Production of articles of bonded particulate material and binder compositions for use therein

Abstract

A binder composition for producing articles of bonded particulate material such as foundry moulds or cores comprises an alkaline aqueous solution of a resol phenol-aldehyde resin and an oxyanion capable of forming a stable complex with the resin the amount of alkali present in the solution being sufficient to substantially prevent stable complex formation. Bonded articles are produced from mixtures of particulate material and the binder composition by passing carbon dioxide gas through the formed articles whereby the oxyanion forms a stable complex with the resin and the resin is cured. The oxyanion may be for example borate, stannate or aluminate.

Description

This invention relates to the production of articles of bonded particulate material and binder compositions for use therein.

The invention will be described with Particular reference to the production of foundry moulds or cores.

It is known from British patent application No. 2037787A to produce foundry moulds or cores from sand and a binder, which can be cured by carbon dioxide gas, consisting of an alcohol-soluble phenolic resin, a polyvalent metal hydroxide (such as calcium hydroxide) and/or oxide, an organic solvent (such as methanol or ethanol), an alkali metal hydroxide and water. Such a binder system is disadvantageous because, since the polyvalent metal hydroxide and/or oxide is a powder, metering of the amount added to the sand is difficult to control and the reactivity of the powder is a function of its particle size. When the binder is in contact with carbon dioxide gas the polyvalent metal (e.g. calcium) ions are solubilised and cause crosslinking of the phenolic resin molecules. Such binders tend to harden slowly in the absence of air and more rapidly when allowed to stand in contact with air.

It is further known from U.S. Pat. No. 2,889,241 to use an aqueous alkaline thermosetting phenol-formaldehyde resin solution to which has been added a boron-oxygen compound such as boric acid, an alkali metal borate or ammonium borate as an adhesive in the manufacture of plywood. In use the adhesive is cured by the action of heat.

It is further known from Japanese Patent Publication No. 60-6302 to use as a binder for refractory materials a polyvinyl alcohol modified, base catalyzed phenol-formaldehyde resin and to harden the resin at room temperature using boric acid and/or a tetraborate as hardener.

It is further known from U.S. Pat. No. 4,584,329 to make a hardenable moulding mass using a phenol-formaldehyde resin binder containing a boric acid compound. The boric acid compound may be incorporated in the resin binder during condensation of the resin or the resin binder may be ground with the boric acid compound.

It is further known from British Patent No. 966678 to condense a phenol with a source of formaldehyde in contact with a borate of zinc or other bivalent metal as catalyst.

According to the present invention there is provided a binder composition comprising an alkaline aqueous solution of a resol of phenol-aldehyde resin and an oxyanion capable of forming a stable complex with the resin the amount of alkali present in the solution being sufficient to substantially prevent stable complex formation between the resin and the oxyanion.

According to a further feature of the invention there is provided a process for the production of an article of bonded particulate material comprising forming to a desired shape a mixture of particulate material and a binder composition comprising an alkaline aqueous solution of a resol phenol-aldehyde resin and an oxyanion capable of forming a stable complex with the resin and passing carbon dioxide gas through the formed shape so as to cause the oxyanion to form a stable complex with the resin and thereby to cure the resin.

The oxyanions present in the binder composition act as cross-linking agents for the resin by forming complexes with adjacent resol phenolaldehyde chains and the cross-linking action of the oxyanions is promoted by the carbon dioxide gas which is passed through the article formed of particulate material and the binder composition. As a result much larger, more highly cross-linked resol phenol-aldehyde molecules are formed and the resin is cured. The exact mechanism by which the carbon dioxide promotes curing of the resin is not certain but the carbon dioxide forms carbonic acid by reaction with water in the binder composition, thus lowering the pH of the binder and the oxyanions form stable complexes with the resin molecules at the reduced pH. The alkalinity of the binder composition must be such that the oxyanions remain largely in the uncomplexed state. Complexing and hence curing of the resin on the passage of carbon dioxide takes place when the pH is reduced.

The preferred resol phenol-aldehyde resin is one which contains predominantly molecules in which adjacent phenolic residues are linked together by methylene groups forming bridges between the ortho and para positions because such molecules have a large number of sites for complexing with the oxyanions. Molecules in which the phenolic residues are linked by ortho-ortho methylene bridges have very few sites for complexing with oxyanions, (in the case of a linear molecule only one site at each end), and it is therefore desirable that such molecules are absent, or that they are present in the resin in relatively small numbers. Resins containing molecules having phenolic residues linked by a combination of ortho-para methylene bridges and ortho-ortho may be used but are less preferred.

In order to maximize the number of sites for oxyanion complexing all the available positions on the phenolic residues which are ortho to the phenolic hydroxyl group in anortho-para methylene bridged molecule should be methylolated.

The phenol which is used to produce the resol phenol-aldehyde resin is preferably one which produces a condensation product when reacted with an aldehyde having the highest possible number of ortho-methylol groups. The preferred phenol is phenol itself. Substituted phenols such as p-cresol or m-cresol, or phenolic compounds such as p-phenol sulphonic acids may be used, either on their own or in a combination with phenol, but these produce resins which give inferior results compared to the results given by resins produced from phenol itself. P-cresol for example, can only form phenol-aldehyde molecules in which the phenolic residues are linked by ortho-ortho methylene bridges and the molecules can therefore only complex with the oxyanions at their ends.

The aldehyde may be for example, formaldehyde, butyraldehyde, glyoxal or furfuraldehyde. Formaldehyde is preferred.

