethane cold-box method and materials suitable as feed components are known to the person skilled in the art, see e.g. WO 2008/1 13765 and DE 10 2012 200 967.

In the feed mass according to the invention, the stoichiometric ratio of isocyanate groups in the polyisocyanate component to hydroxyl groups in the phenolic resin component is preferably in the range from 0.5 to 1.16, preferably in the range from 0.55 to 1.1, more preferably in the range of 0.6 to 0.99, more preferably in the range of 0.7 to 0.95, more preferably in the range of 0.72 to 0.92, most preferably in the range of 0.75 to 0 , the ninth

A further aspect of the present invention relates to a process for producing a feeder, a foundry mold or a foundry core from a molding material mixture, wherein the molding material mixture is bound by means of a two-component binder system according to the invention as defined above or by means of a mixture according to the invention as defined above. With regard to preferred features and embodiments of the two-component binder system according to the invention and the mixture according to the invention, the above statements apply. The molding material mixture to be used in the process according to the invention comprises a molding base material or a mixture of a plurality of molding base materials or, for the production of a feeder, the above-mentioned feeder components. In the production of a feeder, a foundry mold or a foundry core from this molding material mixture of the molding material or the mixture of several molding materials by means of the present invention contained in the molding mixture two-component binder system as defined above or bound by means of the mixture contained in the molding mixture according to the invention as defined above , As mold base, all mold bases commonly used for the production of feeders, foundry molds and foundry cores are suitable as indicated above. The method according to the invention comprises the following steps

Providing or producing a molding base material or a mixture of several molding base materials,

Mixing the masterbatch or the mixture of several masterbatches with the phenolic resin component and the polyisocyanate component of a two-component binder system according to the invention (as defined above), such that one for hardening by contact with a gaseous tertiary amine or with a mixture of two or more formed in the molding material mixture, the stoichiometric ratio of isocyanate groups in the polyisocyanate component to hydroxy groups in the phenolic resin component is less than 1, 2, and preferably in the range of 0.5 to < 1, more preferably in the range of 0.7 to 0.95

Forms of the molding material mixture

and

Contacting the shaped molding material mixture with a tertiary amine or a mixture of two or more gaseous tertiary amines according to the polyurethane cold-box process so that the shaped molding mixture is cured to form the feeder, the foundry mold or the foundry core.

In the molding material mixture formed in the process according to the invention, the stoichiometric ratio of isocyanate groups in the polyisocyanate component to hydroxyl groups in the phenol resin component is preferably in the range of 0.5 to 1.16, preferably in the range of 0.55 to 1 , 1, more preferably in the range of 0.6 to 0.99, more preferably in the range of 0.7 to 0.95, particularly preferably in the range of 0.72 to 0.92, most preferably in the range of 0, 75 to 0.9.

The forming of the molding material mixture is usually carried out by the molding material mixture is filled in a mold, blown or shot and then optionally compressed.

The contacting of the shaped molding material mixture with a tertiary amine (wherein the term "tertiary amine" in the context of this application also includes mixtures of two or more tertiary amines) is preferably carried out according to the polyurethane cold box process. The tertiary amine is preferably selected from the group consisting of triethylamine, dimethylethylamine, diethylmethylamine, dimethylisopropylamine, dimethylpropylamine and mixtures thereof. The tertiary amines to be used are liquid at room temperature and are evaporated by heat supply for use in the polyurethane cold box process, and the vaporized tertiary amine is sprayed or injected into the mold.

Surprisingly, it has been shown that in preferred variants of the process according to the invention, an amount of tertiary amine less than 0.08 mol, preferably less than 0.05 mol, particularly preferably less than 0.035 mol, per mol of isocyanate groups of the polyisocyanate component of the polyisocyanate binder system of the invention contained polyisocyanate sufficient is to cure the shaped molding material mixture and thus form the feeder, the foundry mold or the foundry core. The reduction of the required amounts of tertiary amine is advantageous not only because of the lower odor load and the reduced cost due to the lower cost of materials, but also because of the correspondingly lower cost for the separation and recycling of tertiary amines.

