Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G59/00—Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
  • C08G59/18—Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
  • C08G59/40—Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the curing agents used
  • C08G59/50—Amines
• • 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
  • B22C9/123—Gas-hardening
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
  • B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
  • B01J31/0234—Nitrogen-, phosphorus-, arsenic- or antimony-containing compounds
  • B01J31/0235—Nitrogen containing compounds
  • B01J31/0237—Amines
• • 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
  • B22C1/02—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by additives for special purposes, e.g. indicators, breakdown additives
  • B22C1/10—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by additives for special purposes, e.g. indicators, breakdown additives for influencing the hardening tendency of the mould material
• • 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
• • 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
  • B22C1/162—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 use of a gaseous treating agent for hardening the binder
• • 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
  • B22C1/20—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 organic agents
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22C—FOUNDRY MOULDING
  • B22C9/00—Moulds or cores; Moulding processes
  • B22C9/10—Cores; Manufacture or installation of cores
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D15/00—Casting using a mould or core of which a part significant to the process is of high thermal conductivity, e.g. chill casting; Moulds or accessories specially adapted therefor
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D29/00—Removing castings from moulds, not restricted to casting processes covered by a single main group; Removing cores; Handling ingots

Definitions

• This invention relates to the use of amine blends as curing agents for binder compositions useful in the foundry art for making cores that harden at room temperature. It also relates to combinations of foundry aggregates, such as sand and binder, generally based on phenolic (phenol aldehyde) resins and poly-isocyanates, which, on being formed into a coherent mass with the aggregate in a mould, generally a steel mould, is capable of being cured at room temperature by an amine blend used as curing agent.
• the self-supported cores as obtained can be used in making metal castings.
• a two-component polyurethane binder system is used for the bonding of sand.
• the first component consists in a solution of at least one polyol, generally comprising at least two OH groups per molecule.
• the second component is a solution of at least one isocyanate having at least two NCO groups per molecule.
• tertiary amines as curing agents has long been known in PUCB: see for example U.S. Pat. No. 3,429,848; U.S. Pat. No. 3,485,797; U.S. Pat. No. 3,676,392; and U.S. Pat. No. 3,432,457.
• Such tertiary amines are sometimes utilized with metal salts and provide a fast curing of phenol formaldehyde and poly-isocyanate resins at room temperature. They can be added to the binder system before the moulding stage, in order to bring the two components to reaction (U.S. Pat. No. 3,676,392) or they can pass in a gaseous form through a shaped mixture of an aggregate and the binder (U.S. Pat. No. 3,409,579).
• phenolic resins are used as polyols, which are prepared through condensation of phenol with aldehydes, preferably formaldehyde, in the liquid phase, at temperatures of up to around 130° C., in the presence of divalent metal catalysts.
• aldehydes preferably formaldehyde
• divalent metal catalysts The manufacture of such phenolic resins is described in detail in U.S. Pat. No. 3,485,797.
• substituted phenols especially o-cresol and p-nonylphenol, can be used (see for example EP-A-0 183 782).
• alkoxylated phenolic resins As additional reaction components, according to EP-B-0 177 871, aliphatic monoalcohols with one to eight carbon atoms can be used to prepare alkoxylated phenolic resins. According to this patent, the use of alkoxylated phenolic resins in the binder results in binders that have a higher thermal stability.
• solvents for the phenolic components mixtures of high-boiling point polar solvents (for example, esters and ketones) and high boiling point aromatic hydrocarbons are typically used.
• Preferred tertiary amines used in curing polyurethane cold box (PUCB) processes are trimethyl amine (TMA), dimethyl ethyl amine (DMEA), dimethyl iso-propylamine (DMIPA), dimethyl-n-propylamine (DMPA) and triethyl amine (TEA). All these tertiary amines are taught in the art to be used individually.
• the catalyst is usually introduced as a combination of one inert gas and one amine, in the liquid or gaseous state.
• the boiling point of the amine is preferably below 100° C. to permit evaporation and to achieve satisfactory concentration of amine in the amine-inert gas mixture injected into the steel mould.