The resol phenol-aldehyde resin is preferably produced by the condensation of the phenol and the aldehyde in the presence of a base catalyst which may be for example ammonium hydroxide or an alkali metal hydroxide such as sodium hydroxide or potassium hydroxide. Alkali metal hydroxide catalysts are preferred because they produce a resin in which the phenolic residues are linked predominantly by ortho-para or para-para methylene bridges and from which phenolic residues linked by ortho-ortho methylene bridges are essentially absent.

Other catalysts, such as zinc acetate, may be used, either on their own or in combination with an alkali metal hydroxide. However, catalysts such as zinc acetate are less desirable because they yield resins having a mixed bridging structure containing ortho-ortho benzylic ether bridges and ortho-para methylene bridges, and hence a reduced capacity for complexing with the oxyanions.

The mole ratio of aldehyde (expressed as formaldehyde) to phenol in the resin may be in the range of from 1:1 to 3:1 but is preferably in the range from 1.6:1 to 2.5:1.

The resol phenol-aldehyde resin used in the process and binder composition of the invention preferably has an intrinsic viscosity in the range of from 4.0 to 7.5 cm.sup.3.g.sup.-1 more preferably in the range of from 4.5 to 7.0 cm.sup.3.g.sup.-1.

The viscosity of a liquid is its resistance to flow and when measured by flow of the liquid through a capillary the viscosity is given by the formula. ##EQU1## where .eta. is the viscosity and t is the time taken for a volume V to pass through a capillary of length l and radius r at an external pressure P.

When using a given capillary with the same volume of liquid passing through, and liquids of similar density, the viscosity is directly proportional to the flow time. Thus for a solution of a resin in a solvent the specific viscosity .eta. sp is defined as ##EQU2## where .eta. solution is the viscosity of the resin solution, .eta. solvent is the viscosity of the solvent used to dissolve the resin, ts is the flow time of the resin solution and to is the flow time of the solvent.

The specific viscosity of the resin is dependent on its concentration according to the formula ##EQU3## where c is the concentration of the resin in the solution, A and B are constants and .eta..sub.o is the intrinsic viscosity.

If the specific viscosities of a series of solutions of different concentrations are measured and a graph of .eta. sp/c against c is plotted, a straight line is obtained the intercept on the .eta. s/c axis being the intrinsic viscosity of the resin.

After production the resol phenol-aldehyde resin is made alkaline by the addition of, for example, sodium hydroxide or potassium hydroxide, which is conveniently added as an aqueous solution. The preferred alkali is potassium hydroxide because it results in a binder composition having a lower viscosity for a given degree of polymerization of the resin compared to sodium hydroxide and the performance of the binder composition is superior.

The molar ratio of the total alkali present in the binder (expressed as hydroxyl ions) to phenol is preferably in the range of 0.5:1 to 3.0:1, more preferably 1.5:1 to 2.5:1. The total alkali includes any alkali used as catalyst in the synthesis of the resin, any additional alkali which may be added during the synthesis and alkali added after synthesis of the resin and during manufacture of the binder.

Examples of suitable oxyanions for use in the process and binder composition of the invention include borate, stannate and aluminate ions. Borate ions are preferred.

The oxyanion may be introduced into the binder composition by the addition of for example alkali metal oxyanion salts such as sodium tetraborate decahydrate, potassium tetraborate tetrahydrate, sodium metaborate, sodium pentaborate, sodium stannate trihydrate or sodium aluminate, or an ammonium oxyanion salt such as ammonium borate. Borate ions may also be introduced by the addition of boric acid or they may be formed by reaction between added boric oxide and alkali in the binder solution.

The mole ratio of oxyanions (expressed as boron, tin etc.) to phenol is preferably in the range of from 0.1:1 to 1:1. When the oxyanion is borate the mole ratio of boron to phenol is more preferably in the range of from 0.3:1 to 0.6:1.

The binder composition preferably also contains a silane such as gamma-aminopropyltriethoxysilane, phenol trimethoxysilane or gammaglycidoxypropyltrimethoxysilane usually in an amount of 0.2% to 1.0% by weight.

If desired an additional solvent such as methanol or ethanol may be included in the binder composition.

Although other methods may be used the preferred method of manufacturing the binder of the invention is as follows:

Phenol is melted and formaldehyde (as paraformaldehyde) and the alkali metal hydroxide catalyst solution are then added. A resol phenolformaldehyde is then produced by polymerisation of the phenoland formaldehyde in two or more heating stages over a range of temperatures from about 60.degree. C. to about 95.degree. C. The degree of polymerisation of the resin is monitored by measuring the viscosity of a diluted sample of the resin towards the end of the process. The final resin is cooled, alkali is added as alkali metal hydroxide solution and the oxyanions are added. The binder composition obtained is finally cooled and the silane added.

When the binder composition is used to produce foundry moulds or cores from particulate refractory materials the particulate refractory material may be selected from any such materials known for that use. Examples of suitable materials include silica, olivine, chromite and zircon sands.

The quantity of binder composition used will usually be from 1% to 10% by weight, preferably 1.5% to 5% by weight based on the weight of the particulate refractory material.

By means of the process of the invention foundry moulds and cores may be produced, ready for use in metal casting, in a very short time.

The following examples will serve to illustrate the invention:

EXAMPLE 1

A series of five resol phenol-formaldehyde resins was synthesized having an increasing molar ratio of formaldehyde to phenol (F:P) ranging from 3.0:1 to 2.0:1 using sodium hydroxide as catalyst. The compositions of the resins are tabulated in Table 1 below.

