USRE32720E - Foundry moulds and cores - Google Patents

Foundry moulds and cores Download PDF

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USRE32720E
USRE32720E US06900618 US90061886A USRE32720E US RE32720 E USRE32720 E US RE32720E US 06900618 US06900618 US 06900618 US 90061886 A US90061886 A US 90061886A US RE32720 E USRE32720 E US RE32720E
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binder
molar ratio
process
sand
resin
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US06900618
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Peter H. R. B. Lemon
Jeffrey D. Railton
Peter R. Ludlam
Timothy J. Reynolds
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Borden Chemical UK Ltd
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Borden (UK) Ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G16/00Condensation polymers of aldehydes or ketones with monomers not provided for in the groups C08G4/00 - C08G14/00
    • C08G16/02Condensation polymers of aldehydes or ketones with monomers not provided for in the groups C08G4/00 - C08G14/00 of aldehydes
    • C08G16/0212Condensation polymers of aldehydes or ketones with monomers not provided for in the groups C08G4/00 - C08G14/00 of aldehydes with acyclic or carbocyclic organic compounds
    • C08G16/0218Condensation polymers of aldehydes or ketones with monomers not provided for in the groups C08G4/00 - C08G14/00 of aldehydes with acyclic or carbocyclic organic compounds containing atoms other than carbon and hydrogen
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22CFOUNDRY MOULDING
    • B22C1/00Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds
    • B22C1/16Compositions 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
    • B22C1/20Compositions 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
    • B22C1/22Compositions 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 of resins or rosins
    • B22C1/2233Compositions 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 of resins or rosins obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • B22C1/2246Condensation polymers of aldehydes and ketones
    • B22C1/2253Condensation polymers of aldehydes and ketones with phenols
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G8/00Condensation polymers of aldehydes or ketones with phenols only
    • C08G8/28Chemically modified polycondensates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUSE OF INORGANIC OR NON-MACROMOLECULAR ORGANIC SUBSTANCES AS COMPOUNDING INGREDIENTS
    • C08K5/00Use of organic ingredients
    • C08K5/54Silicon-containing compounds

Abstract

A foundry moulding composition comprising (a) a granular refractory material, and (b) from 0.5% to 8% based on the weight of the refractory material of a binder comprising (i) an aqueous solution of a potassium alkali phenol-formaldehyde resin, said aqueous solution having a solids content of from 50% to 75% and said resin having a weight average molecular weight (Mw) of from 600 to 1500, a formaldehyde:phenol molar ratio of from 1.2:1 to 2.6:1 and a potassium hydroxide:phenol molar ratio of from 0.2:1 to 1.2:1 and (ii) at least one silane in an amount of from 0.05% to 3% based on the weight of said aqueous solution, said binder being curable by contact therewith of from 5% to 60% based on the weight of said aqueous solution of a C1-3 alkyl formate.

Description

BACKGROUND OF THE INVENTION

This invention relates to the manufacture of foundry moulds and cores which do not evolve pungent acid gases on thermal decomposition. More particularly it refers to a method of making moulds and cores of this type rapidly at ambient temperature.

Phenol formaldehyde and phenol formaldehyde/furfuryl alcohol condensation products catalyzed with strong acids such as sulphuric acid, paratoluene sulphonic acid, are well known as binders for sand in the production of foundry moulds and cores. However, they have the disadvantage that pungent fumes of sulphur dioxide are evolved on thermal decomposition.

The use of alkaline phenolic resins catalyzed with esters has been suggested in Japanese Patent Publication No. 130627/1975 and is the subject of co-pending U.S. Application Ser. No. 224,131, filed Jan. 12, 1981, now U.S. Pat. No. 4,426,467, issued Jan. 17, 1984 and U.S. Ser. No. 434,462 filed Oct. 14, 1982, now abandoned. The use of such binder systems enables the manufacture of foundry moulds and cores which do not evolve pungent acid gases on mixing or during casting. Further, by suitable selection of resins and ester catalysts rapid hardening at ambient temperature can be achieved. However, to obtain such results on a large scale it is necessary to use specialized rapid mixing equipment such as that described in British patent specification Nos. 1257181 and 1369445 of Baker Perkins.