• a boiling point below 100° C. also helps to avoid condensation of the amine when it contacts the steel moulds.
• the boiling point of the amine must be preferably high enough to facilitate handling of the amine.
• Trimethylamine (TMA) is a gas at normal ambient temperature (boiling point (Bp) 2.87° C.), which makes it difficult to handle.
• Bp ambient temperature
• TEA triethylamine
• the molecular weight of the amine must be low enough to permit ready diffusion of the amine through sand in the steel mould, especially in the corners and edges of the mold.
• TEA with molecular weight of 101, is probably the highest molecular weight amine permissible for the so-called Cold Process; it has a very low odor intensity and very low amine smell but displays lower curing ability than the tertiary amines with lower molecular weights (Mw) and boiling points.
• tertiary amines containing 5 carbon atoms such as DMIPA (Mw 87, Bp 67° C.) or DMPA (Mw 87, Bp 65-68° C.) or DEMA (Mw 87, Bp 65° C.) constitute good compromise tertiary amines in the field of catalytic gassing agents for curing resins in cold box processes.
• Tertiary amines containing 5 carbon atoms require less energy input and lower gassing temperatures in PUCB equipment than TEA.
• DMIPA has a better reactivity than TEA: 1 kg of DMIPA is capable of curing approximately 1200 kg of sand/resin mixture, whereas 1 kg of TEA is capable of curing only 900 kg of the same sand/resin mixture. DMIPA is less odorant than the lighter tertiary amine DMEA.
• the present invention therefore relates to a new type of amine catalyst for cold box processes, said catalyst allowing a modulation of reactivity and safer and easier handling during use.
• the present invention first relates to the use of a blend of at least two tertiary amines as catalyst for curing a composite resin composition, especially for preparing a foundry shape by the said cold box process.
• the use of the present invention has many advantages, among other a lower amount of the used curing blend of amines as compared to the amount theoretically expected, and allows a modulation of both properties of curing kinetics and safer handling and storage (less odorant and less flammable catalyst), as compared to the known catalysts used in the art, which only consist in one single amine.
• the curing catalyst system used in the present invention is a blend of at least two tertiary amines, each displaying curing reactivity and/or odor difference from one another.
• the blends of amines used in the invention allow a modulation in reactivity.
• the blend does not contain two C5 tertiary amines.
• two C 5 tertiary amines mixed with one or more C 3 , C4 and/or C 6 -C 10 amines are encompassed in the present invention.
• the blend comprises from 10 to 90 parts by weight of any of the amines present in the catalytic mixture.
• each amine is present in the blend in an amount of not less than 10% by weight, and not more than 90% by weight.
• the blend according to the use of the present invention is preferably a mixture of at least one tertiary amine having 3 to 5 carbon atoms with at least one tertiary amine having 6 to 10 carbons.
• Each tertiary amine generally is a trialkylamine, each alkyl group being linear, branched or cyclic, and two alkyl groups possibly forming, together with the nitrogen atom to which they are bonded, a cyclic group containing 2 to 9 carbon atoms, preferably 2 to 6 carbon atoms.
• the invention does not exclude tertiary amines that contain a second, third or even fourth tertiary nitrogen atom.
• the tertiary amines used in the invention may be substituted with functional groups, which do not interfere in the catalytic action of the tertiary amines.
• substitution functional groups of the tertiary amines mention may be made for example of hydroxyl groups, alkoxy groups, amino and alkyl amino groups, ketoxy groups, thio groups, silyl groups and the like.
• tertiary amines used in the present invention are known, commercially available compounds, or may be easily prepared according to known processes, or directly or indirectly from processes disclosed in the scientific literature, patents, in the Chemical Abstracts or on the Internet.
• the blends comprise at least one amine having a low molecular weight with at least one amine of higher molecular weight.
• preferred blends comprise at least one amine having a low boiling point with at least one amine of higher boiling point.
• preferred blends comprise at least one fast curing tertiary amine with at least one less reactive tertiary amine.