TABLE 1______________________________________ Mass/gComponent 1A 1B 1C 1D 1E______________________________________Phenol 800 800 800 800 80091% w/w para 284.3 364.7 348.8 701.3 841.6formaldehyde50% w/w 40.85 40.85 40.85 40.85 40.85aqueous NaOHMolar F:P 1.01:1 1.3:1 1.6:1 2.5:1 3.0:1Molar OH-:P 0.06:1 0.06:1 0.06:1 0.06:1 0.06:1% water in 4.1 4.4 4.7 5.4 5.7startingcomposition______________________________________

The following procedure was used:

1. Charge and melt phenol. 2. Charge paraformaldehyde and sodium hydroxide solution and heat to 65.degree. C. at a rate of 1.degree. C. per minute. 3. Cool to counteract exothermic reaction and maintain at 65.degree. C. for 1 hour. 4. Heat to 75.degree. C. at a rate of 1.degree. C. per minute. 5. Maintain at 75.degree. C. for 30 minutes. 6. Heat to 85.degree. C. at a rate of 1.degree. C. per minute. 7. Maintain at 85.degree. C.

The resins were maintained at 85.degree. C. for sufficient time for each of them to reach the same viscosity range of 4000-6000 cps at 25.degree. C. measured using Paint Research Association Bubble Viscosity Tubes on a 25 g sample diluted with 15 g of 50% w/w potassium hydroxide solution. Resin 1A was maintained at 85.degree. C. for 320 minutes, resin 1B for 280 minutes, resin 1C for 240 minutes, resin 1D for 170 minutes and resin 1E for 150 minutes.

The base resins were used to produce a series of binders of different alkalinity as shown in Table 2 below.

TABLE 2______________________________________F:P Mass/g Molar Base 50% w/w All02Binder Ratio Resin KOH Borax Silane______________________________________1 AA 1.01:1 25 30 5.0 0.391 AB 25 35 5.0 0.391 AC 25 40 5.0 0.391 BA 1.3:1 25 30 5.0 0.391 BB 25 35 5.0 0.391 BC 25 40 5.0 0.391 CA 1.6:1 25 30 5.0 0.391 CB 25 35 5.0 0.391 CC 25 40 5.0 0.391 DA 2.5:1 25 30 5.0 0.391 DB 25 35 5.0 0.391 DC 25 40 5.0 0.391 EA 3.0:1 25 30 5.0 0.391 EB 25 35 5.0 0.391 EC 25 40 5.0 0.39______________________________________

In each case the required amount of potassium hydroxide solution was added to the base resin, the temperature rise due to exothermic reaction was controlled and the resin was cooled. The borax (sodium tetraborate decahydrate) was added and mixed into the resin until it had dissolved. The silane was then added at a temperature of below 30.degree. C.

The binders were tested as binders for foundry sand using the following procedure:

The binder was mixed with 2.0 kg of Chelford 60 sand (AFS Fineness No. 55) and the mixture was used to prepare standard AFS 50 mm.times.50 mm diameter cylindrical cores. In each case the quantity of binder used was such that a constant mass (22.72 g) of base resin was deposited on 2 kg of sand. The cores were hardened by the passage of carbon dioxide gas for various times at a temperature of 20.degree.-25.degree. C., a 0.35 kg/cm.sup.2 line pressure and a 6.0 liters per minute flow rate. The compression strength of the hardened cores was measured immediately after gassing on a Ridsdale Universal Compression tester.

The OH.sup.- :P molar ratio and mass of binder used and the results obtained are tabulated in Table 3 below.

TABLE 3______________________________________ Mass Compression StrengthOH.sup.- :P Deposited (kg .multidot. cm.sup.-2) For GassingMolar on sand Period (seconds)Binder Ratio (g) 30 60 120______________________________________AA 1 48:1 54.88 4.9 6.3 7.41 AB 1.71:1 59.43 4.2 5.9 7.01 AC 1.95:1 63.97 3.4 5.0 6.41 BA 1.58:1 54.88 4.6 5.5 6.51 BB 1.83:1 59.43 4.9 5.9 7.01 BC 2.09:1 63.97 4.2 5.5 6.21 CA 1.68:1 54.88 3.8 4.9 6.01 CB 1.95:1 59.43 4.9 6.1 7.21 CC 2.22:1 63.97 4.4 5.0 6.21 DA 2.00:1 54.88 12.7 14.8 17.31 DB 2.32:1 59.43 14.1 17.5 18.81 DC 2.65:1 63.97 13.8 16.0 18.01 EA 2.19:1 54.88 13.0 14.8 16.21 EB 2.54:1 59.43 14.8 16.6 18.51 EC 2.89:1 63.97 13.7 16.1 17.3______________________________________

The results show that throughout the range of F:P molar ratios from 1.01:1 to 3.0:1 the resin can be cured by carbon dioxide gas and that there is a marked increase in the compression strength of the cores obtained between a molar ratio of F:P of 1.6:1 and 2.5:1. The results also indicate that the polymer backbone should be fully methylolated for optimum performance. For a methylene bridged polymer the maximum F:P ratio is 2N+1:N where N is the number of phenolic residues per molecule.

At high degrees of polymerisation the maximum formaldehyde incorporation level tends to a F:P ratio of 2.0:1. Very high F:P reaction ratios (of the order of 3.0:1) therefore lead to large amounts of unincorporated formaldehyde and hence reduced masses of useful binder.

EXAMPLE 2

Three series of resol phenol-formaldehyde resins, series 2A, 2B and 2C, having molar ratios of formaldehyde to phenol (F:P) of 1.6:1, 2.3:1 and 2.5:1 respectively were synthesized using a similar procedure to that described in Example 1 but ending at step 5. For each series reaction times at step 5 ranged from 4 to 9 hours.

Series 2A had the same composition as Resin 1C of Example 1 and series 2C had the same composition as Resin 1D of Example 1. Series 2B had the following composition:

______________________________________phenol 800.00 g91% w/w paraformaldehyde 642.20 g50% w/w sodium hydroxide 40.85 gsolutionF:P molar ratio 2.3:1OH.sup.- :P molar ratio 0.06:1water in starting 5.2% w/wcomposition______________________________________

The intrinsic viscosity of each of the resins was determined using the following procedure.