Surprisingly, it has been found that this small amount of gaseous tertiary amine per mole of isocyanate groups of the polyisocyanate contained in the polyisocyanate component of the two-component binder system according to the invention is sufficient to cure the molded molding material mixture and thus form the feeder, the foundry mold or the foundry core ,

The process according to the invention, in particular in its preferred embodiments, is characterized in that it allows the production of feeders, foundry molds and foundry cores with a low binder content and addition of a small amount of tertiary amine, without compromising the strength of the feeders, foundry molds and foundry cores , The small amounts of binder and tertiary amine, the emissions, especially of BTEX aromatics, and the odor pollution are limited. Compared to the prior art smaller ratio of polyisocyanate in the polyisocyanate component to ortho-condensed phenolic resole with etherified and / or unetherified methylol groups in the phenolic resin component of the nitrogen content of the binder is reduced. This causes - in addition to the low binder content of feeders according to the invention, foundry molds and foundry cores - a limitation of the odoriferous emissions of nitrogen compounds during casting and a reduced risk of nitrogen-induced casting errors, such as pinhole error or comma error. Another aspect of the present invention relates to an article from the group consisting of feeders, foundry molds and foundry cores, preparable according to the inventive method described above. With regard to preferred embodiments of the method according to the invention, the above statements apply. The feeders, foundry molds or foundry cores according to the invention are characterized by a high strength at low binder content based on the total mass of the feeder, the foundry core or the foundry mold.

A further aspect of the present invention relates to the use of a two-component binder system according to the invention as defined above or a mixture according to the invention as defined above for binding a molding base material or a mixture of molding base materials in the polyurethane cold box process. With regard to preferred features and embodiments of the two-component binder system according to the invention and the mixture according to the invention, the above statements apply. The invention will be explained below with reference to embodiments and comparative examples.

From molding material mixtures comprising a conventional mixture of molding materials and a two-component binder system comprising a polyisocyanate component and a phenolic resin component as described below are prepared in the cold box process test specimens in the form of bending bars and determines their initial bending strengths.

The production of the test specimens (+ GF + bending strength standard specimens) is carried out in accordance with VDG leaflet P73. For this purpose, the molding material is presented in a mixing container. The phenolic resin component and polyisocyanate component (amounts see Table 1) are then weighed in the mixing container so that they do not mix directly. Subsequently, the base molding material, phenolic resin component and polyisocyanate component are mixed in a paddle mixer (Multiserw, model RN10 / P) for 2 minutes at about 220 revolutions / minute to form a molding material mixture.

The test specimens are produced using a universal core shooting machine LUT, which is equipped with a gasoman LUT / G, both from the company Multiserw. The finished molding material mixture is filled directly after its preparation described above in the shooting head of Kernschießmaschine or initially stored for one hour in a sealed container. The parameters of the core shooting process are as follows: shot time: 3 seconds, delay time after shot: 5 seconds, shooting pressure: 4 bar (400 kPa). For curing, the test specimens are gassed for 10 seconds at a gassing pressure of 2 bar (200 kPa) with dimethylpropylamine (DMPA). It is then purged with air at a purge pressure of 4 bar (400 kPa) for 9 seconds. The flexural strength is measured with a LRu-2e Multiserw tester at specific times (15 seconds, one hour, 24 hours, see Table 2) after the end of the rinse.

During the production of the test specimens the following parameters were varied:

Solvent content and solvent composition of the phenolic resin component

Solvent content and solvent composition of the polyisocyanate component

contained additives

Ratio of the weight of polyisocyanate in the polyisocyanate component to the mass of resole in the phenolic resin component

Storage life of the molding material mixture.

The compositions of the two-component binder systems and molding material mixtures used are listed in Table 1.