The present invention is based on the discovery that the use of esters as catalysts for alkaline phenolic resins in the manufacture of foundry moulds and cores can be adapted to a gassing system which is capable of rapid cure at ambient temperature. The use of gassing to promote curing of binders for foundry moulds and cores is known. The major systems which are or have been industrially used are as follows:

(a) The "Carbon Dioxide Process" in which CO2 is passed through a mixture of sand and sodium silicate. However, the resultant cores or moulds are very sensitive to water and lose strength "damp back" on storage, will not accept aqueous washes and show very poor breakdown on casting. It is necessary to add breakdown agents such as sucrose to promote better breakdown. Over-gassing produces very poor strengths.

(b) The "Sulphur Dioxide Process" disclosed by SAPIC in British Pat. No. 1,411,975 which uses (1) a peroxide which is dangerous to store and dispense, particularly in a foundry environment, and (2) pungent SO2 which has a low Threshold Limit Value (TLV) and is unpleasant to handle.

(c) The "Isocure" process disclosed by Ashland in British Pat. No. 1,190,644 which uses a benzilic ether phenolic polyol and methylene diphenyl diisocyanate. The reaction between the polyol and diisocyanate is accelerated by gassing with triethylamine or dimethyl ethylamine. The diisocyanates have very low TLV's and react with water preferentially over the polyol so that it is necessary to use dry sand and dry air to convey the sand/binder mix into core box or mould. The amines have relatively low TLV's and their toxicology is not well understood. Cured cores tend to absorb water and lose some strength on storage. Certain casting defects are observed with "Isocure" cores/moulds, e.g. "pinholing" caused by the nitrogen content of the binder which reduces to ammonia in the casting environment, dissolves in the molten metal, and is evolved as small blow holes on cooling; "graphitic defect" which is a deposit of graphite carbon which collects in flakes on the surface of the casting; and "finning" or "veining" caused by the mould or core cracking under the expansion stresses during casting and molten metal running into the cracks.

The present invention enables the rapid and efficient production of foundry moulds and cores without the disadvantages of the prior art as described above.

SUMMARY OF THE INVENTION

Accordingly, the present invention provides a method of making a foundry mould or core which method comprises mixing a granular refractory material with from 0.5 to 8% of a binder which comprises an aqueous solution, having a solids content of from 50 to 75% by weight, of a potassium alkali phenol-formaldehyde resin having the following characteristics:

(a) a weight average molecular weight (Mw) of from 600 to 1500;

(b) a formaldehyde: phenol molar ratio of from 1.2:1 to 2.6:1; and

(c) a KOH: phenol molar ratio of from 0.2:1 to 1.2:1, the binder including from 0.05 to 3% by weight based on the weight of the resin solution of at least one silane, forming the mixture in a vented core or mould box and gassing the formed mixture with at least one C1 to C3 alkyl formate to cure the binder.

DETAILED DESCRIPTION OF THE INVENTION

The granular refractory materials used in the present invention may be of any of the refractory materials employed in the foundry industry for the production of moulds and cores, such as silica sand, chromite sand, zircon or olivine sand. The compositions of the invention have the particular advantage that the difficulties commonly associated with the bonding of sands of alkaline reaction such as olivine and chromite or beach sands containing shell fragments and which arise from the neutralization or partial neutralization of the acid catalyst used, are completely overcome since in the invention the binder is cured under alkaline conditions. The invention is, therefore, of particular utility where it is necessary or desirable to employ alkaline sands.

The nature of the phenol-formaldehyde resin used is an important feature of the present invention. There are several features of the resin which are important. Since the present invention is directed to cold set techniques, the resin binder will be used as an aqueous solution of the resin. The solids content of the aqueous solution is in the range 50 to 75% by weight. Solids contents below 50% are not used because they contain too much water which reduces the effectiveness of the binder. Solids contents above 75%, are not used because the viscosity becomes too high.

The phenol-formaldehyde resins used in this invention have a weight average molecular weight (Mw) of from 600 to 1500. Resins with Mw outside this range give products which are relatively weak or build up strength more slowly. We have, to date, obtained best results using resins having Mw in the range 700 to 1100.