Approximately 3 g of the resin were accurately weighed in a weighing bottle and dissolved in 15 cm.sup.3 of methanol. The resulting solution was transferred to a graduated flask and made up to 25 cm.sup.3 with methanol. The flask was inverted to thoroughly mix the solution and the added methanol. The weighing bottle was allowed to stand to allow any methanol remaining in it to evaporate and weighed periodically until it had reached constant weight, thus giving an accurate measure of the amount of sample actually used and accounting for any sample left on the surface of the weighing bottle. The difference between the final weight of the bottle and the initial weight was used to calculate the concentration of the sample in the solution. To adjust the sample concentration to give the actual concentration of resin in the solution a quantity of each sample was placed in a preweighed weighing bottle and heated at 100.degree. C. until constant weight was achieved. Volatiles were thus driven off and an accurate measure of the percentage of resin in the sample was obtained. The concentrations of the sample solutions were adjusted accordingly.

A suspended level Ubbelholde dilution viscometer was used to measure the viscosity of the solutions. Prior to use and before changing samples the viscometer was soaked overnight in concentrated nitric acid, thoroughly washed with filtered distilled water, then with methanol and finally with acetone. The viscometer was then allowed to dry.

The viscometer was submerged in a water bath maintained at 23.80.degree. C..+-.0.1.degree. C. A chrome-aluminel thermocouple placed inside the viscometer and connected to a chart recorder was used to determine when the temperature of the resin solution had reached the temperature of the water bath and to ensure that during a viscosity measurement the temperature did not vary by more than 0.1.degree. C.

As it was found that the 2.3:1 and 2.5:1 F:P molar ratio resins behaved as polyelectrolytes rather than as uncharged polymer chains due to the presence of hydroxide ions in the resin all samples were neutralized before viscosity determinations were done. To prevent the precipitation of the resin which would occur if aqueous acid solutions were used for neutralization dry hydrogen chloride gas, passed through concentrated sulfuric acid and over calcium chloride, was bubbled through the solution until the pH was reduced to 7.

5 cm.sup.3 of sample were pipetted into the viscometer and once the thermocouple reading was constant a measurement was made by timing the flow time of the sample between the graduations of the viscometer. The measurement was repeated 5 times and the measurements were averaged. The sample solution was then diluted with methanol which was thoroughly mixed with the solution by bubbling nitrogen through the mixture. Measurements were then made and the results averaged. This was repeated so that measurements were made on each resin at four dilutions. Finally the flow time of the solvent methanol was measured at a range of temperatures from 23.70.degree. to 23.90.degree. C. so that the correct value of the flow time for methanol could be used for each flow time of the solution for determining the specific viscosity of the samples.

The 2.3:1 and 2.5:1 F:P molar ratio resin samples were diluted with 2 cm.sup.3 of methanol each time the sample was diluted and further measurements were made. In the case of the 1.6:1 F:P molar ratio resins it was found that at low concentrations the solutions began to exhibit polyelectrolyte behaviour. So that the viscometer measurements could be used to produce an accurate value of the specific viscosity, a restricted concentration range was therefore used and each time a sample was diluted 1 cm.sup.3 of methanol was used instead of 2 cm.sup.3.

For each resin sample at each dilution the specific viscosity (solution flow time minus methanol flow time divided by methanol flow time) was calculated and the intrinsic viscosity for each resin sample was then determined by plotting the specific viscosity divided by the concentration against concentration and extrapolation to zero.

The results obtained in the form of intrinsic viscosity plotted against reaction time at 75.degree. C. (i.e. at step 5 in the resin synthesis procedure) are shown in FIG. 1 of the accompanying diagrammatic drawings.

The series 2B resins which had the widest intrinsic viscosity range were used to produce a series of binder compositions according to the procedure described in Example 1. The composition of the binders is shown in Table 4 below.

TABLE 4______________________________________Reactiontime at Mass/g 75.degree. C. Base 50% w/w All02Binder (Hours) Resin KOH Borax Silane______________________________________2 BA 4 25 35 5.0 0.392 BB 6 25 35 5.0 0.392 BC 8 25 35 5.0 0.392 BD 9 25 35 5.0 0.39______________________________________

Each of the binders was tested using the procedure described in Example 1. In each case the quantity of binder used was such that a constant mass (22.72 g) of base resin was deposited on 2 kg sand, and cores were gassed for 30, 60 and 120 seconds with carbon dioxide.

The boron to phenol molar ratio (B:P), the mass of binder used and the results obtained are tabulated in Table 5 below. The results are also shown graphically in FIG. 2 of the drawings in the form of compression strength of the test cores plotted against resin reaction time at 75.degree. C. for three different carbon dioxide gassing times.

TABLE 5______________________________________ MassBoron: deposited Compression strength/Phenol on 2 kg kg cm.sup.-2 for GassingMolar CHELFORD PeriodRatio 60 sand 30s 60s 120s______________________________________2 BA 0.36:1 59.42 g 11.5 12.5 13.02 BB 0 36:1 59.42 g 15.1 17.0 18.52 BC 0.36:1 59.42 g 14.0 16.0 17.52 BD 0.36:1 59.42 g 11.5 14.0 15.4______________________________________

The results indicate that adequate test core compression strength is achieved using resins which have been reacted for between 4 and 9 hours at step 5 in the synthesis procedure, with optimum strengths being obtained using resins which have been reacted for between 5 and 8 hours at step 5. As can be seen from FIG. 1 reaction times at step 5 of 4 to 9 hours correspond to intrinsic viscosities of the resin of about 4.7 to 7.5 cm.sup.3.g.sup.-1 and reaction times at step 5 of 5 to 8 hours correspond to intrinsic viscosities of about 5.0 to 6.5 cm..sup.3 g.sup.-1.