• preferred blends comprise at least a fast curing tertiary amine having a low molecular weight and a low boiling point with at least a less reactive tertiary amine of higher molecular weight and higher boiling point.
• curing of polyurethane binder is less odorant and safer to handle and store, than when a fast curing amine is applied alone, and faster and more complete than with the use of a high boiling tertiary amine alone.
• Examples of C 3 -C 6 amines that can be used in the present invention comprise:
• Preferred amines for use in the blends according to the present invention are DMEA, DMIPA, DEMA, DMPA and TEA.
• Examples of preferred blends of tertiary amines for use in the present invention are: DMEA-DMIPA, DMEA-DEMA, DMEA/DMPA and DMEA-TEA.
• Preferred blends are (weight ratios): 50/50 DMEA/DMIPA, 20/80 DMEA/DMIPA, 10/90 DMEA/DMIPA, 50/50 DMEA/DMPA, 20/80 DMEA/DMPA, 10/90 DMEA/DMPA, 50/50 DMEA/DEMA, 20/80 DMEA/DEMA, 10/90 DMEA/DEMA, 50/50 DMEA/TEA, 20/80 DMEA/TEA, 10/90 DMEA/TEA, 80/20 DMEA/TEA and 90/10 DMEA/TEA, preferably 20/80 DMEA/DMIPA, 20/80 DMEA/TEA and 80/20 DMEA/TEA.
• the blend contains from 10 to 30 parts by weight of DMEA.
• Such blends lead to improved curing efficiency as compared to the performance of the highest boiling amine in the catalytic mixture for polyurethane cold box curing and for odor improvement as compared to the odor carried by the lowest boiling component, if used alone.
• blends of DMEA-DEMA and blends of DMEA-TEA display a synergy at curing; this curing synergy can be appreciated by measuring the global amount of amines blend needed for a 100% curing of a sand+binder mixture versus the theoretical amount of blend that is expected by adding the optimized volumes for each amine modulated by their abundance ratio in the blend.
• Such a behavior is particularly advantageous because it allows not only a better and immediate volatile organic compounds (VOC) reduction as compared to other curing systems which do not display such a synergy, but also presents other advantages such as a faster curing than the one obtained with a high boiling and high molecular weight tertiary amine when used as single curing catalyst, and less pungent and clothe impregnating than the one obtained with a low boiling and low molecular weight tertiary amine when used as single curing catalyst.
• VOC volatile organic compounds
• Tertiary amine blends may be used in a liquid state or preferably in a gaseous state and in any desired predetermined concentration, alone or preferably in combination with an inert carrier.
• the inert gaseous carrier can be nitrogen or air, but carbon dioxide, less expensive than nitrogen, is sometimes utilized.
• a mixture comprising, in addition to the tertiary amines blend, up to 25%, and preferably up to 10% by weight (to the total weight of all amines present in the blend) of at least one other, primary and/or secondary amine.
• the amount of primary and/or secondary amine in the amine blend is more preferably maintained at 0.5% by weight or less.
• the tertiary amine blend can also comprise small amounts of water: the concentration of water in the blend is preferably kept below 0.2% by weight.
• the present invention also relates to a process for preparing a foundry shape by the cold box process.
• This process invention has many advantages, among other a lower amount of the used curing blend of amines as compared to the amount theoretically expected, and allows a modulation of both properties of curing kinetics and safer handling and storage (less odorant and less flammable catalyst), as compared to the known catalysts used in the art, which only consist in one single amine.
• the invention thus relates to a process for preparing a foundry shape by the cold box process, which process comprises the following steps:
• the binder system comprises at least one phenolic resin component and at least one isocyanate component.
• Phenolic resins are most generally manufactured by condensation of phenols and aldehydes (Ullmann's Encyclopedia of Industrial Chemistry, Bd. A19, pages 371 ff, 5th, edition, VCH Publishing House, Weinheim). Substituted phenols and mixtures thereof can also be used. All conventionally used substituted phenols are suitable.