The resins used in this invention are potassium alkaline phenol-formaldehyde resins by which is meant that the alkali in the resin is potassium alkali. This alkali will usually be present in the resin during manufacture but can be added to the resin subsequently as KOH, preferably in aqueous solution of suitable strength. The alkalinity of the resin is expressed in terms of its KOH content and specifically by the molar ratio of KOH to the phenol in the resin. Other alkalis are not expressly excluded and may be present in minor amounts but will not be specifically added because they give products having lower strength.

The molar ratio of KOH: phenol in the resin solution is in the range 0.2:1 to 1.2:1 preferably 0.3:1 to 1:1. Outside this range the products have relatively poor strength and, above the top range limit, the resin is hazardously alkaline. We have obtained best results using resin solutions having a KOH: phenol molar ratio in the range of 0.4 to 0.6.

The resins used have a formaldehyde to phenol molar ratio of from 1.2:1 to 2.6:1, preferably 1.5:1 to 2.2:1. Lower ratios are not used because the resins are relatively unreactive. Higher ratios are not used because the resins produced contain undesirably high levels of unreacted formaldehyde and give products having lower strength.

It is a subsidiary aspect of this invention that the resin used satisfies the following criteria:

(a) Mw from 700 to 1100;

(b) KOH: phenol molar ratio 0.4:1 to 0.6:1 and

(c) formaldehyde: phenol molar ratio 1.5:1 to 2.2:1

A silane is included in the binder to improve strength. Amounts as low as 0.05% by weight on the weight of resin solution provide a significant improvement in strength.

Increasing the amount of silane gives greater improvements in strength up to about 0.6% by weight on the resin solution. Higher silane concentrations are not preferred because of added cost. Further, because the silane typically used is γ-aminopropyltriethoxy silane which contains nitrogen, use of excess silane may increase the risk of pinholing defects and for these reasons amounts in excess of 3% by weight on the resin solution are not used.

The binder and particulate refractory material can be mixed and formed by conventional techniques. The vented core and mould boxes used can also be of conventional type as are used in prior art gassing systems. The binder is cured, according to the present invention, by gassing with a C1 to C3 alkyl formate, very preferably methyl formate. The alkyl formate curing catalyst will not usually be used as a pure gas but as a vapour or aerosol in an inert carrier gas. By inert carrier gas we mean a gas which does not react with the formate catalyst or have an adverse effect on the curing reaction or the properties of the product. Suitable examples include air, nitrogen or carbon dioxide.

The gassing catalyst is a C1 to C3 alkyl formate preferably dispersed in a carrier gas as vapour or an aerosol. Other esters e.g. formate esters of higher alcohols such as butyl formate, and esters of C1 to C3 alcohols with higher carboxylic acids such as methyl and ethyl acetates, are not effective as gassing catalysts. Methyl formate is significantly more active as a catalyst than ethyl formate which is better than the propyl formates. The reasons for the catalytic activity of the C1 to C3 alkyl formates and, within this group, the marked superiority of methyl formate, are not clear. The relative volatility of these compounds enables their use as gassing catalysts. This is especially true of methyl formate which is a volatile liquid having a boiling point at atmospheric pressure of 31.5° C. At ambient temperatures (below 31.5° C.), typically 15° to 25° C., it is sufficiently volatile that passing carrier gas through liquid methyl formate (maintained at ambient temperature) gives a concentration of methyl formate vapour in the carrier gas sufficient to act as catalyst to cure the binder. Ethyl and the propyl formates are less volatile than the methyl ester, having boiling points in the range 54° to 82° C. at atmospheric pressure.

In order to entrain sufficient of these esters in the gas phase to enable effective catalysis, we have found it appropriate to heat the esters to near their boiling point and use a stream of carrier gas preheated to e.g. 100° C.

An alternative to true vaporization is to form an aerosol in the carrier gas. Methyl formate is so volatile as to make this impractical. Using ethyl and propyl formates it is desirable to pre-heat them to enhance even distribution in the core or mould during gassing.

As is indicated above, methyl formate is the most active catalyst and, by virtue of its volatility, is the easiest to use. Accordingly, the use of methyl formate in a stream of inert carrier gas as the gassing catalyst forms a particular aspect of this invention. A further practical advantage of these formate esters, especially methyl formate is their relative low toxicity and the fact that their toxicity is well understood.