EXAMPLE 3

A base resin of the same composition as the series 2B resin of Example 2 was synthesized.

The base resin was synthesized using the procedure described in Example 1 and was maintained at a temperature of 85.degree. C. at step 7 for 190 minutes. The viscosity of the base resin was in the range 4000-6000 cps at 25.degree. C. measured using the procedure described in Example 1.

The base resin was used to produce a series of binders of different levels of alkalinity as shown in Table 6 below.

TABLE 6______________________________________Mass/9 Base 50% w/w All02Binder Resin KOH Borax Silane______________________________________3A 25 15 5.0 0.393B 25 20 5.0 0.393C 25 25 5.0 0.393D 25 30 5.0 0.393E 25 35 5.0 0.393F 25 40 5.0 0.393G 25 45 5.0 0.393H 25 50 5.0 0.39______________________________________

Each of the binders was tested using the procedure described in Example 1. In each case the quantity of binder used was such that a constant mass (22.72 g) of base resin was deposited on 2 kg sand and the cores were gassed for 120 seconds.

The OH.sup.- :P ratio and mass of binder used and the results obtained are tabulated in Table 7 below.

TABLE 7______________________________________ Mass deposited Compression OH.sup.- :P on 2 kg CHELFORD Strength/kg cm.sup.-2Binder Ratio 60 sand Gassing Period 120 s______________________________________3A 1.00:1 41.25 g 03B 1.31:1 45.79 g 03C 1.62:1 50.33 g 14.63D 1.93:1 54.88 g 18.43E 2.25:1 59.43 g 19.13F 2.56:1 63.97 g 18.43G 2.87:1 68.51 g 19.53H 3.18:1 73.06 g 18.2______________________________________

The results indicate that for the particular binder compositions tested OH.sup.- :P molar ratios above about 1.8 yield the optimum binder performance.

Binders 3A and 3B were very viscous and formed very "dry" mixtures with sand with the result that the test cores had compression strengths which were too low for any reading to be recorded on the equipment used.

Binders of the same composition as binders 3A and 3B were therefore prepared from a similar base resin and further diluted with water, methanol and/or 50% w/w aqueous potassium hydroxide.

The binders were tested using the procedure described in Example 1. In each case the quantity of binder used was 59.4 g so that 22.72 g base resin were deposited on 2 kg of Chelford 60 sand.

The composition of the binders and the results obtained are tabulated in Table 8 below. Tests were also made using a binder (3K) having the same composition as binder 3E for comparison.

TABLE 8______________________________________ Mass/gCOMPOSITION 3I 3J 3K 3L 3M______________________________________Base Resin 25.0 25.0 25.0 25.0 25.050% w/w KOH 15.0 20.0 35.0 15.0 25.0Water 20.0 15.0 -- -- --Methanol -- -- -- 20.0 10.0Borax 5.0 5.0 5.0 5.0 5.0All02Silane 0.39 0.39 0.39 0.39 0.39______________________________________GASSINGPERIOD COMPRESSION STRENGTH (Kg .multidot. cm.sup.-2)______________________________________ 30s 14.8 15.8 15.8 7.4 13.7 60s 13.5 15.6 17.0 9.1 15.1 120s 13.5 15.8 18.5 10.5 16.6______________________________________

Dilution with water gave compression strengths which were approximately 75-90% of those obtained when diluting with 50% w/w KOH solution. Dilution with methanol gave more viscous binders than those diluted with water. The compression strengths were 60-90% of those obtained when diluting with 50% w/w KOH solution.

EXAMPLE 4

The base resin of Example 3 was used to produce a series of binders of different borate ion contents using the procedure described in Example 1. The composition of the binders is shown in Table 9 below.

TABLE 9______________________________________Mass/g All02Binder Base Resin 50% KOH Borax Silane______________________________________4 A 25 35 0 0.394 B 25 35 2 0.394 C 25 35 3 0.394 D 25 35 4 0.394 E 25 35 5 0.394 F 25 35 6 0.394 G 25 35 7 0.394 H 25 35 8 0.394 I 25 35 10 0.39______________________________________

In each case the borate ions were added as sodium tetraborate decahydrate.

The binders were tested as described in Example 1 and as in Example 1, the quantity of binder used was such that 22.72 g of base resin were deposited on 2 kg of sand.

The boron to phenol molar ratio (B:P), the mass of binder used and the results obtained are tabulated in Table 10 below.

TABLE 10______________________________________ Compression Mass deposited Strength/kg cm.sup.-2 Boron:phenol on 2 kg CHELFORD Gassing PeriodBinder Molar Ratio 60 sand 120 s______________________________________4 A 0.00:1 54.88 g 04 B 0.15:1 56.70 g 9.74 C 0.22:1 57.61 g 14.34 D 0.29:1 58.52 g 17.04 E 0.36:1 59.43 g 19.04 F 0.44:1 60.34 g 18.44 G 0.51:1 61.24 g 18.14 H 0.59:1 62.16 g 17.34 I 0.73:1 63.97 g 16.6______________________________________

The binder containing no borate ions did not cure on gassing with carbon dioxide. The optimum compression strengths were achieved using binders containing a molar ratio of B:P of about 0.3:1 to about 0.6:1.

EXAMPLE 5

The base resin of Example 3 was used to produce a series of binders of different silane contents using the procedure described in Example 1. The composition of the binders is shown in Table 11 below.