• the phenolic binders are preferably not substituted, either in both ortho-positions or in one ortho- and in the para-position, in order to enable the polymerization.
• the remaining ring sites may be substituted.
• substituted phenols are alkyl-substituted phenols, aryl-substituted phenols, cycloalkyl-substituted phenols, alkenyl-substituted phenols, alkoxy-substituted phenols, aryloxy-substituted phenols and halogen-substituted phenols.
• substituents have 1 to 26, and preferably 1 to 12, carbon atoms.
• suitable phenols in addition to the especially preferred unsubstituted phenols, are o-cresol, m-cresol, p-cresol, 3,5-xylol, 3,4-xylol, 3,4,5-trimethyl phenol, 3-ethylphenol, 3,5-diethylphenol, p-butylphenol, 3,5-dibutylphenol, p-amylphenol, cyclohexylphenol, p-octylphenol, 3,5-dicyclohexylphenol, p-crotylphenol, p-phenylphenol, 3,5-dimethoxyphenol, 3,4,5-trimethoxyphenol, p-ethoxyphenol, p-butoxyphenol, 3-methyl-4-methoxyphenol, and p-phenoxyphenol.
• phenol itself.
• aldehydes which are traditionally used for the manufacture of phenolic resins, can be used within the scope of the invention. Examples of these are formaldehyde, acetaldehyde, propionaldehyde, furfuraldehyde, and benzaldehyde.
• the aldehydes commonly used should have the general formula R′CHO, where R′ is hydrogen or a hydrocarbon radical with 1-8 carbon atoms.
• R′ is hydrogen or a hydrocarbon radical with 1-8 carbon atoms.
• Particularly preferred is formaldehyde, either in its diluted aqueous form or as paraformaldehyde.
• a molar ratio aldehyde to phenol of at least 1.0 should be used.
• a molar ratio of aldehyde to phenol is preferred of at least 1:1.0, with at least 1:0.58 being the most preferable.
• primary and secondary aliphatic alcohols are used, having an OH-group containing from 1 to 10 carbon atoms.
• Suitable primary or secondary alcohols include, for example, methanol, ethanol, n-propanol, isopropanol, n-butanol, and hexanol.
• Alcohols with 1 to 8 carbon atoms are preferred, in particular, methanol and butanol.
• alkoxy-modified phenolic resins are described for example in EP-B-0 177 871. They can be manufactured using either a one-step or a two-step process. With the one-step-process, the phenolic components, the aldehyde and the alcohol are brought to a reaction in the presence of suitable catalysts. With the two-step-process, an unmodified resin is first manufactured, which is subsequently treated with alcohol.
• the ratio of alcohol to phenol influences the properties of the resin as well as the speed of the reaction.
• the molar ratio of alcohol to phenol amounts to less than 0.25.
• a molar ratio of from 0.18-0.25 is most preferred. If the molar ratio of alcohol to phenol amounts to more than 0.25, the moisture resistance decreases.
• Suitable catalysts are divalent salts of Mn, Zn, Cd, Mg, Co, Ni, Fe, Pb, Ca and Ba. Zinc acetate is preferred.
• Alkoxylation leads to resins with a low viscosity.
• the resins predominantly exhibit ortho-ortho benzyl ether bridges and furthermore, in ortho- and para-position to the phenolic OH-groups, they exhibit alkoxymethylene groups with the general formula —(CH 2 O) n R.
• R is the alkyl group of the alcohol, and n is a small whole number in the range of 1 to 5.
• solvents which are conventionally used in binder systems in the field of foundry technology, can be used. It is even possible to use aromatic hydrocarbons in large quantities as essential elements in the solution, except that those solvents are not preferred because of environmental considerations. For that reason, the use of oxygen-rich, polar, organic solvents are preferred as solvents for the phenolic resin components.
• the most suitable are dicarboxylic acid ester, glycol ether ester, glycol diester, glycol diether, cyclic ketone, cyclic ester (lactone) or cyclic carbonate.