The concentration of the formate catalyst in the carrier gas is preferably at least 0.2% by volume and typically from 0.5 to 5% by volume. The total amount of catalyst used will typically be from 5 to 60% preferably from 15 to 35%, by weight on the weight of the resin solution. The time required for adequate gassing depends on the size and complexity of the core or mould and on the particular resin used. It can be as short as 0.1 secs but more usually is in the range 1 sec to 1 min. Longer times e.g. up to 5 mins can be used if desired or for large moulds or cores. After gassing the core or mould is stripped from the box. Sufficient time must elapse to permit the strength of the mould or core to build up to enable stripping without damage. Production speed can be enhanced by purging the mould or core box with a suitable inert gas such as air which removes residual catalyst vapour and water and other by-products of the curing reaction.

The amount of resin solution used as binder is from 0.5 to 8%, preferably 1 to 3%, by weight on the weight of the refractory particulate material. Use of lower amounts of binder gives cores of poor strength. Higher amounts of binder give no significant advantage and give generally poorer breakdown on casting and increase the difficulty of sand recovery.

The following Examples illustrate the invention.

The techniques used in the Examples are described below:

Manufacture of phenol formaldehyde resin solutions

100% phenol was dissolved in 50% aqueous KOH in an amount corresponding to the desired KOH:phenol molar ratio (from 0.2 to 1.2). The solution was heated to reflux and 50% aqueous formaldehyde was added slowly, whilst maintaining reflux, in an amount corresponding to the desired formaldehyde:phenol molar ratio (1.6, 1.8 or 2.0). The reaction mixture was maintained under reflux until it attained a pre-determined viscosity corresponding to the desired value of Mw. (If desired the solids content can be adjusted by distillation, but this is not usually necessary, a further advantage of the invention. In some cases minor amounts of KOH solution were added to adjust the KOH:phenol ratio, but this would not be necessary in full scale production.) The resin solution was cooled to 40° C. and 0.4% by weight on the weight of the resin solution of γ-aminopropyl triethoxy silane was added.

Testing of resins

(a) viscosity--measured using an Ostwald (U-tube) viscometer at 25° C.

(b) solids content--measured by heating a weighed sample (2.0±0.1 g) in an air circulating oven for 3 hrs at 100° C.

(c) Molecular weight Mw)--measured using gel permeation chromatography. Samples were prepared by precipating resin from the resin solution by adding H2 SO4 ; separating, washing and drying the precipitate and dissolving it in tetrahydrofuran.

Preparation of foundry sand core mix

1 kg of the selected sand was charged into a Fordath laboratory core mixer and mixed for 2 mins, with 20 g phenol-formaldehyde resin prepared as described above. The mix was discharged into a tin and sealed immediately to prevent evaporation of water.

Preparation of test foundry cores

5×5 cm cylinder compression test pieces were prepared by the standard procedure recommended by I.B.F. working party P but using a perforated bottom plate of the cylinder with a recess which could be connected to a source of negative pressure. The top of the cylinder was sealed with another perforated plate connected to a bubbler containing liquid methyl formate at ambient temperature. When vacuum was applied to the bottom plate air was bubbled through the methyl formate and the ester vapour conveyed in the air stream through the sand resin mix in the cylinder core box. Compression strength was determined on the resultant cores after storing at 20° C., 50% relative humidity for 1 min, 5 mins, 1 hr. 2 hrs. 3 hrs. and 24 hrs. Initial tests indicated that 30 secs. was sufficient time to produce the optimum strength and this was used as a standard in the Examples below.

EXAMPLE 1

Test cores were made using solutions of resins having the following properties:

formaldehyde:phenol molar ratio--2.0

KOH:phenol molar ratio from--0.4 to 0.8.

Mw --960 or 1000

Solids content--63.5%

0.4% by weight on the resin solution of γ-aminopropyltriethoxy silane was added. The sand used was Chelford 50 and the amount of resin was 2% by weight resin solution on the sand. The results are set out in Tables 1 and 2. Table 1 gives the results for resins with Mw =960 and Table 2 for resins with Mw =1000.