TABLE 11______________________________________Mass/g All02Binder Base Resin 50% KOH Borax Silane______________________________________5 A 25 35 5.0 0.005 B 25 35 5.0 0.155 C 25 35 5.0 0.395 D 25 35 5.0 0.455 E 25 35 5.0 0.60______________________________________

The binders were tested as described in Example 1 and as in Example 1, the quantity of binder used was such that 22.72 g of base resin were deposited on 2 kg of sand. Three series of tests were carried out for gassing times of 30 seconds, 60 seconds and 120 seconds.

The silane content of the binder and the mass of binder used and the results obtained are tabulated in Table 12 below.

TABLE 12______________________________________ Mass% Silane depositedin on 2 kg Compression Strength/kgbinder CHELFORD cm.sup.-2 for Gassing PeriodBinder w/w 60 sand 30 s 60 s 120 s______________________________________5 A 0.00 59.07 g 4.4 5.3 6.75 B 0.23 59.21 g 11.6 13.4 16.55 C 0.60 59.43 g 15.4 16.7 18.55 D 0.69 59.47 g 15.2 18.6 19.35 E 0.91 59.62 g 14.3 17.7 19.1______________________________________

The addition of silane to the binder produces a considerable improvement in binder performance. High compression strengths were observed for silane addition levels above 0.2% w/w.

EXAMPLE 6

The base resin of Example 3 was used to prepare two binder compositions containing borate ions from two different sources, borax (sodium tetraborate decahydrate) and potassium tetraborate tetrahydrate.

The composition of the binders is shown in Table 13 below.

TABLE 13______________________________________ BINDER 6A BINDER 6BSource of Borate ion Na.sub.2 B.sub.4 O.sub.7.10H.sub.2 O K.sub.2 B.sub.4 O.sub.7.4H.sub.2 OFormula Weight 381.37 305.5______________________________________Resin 25 g 25 g50% KOH 35 g 35 gBorate ion source 5.5 g 4.41 gSilane (A1102) 0.39 g 0.39 g______________________________________

The binders were tested as described in Example 1 and as in Example 1, the quantity of binder used was such that 22.72 g of base resin were deposited on 2 kg of sand. In each case the quantity of the borate source was such that 0.058 moles of boron were deposited on 2 kg of sand. Thus in each case the same amount of boron was available for complexing.

The mass of binder used and the results obtained are tabulated in Table 14 below.

TABLE 14______________________________________ Mass deposited on 2 kg Compression StrengthSource of CHELFORD kg cm.sup.-2Binder Borate ion 60 sand 30 s 60 s 120 s______________________________________6A Na.sub.2 B.sub.4 O.sub.7.10H.sub.2 O 59.88 g 12.2 15.7 18.16B K.sub.2 B.sub.4 O.sub.7.4H.sub.2 O 58.89 g 14.1 16.7 17.2______________________________________

Both sodium tetraborate decahydrate and potassium tetraborate tetrahydrate yield similar results when used at equivalent boron addition levels.

EXAMPLE 7

Two series of binders were prepared using the base resin of Example 3, one series containing various amounts of boric acid and the other various amounts of sodium metaborate tetrahydrate. Each binder contained the same amount of potassium hydroxide and the same amount of A1102 silane.

The composition of each of the binders is tabulated in Tables 15 and 16 below.

TABLE 15______________________________________Mass/g Sodium Base Metaborate A1102 B:P MolarBinder Resin 50% KOH Tetrahydrate Silane Ratio______________________________________7A 25 35 3.0 0.39 0.15:17B 25 35 4.0 0.39 0.20:17C 25 35 5.0 0.39 0.25:17D 25 35 6.0 0.39 0.30:17E 25 35 7.0 0.39 0.35:17F 25 35 8.0 0.39 0.40:1______________________________________ TABLE 16______________________________________Mass/g Base Boric A1102 B:P MolarBinder Resin 50% KOH Acid Silane Ratio______________________________________7G 25 35 1.0 0.39 0.11:17H 25 35 2.0 0.39 0.23:17I 25 35 3.0 0.39 0.34:17J 25 35 4.0 0.39 0.45:17K 25 35 5.0 0.39 0.56:17L 25 35 6.0 0.39 0.68:1______________________________________

The binders were tested as described in Example 1 and as in Example 1, the quantity of binder used was such that 22.72 g of base resin were deposited on 2 kg of sand A similar binder (7M) containing an optimized level of borax (5.5 g borax, B:P molar ratio 0.40:1) was used as the comparison standard for each series.

The boron to phenol ratio (B:P) and mass of binder used and the results obtained are tabulated in Table 17 below.

TABLE 17______________________________________ MassB:P deposited on Compression Strength/Molar 2 kg CHELFORD kg cm.sup.2 for Gassing PeriodBinder Ratio 60 Sand 30 s 60 s 120 s______________________________________7A 0.15:1 57.61 7.2 6.8 6.37B 0.20.1 58.52 8.4 10.5 10.77C 0.25:1 59.43 12.2 12.7 12.87D 0.30:1 60.34 13.5 15.1 16.27E 0.35:1 60.24 15.0 16.3 17.57F 0.40:1 62.15 14.8 15.6 17.87M 0.40:1 59.88 13.7 15.8 18.17G 0.11:1 55.79 3.0 2.7 3.07H 0.23:1 56.70 10.5 11.1 10.97I 0.34:1 57.61 11.6 13.9 16.57J 0.45:1 58.52 11.2 11.4 13.47K 0.56:1 59.43 9.7 10.3 12.67L 0.68:1 60.34 9.9 12.6 12.77M 0.40:1 59.88 12.6 15.2 17.2______________________________________

From the results obtained in Example 7 and from those obtained in Example 4 it is apparent that the choice of source of borate ions does not significantly affect the strength of the cured resin-bonded sand cores attainable. Although borax-, sodium metaborate tetrahydrate- and boric acid-containing binders show optimum performance at different weight levels of the borate source, the optimum molar B:P ratio for all three sources is comparable.