• Dicarboxylic acid ester exhibits the formula R 1 OOC—R 2 —COOR 1 , where the R 1 , independently from one another, represent an alkyl group with 1-12, and preferably 1-6 carbon atoms, and R 2 is an alkylene group with 1-4 carbon atoms.
• R 1 independently from one another, represent an alkyl group with 1-12, and preferably 1-6 carbon atoms
• R 2 is an alkylene group with 1-4 carbon atoms.
• Examples are dimethyl ester from carboxylic acids with 4 to 6 carbon atoms, which can, for example, be obtained under the name “dibasic ester” from DuPont.
• Glycol ether esters are binders with the formula R 3 —O—R 4 —OOCR 5 , where R 3 represents an alkyl group with 1-4 carbon atoms, R 4 is an alkylene group with 2-4 carbon atoms, and R 5 is an alkyl group with 1-3 carbon atoms (for example butyl glycolacetate), with glycol etheracetate being preferred.
• Glycol diesters exhibit the general formula R 5 COO—R 4 —OOCR 5 where R4 and R 5 are as defined above and the remaining R 5 are selected, independently of each other (for example, propyleneglycol diacetate), with glycol diacetate being preferred.
• Glycol diether is characterized by the formula R 3 —O—R 4 —O—R 3 , where R 3 and R 4 are as defined above and the remaining R 3 are selected independent of each other (for example, dipropyleneglycol dimethyl ether).
• Cyclic ketone, cyclic ester and cyclic carbonate with 4-5 carbon atoms are likewise suitable (for example, propylene carbonate).
• the alkyl- and alkylene groups can be branched or unbranched.
• organic polar solvents can preferably be used either as stand-alone solvents for the phenolic resin or in combination with fatty acid esters, where the content of oxygen-rich solvents in a solvent mixture should predominate.
• the content of oxygen-rich solvents is preferably at least 50% by weight, more preferably at least 55% by weight of the total solvents.
• phenolic resins generally contain around 45% by weight and, sometimes, up to 55% by weight of solvents, in order to achieve an acceptable process viscosity (of up to 400 mPa ⁇ s)
• the amount of solvent in the phenolic-component can be restricted to at most 40% by weight, and preferably even 35% by weight, through the use of the low viscosity phenolic resins described herein, where the dynamic viscosity is determined by the Brookfield Head Spindle Process.
• the viscosity with reduced quantities of solvent lies well outside the range, which is favorable for technical applications of up to around 400 mPa ⁇ s. In some parts, the solubility is also so bad that at room temperature phase separation can be observed. At the same time the immediate strength of the cores manufactured with this binder system is very low.
• Suitable binder systems exhibit an immediate strength of at least 150 N/cm 2 when 0.8 parts by weight each of the phenolic resin and isocyanate component are used for 100 parts by weight of an aggregate, like, for example, Quarzsand H32 (see for instance EP 771 599 or DE 43 27 292).
• fatty acid ester to the solvent of the phenolic component leads to especially good release properties.
• Fatty acids are suitable, such as, for example, those with 8 to 22 carbons, which are esterified with an aliphatic alcohol.
• fatty acids with a natural origin are used, like, for example, those from tall oil, rapeseed oil, sunflower oil, germ oil, and coconut oil.
• single fatty acids like palmitic fatty acid or myristic fatty acid can, of course, be used.
• Aliphatic mono alcohols with 1 to 12 carbons are particularly suitable for the esterification of fatty acids. Alcohols with 1 to 10 carbon atoms are preferred, s with alcohols with 4 to 10 carton atoms being especially preferred. Based on the low polarity of fatty acid esters, whose alcohol components exhibit 4 to 10 carbon atoms, it is possible to reduce the quantity of fatty acid esters, and to reduce the buildup of smoke. A line of fatty acid esters is commercially obtainable.
• Fatty acid esters whose alcohol components contain from 4 to 10 carbon atoms, are especially advantageous, since they also give binder systems excellent release properties, when their content in the solvent component of the phenolic component amounts to less than 50% by weight based upon the total amount of solvents in the phenolic resin component.