The data in the table show that cores of adequate strength can be made but that the strength falls of somewhat at KOH:phenol ratios greater than 0.6.

              TABLE 1______________________________________Test No.  1        2        3      4      5______________________________________KOH:Phenol     0.4      0.5      0.6    0.7    0.8Viscosity (cP)     500      390      313    250    --CompressionStrength (MPa)1 min     1.2      2.2      2.6    2.6    2.95 min     1.9      3.6      3.1    3.0    3.01 hr      2.2      3.4      3.5    3.2    3.03 hr      2.1      3.9      4.0    3.5    3.124 hr     3.0      4.3      4.8    3.2    2.2______________________________________

              TABLE 2______________________________________Test No.     6       7          8     9______________________________________KOH:Phenol   0.4     0.5        0.6   0.7Viscosity (cP)        688     500        375   --CompressionStrength (MPa)1 min        1.7     2.4        2.9   2.95 min        2.4     3.2        3.2   3.31 hr         2.4     3.4        3.7   3.63 hr         3.2     4.1        3.2   3.424 hr        4.4     4.8        3.9   2.9______________________________________
EXAMPLE 2

Test cores were made using solutions of resins having the following properties:

formaldehyde:phenol molar ratio--2.0

KOH:phenol molar ratio--0.65

Mw from--718 to 1050

Solids content--66%

0.4% by weight γ-aminopropyltriethoxy silane was added to the resin solution. The sand used was Chelford 50 and the amount of resin solution used was 2% by weight on the sand. The experiment was reported using similar solutions to which 50% KOH solution was added to increase the KOH:phenol ratio to 0.85. The solids contents of these resin solutions were 64%. The results are set out in Table 3. The data for the resins with KOH:phenol=0.65 is in the (a) columns and for resins with KOH:phenol=0.85 in the (b) columns. As in Example 1 the use of higher KOH:phenol ratios gives inferior results especially at the higher values of Mw.

              TABLE 3______________________________________  Test No.  10      11        12        13  --M.sub.w  718     849       966       1050  a    b      a      b    a    b    a    b______________________________________KOH:Phenol     0.65   0.85   0.65                        0.85                             0.65                                  0.85                                       0.65                                            0.85Solids (%)     66    64      66   64   66   64   66   64Viscosity    107    81     220  111  320  144  405  167(cP)CompressionStr. (MPa)1 min    2.7    2.3    2.9  2.2  2.6  2.0  1.9  2.05 min    3.4    2.7    3.3  2.6  3.0  1.1  2.2  2.01 hr     3.0    2.7    3.5  2.7  2.7  2.2  2.2  2.03 hr     3.6    3.2    3.5  2.6  2.9  1.7  1.9  2.024 hr    4.5    2.9    3.5  1.1  1.8  0.8  1.2  0.9______________________________________
EXAMPLE 3

Resins with varying properties were used to make test cores as described above. The sand used was Chelford 50, the amount of resin solutions was 2% by weight on the sand and all the resin solutions contained 0.4% by weight γ-aminotreithoxy silane. The results are set out in Table 4.

              TABLE 4______________________________________Test No. 14     15     16   17   18   19   20   21______________________________________--M.sub.w    850    850    850  1000 1000 1000 1000 1000KOH:Phenol     0.72   0.72   0.45                        0.34                             0.57                                  0.68                                       0.85                                            1.02formalde-    1.6    1.6    1.6  2.0  2.0  2.0  2.0  2.0hyde:phenolSolids (%)    60.2   66.2   65.4 64.0 64.0 64.0 64.0 64.0Viscosity    277    414    600  --   --   --    150 --(cP)CompressionStrength(MPa)1 min    2.4    2.3    1.8  0.9  2.7  2.5  2.3  1.65 min    2.5    2.4    2.5  2.7  2.8  2.7  2.4  1.81 hr     2.5    2.7    2.0  2.3  2.8  2.8  2.4  2.03 hr     2.5    3.2    2.1  2.2  3.9  3.2  2.3  --24 hr    1.2    3.0    3.5  3.1  4.5  2.2  1.8  1.9______________________________________

While the invention has been disclosed in this patent application by reference to the details of preferred embodiments of the invention, it is to be understood that this disclosure is intended in an illustrative rather than in a limiting sense, as it is contemplated that modifications will readily occur to those skilled in the art, within the spirit of the invention and the scope of the appended claims.