The phenolic resin component comprises a resol having unetherified terminal methylol groups, ie, terminal groups of structure -CH ₂ OH, and a solvent comprising the constituents

LM1 dimethyl ester of C ₄ -C ₆ dicarboxylic acids

LM2 mixture of aromatic hydrocarbons

LM3 Rapeseed Oil Methyl Ester The phenolic resin component of Examples 1.1 and 2.1 contains as additives a silane and 40% hydrofluoric acid (the sand life-prolonging additive). In the other examples, the phenolic resin component contains no additives.

The polyisocyanate component contains diphenylmethane diisocyanate (methylenebis (phenyl) isocyanate), MDI) as the polyisocyanate, as well as a sand life-prolonging additive and, as solvent, a mixture of aromatic hydrocarbons. The polyisocyanate component of Examples 1.1, 1.2 and 1.3 contains, as the sand life-prolonging additive, an additive mixture preparable by reacting a premix of the abovementioned components (av), (bv) and (cv) as described in the patent application WO 2013/1 17256 in an amount of 1, 2%, based on the total weight of the polyisocyanate component (Example 1 .1) or 1, 4%, based on the total weight of the polyisocyanate component (Examples 1 .2 and 1.3). The polyisocyanate component of Examples 2.1, 2.2 and 2.3 contains as the sand life-prolonging additive phosphorus oxychloride in an amount of 0.3%, based on the total weight of the polyisocyanate component. In Examples 1.1 and 2.1, which are not according to the invention, the two components of the binder system were each used in a quantity and composition customary in the prior art, these examples therefore serve as a reference. In the examples according to the invention, the solvent content of the polyisocyanate component is reduced compared to the reference example and the solvent content of the phenolic resin component is increased compared to the reference example. In all the examples according to the invention, the stoichiometric ratio of isocyanate groups in the polyisocyanate component to hydroxyl groups in the phenolic resin component is less than 1.2, in examples 1.3 and 2.3 even less than 1.

In Table 1, mean:

GT parts by weight

FGS molding material

LM solvent

BM binder (less solvent and additives).

The results of the measurements of the flexural strength as a function of the storage period of the molding material mixture preceding the core production and the time elapsed after the end of the rinsing are summarized in Table 2. The flexural strength values measured at 15 seconds after the end of the rinse are critical to the usefulness of cores and are referred to herein as initial strengths. Table 1

composition

Composition phenolic resin polyisocyanate composition molding material mixture

component

At GT GT

Fabric game phenol-polyiso-Mas- Stoff¬

GT GT Amount Stof No. Addiharz cyanate GT amount

Resol LM1 LM2 LM3 MDI LM Additive Resole / MDI / [mol] Multi-component Compo- Compo- BMI 100 [mol] OH /

[%] [%] [%] [%] [%] [%] ve [%] 100 GT 100 GT NCO / reg

[%] nents / ns MDI GT FGS 100 GT

FGS FGS 100 GT NCO / 100 GT 100 GT / Resol FGS

FGS

FGS FGS

1.1 50.83 17.1 18.63 12.99 0.45 85 13.8 1.2 0.75 0.75 0.38 0.64 1.680 1.02 0.00359 0.00483 1.345

1.2 47 20 20 13 0 95 3.6 4.6 0.9 0.6 0.40 0.57 1.439 0.97 0.00374 0.00431 1.152

1.3 44 21 21 14 0 95 3.6 1.4 1 0.5 0.44 0.48 1.080 0.88 0.00416 0.00360 0.864

2.1 50.83 17.1 18.63 12.99 0.45 85 14.7 0.3 0.75 0.75 0.38 0.64 1.680 1.02 0.00359 0.00483 1.345

2.2 47 20 20 13 0 95 4.3 4.3 0.7 0.9 0.6 0.40 0.57 1.439 0.97 0.00374 0.00431 1.152