EXAMPLE 8

The base resin of Example 3 was used to prepare two series of binder compositions, one series containing sodium stannate dihydrate as the source of oxyanions and the other sodium aluminate (Fison technical grade). Two binders containing no oxyanion were also prepared for comparison.

The composition of the binders is shown in Table 18 below

TABLE 18______________________________________Mass/g Base 50% Sodium Sodium A1102Binder Resin KOH w/w Stannate Aluminate Silane______________________________________8A 25 35 0 -- 0.398B 25 35 3 -- 0.398C 25 35 4 -- 0.398D 25 35 5 -- 0.398E 25 35 6 -- 0.398F 25 35 7 -- 0.398G 25 35 -- 0 0.398H 25 35 -- 3 0.398I 25 35 -- 4 0.398J 25 35 -- 5 0.398K 25 35 -- 6 0.398L 25 35 -- 7 0.39______________________________________

The binders were tested as described in Example 1 and as in Example 1, the quantity of binder used was such that 22.72 g of base resin were deposited on 2 kg of sand.

The Sn:P or Al:P molar ratio and mass of binder used and the results obtained are tabulated in Table 19 below.

TABLE 19______________________________________ Mass deposited Compression Sn:P or Al:P 2 kg CHELFORD Strength (Kg .multidot. cm.sup.-2)Binder Molar Ratio 60 sand Gassing period 120 s______________________________________8A 0.00:1 54.88 08B 0.08:1 57.61 7.68C 0.11:1 58.52 8.48D 0.13:1 59.43 8.98E 0.16:1 60.34 8.68F 0.18:1 61.24 8.98G 0.00.1 54.88 08H 0.22:1 57.61 4.48I 0.29:1 58.52 5.08J 0.36:1 59.43 5.18K 0.44:1 60.34 5.38L 0.51:1 61.24 4.9______________________________________

The results show that stannate ions or aluminate ions can be used as alternatives to borate ions in the binder compositions of the invention.

EXAMPLE 9

A resol p-cresol-formaldehyde resin was prepared having a formaldehyde-p-cresol (F:P) molar ratio of 1.5:1. Only low F:p-cresol molar ratios are possible because the para position on

______________________________________p-cresol 800 g91% w/w paraformaldehyde 366.3 g50% w/w sodium hydroxide 40.85 gsolutionF:p-cresol molar ratio 1.5:1OH.sup.- :p-cresol molar ratio 0.07:1water in starting 4.4% w/wcomposition______________________________________

The procedure used was that described in Example 1 and at step 7 the resin was maintained at 85.degree. C. for 300 minutes. The viscosity of the resin measured as described in Example 1 was in the range of 3500-5000 cps at 25.degree. C.

The resin was used to prepare a series of binder compositions containing different levels of borate ions as described in Examples 1 and 4. The compositions are tabulated in Table 20 below.

TABLE 20______________________________________ Mass/g Base 50% w/w A1102Binder Resin KOH Borax Silane______________________________________9 A 25 35 0 0.399 B 25 35 4 0.399 C 25 35 5 0.399 D 25 35 6 0.399 E 25 35 7 0.39______________________________________

The binders were tested as described in Example 1. The quantity of binder used was such that 22.72 g of base resin were deposited on 2 kg of Chelford 60 sand and the cores were gassed for 120 seconds with carbon dioxide.

The boron to p-cresol molar ratio (B:P), the mass of binder used and the results obtained are tabulated in Table 21 below.

TABLE 21______________________________________ Compression B:P Mass deposited on strength (kg .multidot. cm.sup.-2) Molar 2 kg Chelford 60 Gassing periodBinder Ratio sand 120 s______________________________________9 A 0.00:1 54.88 09 B 0.27:1 58.52 6.39 C 0.33:1 59.43 7.79 D 0.40:1 60.34 7.69 E 0.47:1 61.24 6.5______________________________________

Example 9 when compared with Example 4 shows that although useful binders can be obtained from substituted phenols such as p-cresol the properties of the binders are inferior to those of similar binders obtained from phenol due to the fact that the p-cresol-formaldehyde resins contain only ortho-ortho linkages and the molecules can only complex with borate ions at their ends.

EXAMPLE 10

A resol phenol-formaldehyde having the following composition was prepared using zinc acetate dihydrate as catalyst:

______________________________________Phenol 800 g91% w/w paraformaldehyde 642.2 gzinc acetate dihydrate 111.9 gwater 6.1 gmolar F:P ratio 2.3:1molar zinc acetate:P ratio 0.06:1% water in starting 5.3 w/wcomposition______________________________________

The procedure used was as described in Example 1 as far as step 5. Thereafter the resin was heated to 90.degree. C. at a rate of 1.degree. C. per minute and maintained at 90.degree. C. for 270 minutes.

The viscosity of the base resin obtained, measured as described in Example 1, was in the range 3000-5000 cps at 25.degree. C.

The resin was used to prepare a series of binder compositions containing different levels of borate ions as described in Examples 1 and 4. The compositions are tabulated in Table 22 below.

TABLE 22______________________________________Mass/g Base 50% w/w A1102Binder Resin KOH Borax Silane______________________________________10 A 25 35 0 0.3910 B 25 35 4 0.3910 C 25 35 5 0.3910 D 25 35 6 0.3910 E 25 35 7 0.39______________________________________

The binders were tested as described in Example 1. The quantity of binder used was such that 22.72 g of base resin were deposited on 2 kg of Chelford 60 sand, and the cores were gassed for 120 seconds with carbon dioxide.