Claims (16)

What is claimed is:
1. A process for the production of foundry moulds or cores which comprises;
mixing a granular refractory material with from 0.5% to 8% based on the weight of the refractory material of a binder solution, said binder solution comprising (i) an aqueous solution of a potassium alkali phenol-formaldehyde resin, said aqueous solution having a solids content of from 50% to 75% and said resin having a weight average molecular weight (Mw) of from 600 to 1500, a formaldehyde:phenol molar ratio of from 1.2:1 to 2.6:1 and a potassium hydroxide:phenol molar ratio of from 0.2:1 to 1.2:1 and (ii) at least one silane in an amount of from 0.05% to 3% based on the weight of said aqueous solution,
discharging the mixture into a vented core or mould box, and
gassing the formed mixture with at least one C1-3 alkyl formate to cure the binder.
2. The process of claim 1 wherein the refractory material is selected from the group comprising silica sand, quartz, chromite sand, zircon, olivine sand or beach sands containing shell fragments.
3. The process of claim 2 wherein the refractory material is chromite sand, olivine sand or beach sands containing shell fragments.
4. The process of claim 1 wherein the Mw of said resin is from 700 to 1100.
5. The process of claim 1 wherein the potassium hydroxide:phenol molar ratio is from 0.3:1 to 1:1.
6. The process of claim 4 or 5 wherein the potassium hydroxide:phenol molar ratio is from 0.4:1 to 0.6:1.
7. The process of claim 1 wherein the formaldehyde:phenol molar ratio is from 1.5:1 to 2.2:1.
8. The process of claim 6 wherein the formaldehyde:phenol molar ratio is from 1.5:1 to 2.2:1.
9. The process of claim 1 wherein said refractory material is mixed with from 1% to 3% based on the weight of the refractory material of said binder solution.
10. Th process of claim 1 wherein the mixture is gassed with from 5% to 60% based on the weight of the aqueous solution of said alkyl formate.
11. The process of claim 10 wherein the mixture is gassed with from 15% to 35% based on the weight of the aqueous solution of said alkyl formate.
12. The process of claim 11 wherein said alkyl formate is methyl formate.
13. The process of claim 1 or 12 wherein said alkyl formate is dispersed in a carrier gas.
14. The process of claim 13 wherein the concentration of said formate in the carrier gas is from 0.5% to 5% by volume. .Iadd.
15. A process for the production of foundry moulds or cores from a mixture of sand with a curable binder, which comprises:
mixing sand with from 0.5% to 8% based on the weight of the sand of a binder solution, said binder solution comprising (i) an aqueous solution of a potassium alkali phenol-formaldehyde resin, said aqueous solution having a solids content of from 50% to 75% and said resin having a weight average molecular weight (Mw) of from 600 to 1500, a formalehyde-phenol molar ratio of from 1.2:1 to 2.6:1 and a potassium hydroxide:phenol molar ratio of from 0.2:1 to 1.2:1, and (ii) at least one silane in an amount that provides a significant improvement in strength,
discharging the mixture into a vented core or mould box, and
gassing the formed mixture with at least one C1-3 alkyl formate to cure the binder..Iaddend. .Iadd.16. The process of claim 15 wherein the weight average molecular weight of said resin is from 700 to 1100..Iaddend. .Iadd.17. The process of claim 15 wherein the potassium hydroxide:phenol molar ratio is from 0.3:1 to 1:1..Iaddend. .Iadd.18. The process of claim 15 wherein the formaldehyde-phenol molar ratio is from 1.5:1 to 2.2:1..Iaddend. .Iadd.19. The process of claim 15 wherein the mixture is gassed with from 5% to 60% of said alkyl formate, based on the weight of the aqueous solution of binder resin..Iaddend. .Iadd.20. A process for the production of foundry moulds or cores from a mixture of sand with a curable binder, which comprises:
mixing sand with from 0.5% to 8% by weight of a binder solution based on the weight of the sand, said binder solution comprising (i) an aqueous solution of a potassium alkali phenol-formaldehyde resin, said aqueous solution having a solids content of from 50% to 75% and said resin having a weight average molecular weight of from 700 to 1100, a formaldehyde-phenol molar ratio of from 1.5:1 to 2.2:1, and a potassium hydroxide:phenol molar ratio of from 0.3:1 to 1:1, and (ii) at least one silane in an amount that provides a significant improvement in strength,
discharging said mixture into a vented core or mould box, and
gassing the formed mixture with from 5% to 60% of at least one C1-3 alkyl formate, based on the weight of the aqueous resin binder solution, to cure said binder..Iaddend. .Iadd.21. The process of claim 20 wherein the potassium hydroxide:phenol molar ratio is from 0.4:1 to 0.6:1..Iaddend. .Iadd.22. The process of claim 20 wherein the alkyl formate is methyl formate..Iaddend. .Iadd.23. A cold set system for the production of foundry moulds or cores utilizing vented core boxes or vented mould boxes, during which production foundry sand is mixed with a phenolic resin binder, the sand is shaped, and a curing agent is applied, to cure the binder, comprising:
a phenolic binder comprising an aqueous solution of a potassium alkali phenol-formaldehyde resin, said aqueous solution having a solids content of from 50% to 75% and said resin having a weight average molecular weight of from 600 to 1500, a formaldehyde:phenol molar ratio of from 1.2:1 to 2.65:1 and a potassium hydroxide:phenol molar ratio of from 0.2:1 to 1.2:1, and,
for curing said binder upon contact therewith, after said binder has been applied to said sand and said sand has been shaped in a vented core box or a vented mould box, at least one C1 to C3 alkyl formate dispersed in a carrier gas as a vapor or as an aerosol..Iaddend. .Iadd.24. The system of claim 23 wherein the weight average molecular weight of said
resin is from 700 to 1100..Iaddend. .Iadd.25. The system of claim 23 wherein the potassium hydroxide:phenol molar ratio is from 0.3:1 to 1:1..Iaddend. .Iadd.26. The system of claim 23 wherein the formaldehyde:phenol molar ratio is from 1.5:1 to 2.2:1..Iaddend. .Iadd.27. The system of claim 23 wherein said binder comprises at least one silane in an amount that provides a significant improvement in strength..Iaddend. .Iadd.28. A cold-set system for the production of foundry moulds or cores utilizing vented core boxes or vented mould boxes, during which production foundry sand is mixed with a phenolic resin binder, the sand is shaped, and a curing agent is applied to cure the binder, comprising:
a phenolic binder comprising an aqueous solution of a potassium alkali phenol:formaldehyde resin, said aqueous solution having a solids content of from 50% to 75%, and said resin having a weight average molecular weight of from 700 to 1100, a formaldehyde:phenol molar ratio of from 1.5:1 to 2.2:1, and a potassium hydroxide:phenol molar ratio of from 0.3:1 to 1:1, and said binder comprising at least one silane in an amount that provides a significant improvement in strength upon curing, and
for curing said binder upon contact therewith after said binder has been applied to said sand and said sand has been shaped in a vented core box or a vented mould box, at least one C1 to C3 alkyl formate dispersed in a carrier gas as a vapor or as an aerosol..Iaddend. .Iadd.29. The system of claim 28 wherein said potassium hydroxide:phenol molar ratio is from 0.4:1 to 0.6:1..Iaddend. .Iadd.30. The system of claim 28 wherein said alkyl formate comprises methyl formate..Iaddend.
US06900618 1982-11-09 1986-08-26 Foundry moulds and cores Expired - Lifetime USRE32720E (en)