• fatty acid esters with longer alcohol components are the butyl esters of oleic acids and tall oil fatty acid, as well as the mixed octyl-decylesters of tall oil fatty acids.
• the two components of the binder system include an aliphatic, cycloaliphatic or aromatic polyisocyanate, preferably with 2 to 5 isocyanate groups. Based on the desired properties, each can also include mixtures of organic isocyanates.
• Suitable polyisocyanates include aliphatic polyisocyanates, like, for example, hexamethylenediisocyanate, alicyclic polyisocyanates like, for example, 4,4′-dicyclohexylmethanediisocyanate, and dimethyl derivates thereof.
• aromatic polyisocyanates examples include toluol-2,4-diisocyanate, toluol-2,6-diisocyanate, 1,5-napththalenediisocyanate, triphenylmethane-triisocyanate, xylylenediisocyanate and its methyl derivatives, polymethylenepolyphenyl isocyanate and chlorophenylene-2,4-diisocyanate.
• Preferred polyisocyanates are aromatic polyisocyanates, in particular, polymethylenepolyphenyl polyisocyanates such as diphenylmethane diisocyanate.
• polyisocyanates In general 10-500% by weight of the polyisocyanates compared to the weight of the phenolic resins are used. 20-300% by weight of the polyisocyanates is preferred. Liquid polyisocyanates can be used in undiluted form, whereas solid or viscous polyisocyanates can be dissolved in organic solvents. The solvent can consist of up to 80% by weight of the isocyanate components.
• solvents for the polyisocyanate either the above-named fatty acid esters or a mixture of fatty acid esters and up to 50% by weight of aromatic solvents can be used.
• aromatic solvents are naphthalene, alkyl-substituted naphthalenes, alkyl-substituted benzenes, and mixtures thereof.
• aromatic solvents which consist of mixtures of the above named aromatic solvents and which have a boiling point range of between 140 and 230° C. However, preferably no aromatic solvents are used.
• the amount of polyisocyanate used results in the number of the isocyanate group being from 80 to 120% with respect to the number of the free hydroxyl group of the resin.
• the binder systems can include one or more conventional additives, like, for example, those chosen from among silanes (see for instance U.S. Pat. No. 4,540,724), drying oils (U.S. Pat. No. 4,268,425) or “Komplex Kunststoffner” (WO 95/03903).
• the binder systems are offered, preferably, as two-component-systems, whereby the solution of the phenolic resin represents one component and the polyisocyanate, also in solution, if appropriate, is the other component. Both components are combined and subsequently mixed with sand or a similar aggregate, in order to produce the moulding compound.
• the moulding compound contains an effective binding quantity of up to 15% by weight of the binder system with respect to the weight of the aggregate.
• the mixture can contain other conventional ingredients, like iron oxide, ground flax fiber, xylem, pitch and refractory meal (powder).
• the aggregate In order to manufacture foundry-moulded pieces from sand, the aggregate should exhibit a sufficiently large particle size. In this way, the founded piece has sufficient porosity, and fugitive gasses can escape during the casting process. In general at least 80% by weight and preferably 90% by weight of the aggregate should have an average particle size of less than or equal to 290 ⁇ m. The average particle size of the aggregate should be between 100 ⁇ m and 300 ⁇ m.
• sand is preferred as the aggregate material to be used, where at least 70% by weight, and preferably more than 80% by weight of the sand is silicon dioxide.
• Zircon, olivine, aluminosilicate sands and chromite sands are likewise suitable as aggregate materials.
• the aggregate material is the main component in founded pieces.
• the proportion of binder in general amounts to up to 15% by weight, and often between 0.5% and 7% by weight, with respect to the weight of the aggregate.
• Especially preferred is 0.6% to 5% by weight of binder compared to the weight of the aggregate.
• the founded piece is cured so that it retains its exterior shape after being removed from the mold.
• silane with the general formula therefore —(R′—O) 3 —Si—R— is added to the moulding compound before the curing begins.