The boron to phenol molar ratio (B:P), the mass of binder used and the results obtained are tabulated in Table 23 below.

TABLE 23______________________________________ Compression Mass deposited strength kg/cm.sup.-2 B:P on 2 kg Chelford Gassing PeriodBinder Molar Ratio 60 sand 120 s.______________________________________10 A 0.00:1 54.88 g 010 B 0.29:1 58.52 g 4.810 C 0.36:1 59.43 g 5.110 D 0.44:1 60.34 g 4.310 E 0.51:1 61.24 g 4.2______________________________________

Example 9 when compared with Example 4 shows that although useful binders can be obtained using zinc acetate catalyzed resol phenol-formaldehyde resins the properties of the binders are inferior to those of similar binders obtained using alkali catalyzed resol phenol-formaldehyde resins due to the reduced capacity in the zinc acetate catalyzed resins for complexing with borate ions.

Claims

1. A process for the production of an article of bonded particulate material comprising the steps of:

(a) forming to a desired shape a mixture comprising particulate material and a binder comprising an alkaline aqueous solution of a resol phenol-aldehyde resin and an oxyanion capable of forming a stable complex with the resin, the amount of alkyl present in the solution being sufficient to solubilize the resin and to prevent a stable complex formation between the resin and the oxyanion, and the amount of oxyanion present being sufficient to cure the resin when stable complex formation is permitted to take place; and (b) passing carbon dioxide gas through the formed shape to reduce the alkalinity of the solution so as to cause the oxyanion to form a stable complex with the resin and thereby to cure the resin.

2. A process according to claim 1 wherein the mixture contains 1% to 10% by weight of the binder based on the weight of the particulate material.

3. A process according to claim 2 wherein the mixture contains 1.5% to 5% by weight of the binder based on the weight of the particulate material.

4. A process as recited in claim 1 wherein said forming step is practiced by providing the phenol as phenol itself, a substituted phenol such as p-cresol or m-cresol, or a phenolic compound such as p-phenol sulphonic acid.

5. A process as recited in claim 1 wherein said forming step is practiced by providing the aldehyde as formaldehyde, butyraldehyde, glyoxal or furfuraldehyde.

6. A process as recited in claim 1 wherein said forming step is practiced by providing as the phenol-aldehyde resin one produced by condensation in the presence of a base catalyst.

7. A process as recited in claim 1 wherein said forming step is practiced by providing the molar ratio of aldehyde (expressed as formaldehyde) to phenol in the resin as from 1:1 to 3:1.

8. A process as recited in claim 7 wherein said forming step is practiced by providing the molar ratio of aldehyde (expressed as formaldehyde) to phenol in the resin as from 1.6:1 to 2.5:1.

9. A process as recited in claim 1 wherein said forming step is practiced by providing the phenol-aldehyde resin as one having an intrinsic viscosity of from 4.0 to 7.5 cm.sup.3.g.sup.-1.

10. A process as recited in claim 9 wherein said forming step is practiced by providing the phenol-aldehyde resin as one having an intrinsic viscosity of from 4.5 to 7.0 cm.sup.3.g.sup.-1.

11. A process as recited in claim 1 wherein said forming step is practiced by providing the phenol-aldehyde resin as one containing predominantly molecules in which adjacent phenolic residues are linked together by methylene groups forming bridges between the ortho and para positions.

12. A process as recited in claim 11 wherein said forming step is practiced by providing all the available positions on the phenolic residues which are ortho to the phenolic hydroxyl group in an ortho-para methylene bridged molecule as methylolated ones.

13. A process as recited in claim 1 wherein said forming step is practiced by providing the molar ratio of alkali (expressed as hydroxyl ions) to phenol as from 0.5:1 to 3.0:1.

14. A process as recited in claim 1 wherein said forming step is practiced by providing the molar ratio of alkali (expressed as hydroxyl ions) to phenol as from 1.5:1 to 2.5:1.

15. A process as recited in claim 1 wherein said forming step is practiced by providing the oxyanion as borate, stannate or aluminate.

16. A process as recited in claim 15 wherein said forming step is practiced by providing as the oxyanion an alkali metal borate, stannate or aluminate.

17. A process as recited in claim 16 wherein said forming step is practiced by providing as the oxyanion sodium tetraborate decahydrate, potassium tetraborate tetrahydrate, sodiummetaborate, sodium pentaborate, ammonium borate, sodium stannate trihydrate or sodium aluminate.

18. A process as recited in claim 15 wherein said forming step is practiced by providing as the borate, boric acid.

19. A process as recited in claim 15 wherein said forming step is practiced by providing the borate by reaction between boric oxide and alkali present in the binder.

20. A process as recited in claim 1 wherein said forming step is practiced by providing the molar ratio of oxyanion (expressed as the element forming the oxyanion with oxygen) to phenol as from 0.1:1 to 1.0:1.

21. A process as recited in claim 1 wherein said forming step is practiced by providing the oxyanion as borate, and the molar ratio of boron to phenol from 0.3:1 to 0.6:1.

22. A process as recited in claim 1 wherein said forming step is practiced by providing, in addition, a silane.

23. A process as recited in claim 22 wherein said forming step is practiced by providing the silane as gamma-aminopropyltriethoxysilane, phenol trimethoxysilane or gammaglycidoxypropyltrimethoxysilane.

24. A process as recited in claim 1 wherein the particulate material is sand, and wherein steps (a) and (b) are practiced to form the sand into a foundry mold or core.

25. A process as recited in claim 24 wherein step (a) is practiced to provide a mixture which contains 1-10% by weight of the binder based upon the weight of the particulate material.

26. A process as recited in claim 25 wherein step (a) is further practiced so that the mixture contains 1.5%-5% by weight of the binder based on the weight of the particulate material.