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EP0324579A2 (en) * 1988-01-12 1989-07-19 Borden (Uk) Limited Foundry moulding composition
DE4017602A1 (en) * 1989-06-26 1991-01-03 Borden Inc A process for the bonding of lignocellulosic material with houses on gaseous esters
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EP0422756A1 (en) * 1989-10-10 1991-04-17 Borden, Inc. Method to improve flowability of alkaline phenolic resin coated sand
US5021539A (en) * 1989-03-24 1991-06-04 Acme Resin Corporation Alkaline benzylic ether phenolic resin binders
US5043412A (en) * 1988-06-23 1991-08-27 Borden, Inc. Ambient temperature curing, high carbon contributing compositions
US5074946A (en) * 1986-09-30 1991-12-24 Borden, Inc. Wood bending methods employing fast curing phenolic resins
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US5126089A (en) * 1990-03-05 1992-06-30 Acme Resin Corp. Method for easy removal of sand cores from castings
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US5223554A (en) * 1990-08-02 1993-06-29 Borden, Inc. Accelerators for curing phenolic resole resins
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Cited By (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5074946A (en) * 1986-09-30 1991-12-24 Borden, Inc. Wood bending methods employing fast curing phenolic resins
EP0324579A3 (en) * 1988-01-12 1990-09-05 Borden (Uk) Limited Foundry moulding composition
US4980394A (en) * 1988-01-12 1990-12-25 Borden (Uk) Limited Foundry moulding composition
EP0324579A2 (en) * 1988-01-12 1989-07-19 Borden (Uk) Limited Foundry moulding composition
US5234973A (en) * 1988-04-08 1993-08-10 Acme Resin Corporation Compositions for foundry molding processes utilizing reclaimed sand
US5043412A (en) * 1988-06-23 1991-08-27 Borden, Inc. Ambient temperature curing, high carbon contributing compositions
US4994505A (en) * 1988-11-15 1991-02-19 Borden, Inc. Binder compositions comprising low molecular weight poly(orthomethylolated) phenolic compound and novolac resin
US5340888A (en) * 1988-12-22 1994-08-23 Borden Inc. Phenolic resin composition
US5021539A (en) * 1989-03-24 1991-06-04 Acme Resin Corporation Alkaline benzylic ether phenolic resin binders
USRE34228E (en) * 1989-03-24 1993-04-20 Acme Resin Corp. Alkaline benzylic ether phenolic resin binders
DE4017602A1 (en) * 1989-06-26 1991-01-03 Borden Inc A process for the bonding of lignocellulosic material with houses on gaseous esters
EP0422756A1 (en) * 1989-10-10 1991-04-17 Borden, Inc. Method to improve flowability of alkaline phenolic resin coated sand
US5077323A (en) * 1989-10-10 1991-12-31 Acme Resin Corporation Method to improve flowability of alkaline phenolic resin coated sand
US5126089A (en) * 1990-03-05 1992-06-30 Acme Resin Corp. Method for easy removal of sand cores from castings
US5169880A (en) * 1990-04-03 1992-12-08 Kao Corporation Process for making foundry sand mold
US5602192A (en) * 1990-07-05 1997-02-11 Kao Corporation Process for producing sand mold
US5179177A (en) * 1990-08-02 1993-01-12 Borden, Inc. Method for retarding ambient temperature hardening of a phenolic resin composition
US5182346A (en) * 1990-08-02 1993-01-26 Borden, Inc. Accelerators for curing phenolic resole resins
US5214111A (en) * 1990-08-02 1993-05-25 Borden, Inc. Retarders for curing phenolic resole resins
US5214079A (en) * 1990-08-02 1993-05-25 Borden, Inc. Accelerators for curing phenolic resole resins
US5218010A (en) * 1990-08-02 1993-06-08 Borden, Inc. Accelerators for refractory magnesia
US5223554A (en) * 1990-08-02 1993-06-29 Borden, Inc. Accelerators for curing phenolic resole resins
US5182347A (en) * 1990-08-02 1993-01-26 Borden, Inc. Accelerators for refractory magnesia
US5248707A (en) * 1990-08-02 1993-09-28 Borden, Inc. Accelerators for refractory magnesia
US5294649A (en) * 1990-08-02 1994-03-15 Borden, Inc. Accelerators for curing phenolic resole resins
US5096983A (en) * 1990-08-02 1992-03-17 Borden, Inc. Method for making a phenolic resole resin composition having extended work life
US5145887A (en) * 1991-04-04 1992-09-08 Borden, Inc. High surface area magnesia as hardener for phenolic resins
US6505671B1 (en) 2000-12-28 2003-01-14 Hayes Lemmerz International, Inc. Method for producing a sand core

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