• R′ is a hydrocarbon radical, preferably an alkyl radical with 1-6 carbon atoms
• R is an alkyl radical, an alkoxy-substituted alkyl radical or an alkyl amine-substituted amine radical with alkyl groups having 1-6 carbon atoms.
• silanes examples include Dow Coming Z6040 and Union Carbide A-187 ( ⁇ -glycidoxypropyltrimethoxysilane), Union Carbide A-1100 ( ⁇ -aminopropyl triethoxysilane), Union Carbide A-1120 (N- ⁇ -(aminoethyl)- ⁇ -amino-propyltrimethoxysilane) and Union Carbide A1160 (ureidosilane).
• additives can be used, including wetting agents and sand mixture extending additives (English Benchlife-additives), such as those disclosed in U.S. Pat. No. 4,683,252 or U.S. Pat. No. 4,540,724.
• mould release agents like fatty acids, fatty alcohols and their derivatives can be used, but as a rule, they are not necessary.
• the curing of the founded piece i.e. binder+aggregate is carried out under conditions well known in the art, using, as catalytic system, a blend of at least two tertiary amines as hereinbefore described.
• the present invention also relates to a process of casting a metal, said process comprises:
• a test was firstly carried out for the measurement of the optimized, i.e. minimum amount of, amine quantity of a single tertiary amine (DMEA, DEMA or DMIPA) or a blend of tertiary amines (DMEA-DEMA, DMEA-TEA) for full curing in order to show the difference of reactivity.
• DMEA a single tertiary amine
• DEMA DMIPA
• DMEA-DEMA tertiary amines
• DMEA-TEA a blend of tertiary amines
• the various resins used for this test are commercial resins from Ashland-Avébène (Usine du Goulet—20, rue Croix du Vallot, 27600 St Pierre-la-Garenne, France) sold under the trade name Avecure®; these resins are composed of a formo-phenolic resin and of an isocyanate resin, in accordance with the present description.
• a fixed amount of sand+resins mixture with a predetermined amount of resins per mass unit of sand (normally between 0.5 and 2% by weight of each resin based on the amount of sand mixed) is placed in a long cylindrical shaped mould, the amine is poured as liquid ahead of the sand-resins cylinder in a U tube and a heated stream of carrier gas (normally nitrogen) at a fixed and predetermined rate is passed through the amine loaded U tubing.
• carrier gas normally nitrogen
• Test cores were prepared as follows:
• the 3 gassings are made at 5.5 bars (static) equivalent to 4.8 bars (dynamic). 2 purgings of 10 seconds each are applied between each gassing operation. Gassing itself lasts 10 seconds at 1.5 bars (dynamic). Carrier gas heater is adjusted to 75° C. ⁇ 3° C. except for TEA for which it was modified to 95° C.
• the optimum (lowest) volume for 100% curing for each amine or blend of amine is obtained by increasing the volume of injected amine(s) by steps of 0.05 mL from 0, until reaching the catalytic volume for which no more sand is left free (100% curing, the sand+binder test core is totally solidified).
• Amine(s) optimized volumes have been converted to weights required for full curing through usage of their corresponding densities.
• the amines density was measured or checked from literature on a densimeter Metier Toledo DA-100M.
• the density of DMEA is 0.678
• the one of DEMA is 0.706
• density of TEA is 0.728.
• Table 1 indicates the amounts (in grams) of single tertiary amine (DMEA or DEMA) and the amount of different DMEA/DEMA blends required for a full curing core test as described above.
• Theoretical masses (Theo. Mass) of blends needed for 100% test core curing in Table 1 are calculated according to the s following equation:
• Theo Mass (ratio of DMEA ⁇ mass of DMEA alone needed for full curing+ratio of DEMA ⁇ mass of DEMA alone needed for full curing).
• Theo Mass (ratio of DMEA ⁇ mass of DMEA alone needed for full curing+ratio of TEA ⁇ mass of TEA alone needed for full curing).
• Table 2 indicates the amount of single tertiary amine (DMEA or TEA) and the amount of different DMEA/TEA blends required for a full test core curing as described above.

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