2.3 44 21 21 14 0 95 4.3 0.7 1 0.5 0.44 0.48 1.080 0.88 0.00416 0.00360 0.864

Table 2

In the examples with a binder system according to the invention (1.2, 1.3, 2.2, 2.3) higher initial flexural strengths are achieved, although the binder content (without solvent and additives) of the molding material mixture is lower here than in the reference examples. That the flexural strengths in the examples according to the invention are lower after one hour or after 24 h than in some reference examples is of secondary importance in practice. On the other hand, it is crucial for partially and fully automated core manufacturing companies that the initial strengths are high in order to avoid breakage of the cores during handling.

Surprisingly, the molding material mixtures according to the invention, regardless of the additive used, a higher storage stability than in the reference examples. This can be seen from the fact that the flexural strengths of test specimens, produced from a molded material mixture according to the invention stored for one hour in a closed container, do not fall off relative to the corresponding flexural strengths of the cores which were produced from the freshly prepared molding material mixture according to the invention.

Claims

claims

1. two-component binder system for use in the polyurethane cold box process,

consisting of a phenolic resin component and a separate polyisocyanate component, wherein

the phenolic resin component comprises an ortho-fused phenolic resole having etherified and / or unetherified terminal methylol groups and a solvent and optionally one or more additives

and

wherein in the polyisocyanate component the proportion of the mass of polyisocyanate is 90% or more, preferably 92% or more, more preferably 95% or more, particularly preferably 98% or more, each based on the total weight of the polyisocyanate component,

in which

and based on the total mass of the phenolic resin component

2. Two-component binder system of claim 1, wherein

the ratio of unetherified terminal methylol groups to etherified terminal methylol groups in the ortho-fused phenolic resole is greater than 1, preferably greater than 2, preferably greater than 4, and particularly preferred zugt greater than 10, wherein preferably no etherified methylol groups are contained in the ortho-condensed phenolic resole,

and or

the polyisocyanate having at least two isocyanate groups per molecule is selected from the group consisting of diphenylmethane diisocyanate, polymethylene-polyphenyl isocyanates (polymeric MDI) and mixtures thereof.

The bicomponent binder system of any one of the preceding claims wherein the phenol resin component solvent comprises one or more compounds selected from the group consisting of

Dialkyl esters of C ₃ .C ₆ -dicarboxylic acids,

saturated and unsaturated fatty acid alkyl esters, preferably vegetable oil alkyl esters, preferably from the group consisting of rapeseed oil methyl ester, tall oil methyl ester, tall oil butyl ester, methyl lauric acid,

Isopropyl acrylate, isopropyl myristate and

Myristinsäureisobutylester,

Alkylene carbonates, preferably propylene carbonate,

Cycloalkanes

cyclic formals,

Aromatic hydrocarbons selected from the group consisting of alkylbenzenes, alkenylbenzenes, dialkylnaphthalenes, dialkenylnaphthalenes,

Substances from the group consisting of cashew nut shell oil, components of cashew nut shell oil and derivatives of cashew nut shell oil, preferably cardol, cardanol and derivatives and oligomers of these compounds.

A bicomponent binder system according to any one of the preceding claims, wherein the solvent of the phenolic resin component comprises:

one or more compounds from the group of alkylbenzenes and alkenylbenzenes

and one or more compounds from the group of saturated and unsaturated fatty acid alkyl esters, preferably vegetable oil alkyl esters, be preferably from the group consisting of rapeseed oil methyl ester, tall oil methyl ester, tall oil butyl ester, methyl lauric acid,

Isopropyl acrylate, isopropyl myristate and

Myristinsäureisobutylester.

A bicomponent binder system according to any one of the preceding claims, wherein the phenolic resin component

at 20 ° C has a viscosity of at most 100 mPas, preferably of at most 50 mPas, each determined according to DIN 53019-1: 2008-09 and / or

less than 5%, preferably less than 1%, of monomers selected from the group consisting of monomeric unsubstituted phenol and monomeric substituted phenols, based on the total mass of the phenolic resin component.

The bicomponent binder system of any one of the preceding claims, wherein the solvent of the polyisocyanate component comprises one or more compounds selected from the group consisting of

Dialkyl esters of C ₃ -C ₆ dicarboxylic acids,

Isopropyl isopropylate, isopropyl myristate, and

Myristinsäureisobutylester,

Alkylene carbonates, preferably propylene carbonate,

Cycloalkanes

cyclic formals,

aromatic hydrocarbons selected from the group consisting of alkylbenzenes, alkenylbenzenes, dialkylnaphthalenes, dialkenylnaphthalenes.

Two-component binder system according to one of the preceding claims, wherein the phenolic resin component and / or the polyisocyanate component as an additive comprises one or more substances selected from the group consisting of

silanes Acid chlorides,

Hydrofluoric acid,

methane

Phosphorus-oxygen acids

Additive mixture can be prepared by reacting a premix of (av) 1, 0 to 50.0 wt .-% methanesulfonic acid

(bv) one or more esters of one or more phosphorus-oxygen acids, the total amount of said esters being in the range of 5.0 to 90.0% by weight,

and

(cv) one or more silanes selected from the group consisting of aminosilanes, epoxysilanes, mercaptosilanes and ureidosilanes, the total amount of said silanes being in the range of 5.0 to 90.0% by weight,

wherein the proportion of water is at most 0, 1 wt .-%,

in each case based on the total amount of constituents (av), (bv) and (cv) in the premix.

Mixture for curing by contacting with a tertiary amine or with a mixture of two or more tertiary amines, wherein the mixture

(a) can be prepared by mixing the components of the two-component binder system according to one of claims 1 to 7,

and or

optionally one or more additives

includes

and wherein the stoichiometric ratio of isocyanate groups in the polyisocyanate component to hydroxy groups in the phenolic resin component is less than 1, 2, and preferably in the range of 0.5 to <1, more preferably in the range of 0.7 to 0.95

wherein the mixture is free of compounds from the group of alkyl silicates and alkyl silicate oligomers

and based on the total mass of the mixture

the proportion of rapeseed oil methyl ester is less than 27.6%, preferably less than 25%.

A mixture according to claim 8, further comprising a masterbatch or a mixture of several masterbatch, wherein the ratio of the total mass of masterbatch to the total mass of other components of the mixture is in the range of 100: 2 to 100: 0.4, preferably 100: 1, 5 to 100: 0.6 is.

Method for producing an article from the group comprising feeders, foundry molds and foundry cores, comprising the steps of:

Mixing the molding material or the mixture of several molding materials with the phenolic resin component and the polyisocyanate component of a two-component binder system according to any one of claims 1 to 7, so that one for curing by contacting with a gaseous tertiary amine or with a mixture of two or formed in the molding material mixture, the stoichiometric ratio of isocyanate groups in the polyisocyanate component to hydroxy groups in the phenolic resin component is less than 1, 2, and preferably in the range of 0.5 to <1, more preferably in the range of 0.7 to 0.95

Forms of the molding material mixture

and contacting the shaped molding material mixture with a gaseous tertiary amine or a mixture of two or more gaseous tertiary amines according to the polyurethane cold box process so as to cure the shaped molding compound and thus the article of the group consisting of feeders, foundry molds and foundry cores is formed, wherein preferably a total amount of gaseous tertiary amines is used which is less than 0.08 mol, preferably less than 0.05 mol per 1 mol of isocyanate groups.

1 1. Article from the group consisting of feeders, foundry molds and foundries, producible according to a method according to claim 10.

12. Use of a two-component binder system according to any one of claims 1 to 7 or a mixture according to claim 8 for binding a molding material or a mixture of molding materials in the polyurethane cold box process.