EP1414901A1

EP1414901A1 - Resol-based co 2-hardenable binding agent system

Info

Publication number: EP1414901A1
Application number: EP02754350A
Authority: EP
Inventors: H-J. Aschland-Südchemie-Kernfest Gmbh SCHWAACK; D. c/o Aschland-Südchemie-Kernfest GmbH KOCH
Original assignee: Ashland Suedchemie Kernfest GmbH
Current assignee: Ashland Suedchemie Kernfest GmbH
Priority date: 2001-07-26
Filing date: 2002-07-11
Publication date: 2004-05-06
Also published as: PL368607A1; WO2003016400A1; NO20040315L; DE10136365A1

Abstract

The invention relates to a binding agent system comprising a resol resin, at least one oxyanion and at least one compound containing nitrogen, selected from the group containing urea, urea/formaldehyde resins, melamine and melamine/formaldehyde resins.

Description

Resol-based CO ₂ -curable binder system

The present invention relates to resole-based binder systems which have an improved ultimate strength when the cores are heated after curing.

The CO ₂ -curable alkaline phenolic resins described in European patent application EP-A-0 323 096, which are used for the production of molds and cores in the foundry industry, have gained a not insignificant market share in recent years.

A disadvantage of these binders are their z. B. low strength compared to the cold box process, so that their use remains essentially limited to simple, solid cores. However, this has the advantage of very good casting results, so that it would be desirable to use binders with higher strengths To have available, with which it is possible to produce cores and shapes of more complex geometry. A binder with improved strengths is described in German patent application DE-A-199 38 043.

A frequently used method for increasing the strength is to additionally apply heat to the shaped bodies with CO ₂ after hardening. Heat is z. B. also necessary if the moldings have been coated with a so-called size and the carrier liquids contained therein, ie generally water or low-boiling alcohols, such as. B. ethanol or isopropanol, wants to evaporate quickly.

If moldings which have been produced using a binder known from EP-A-0 323 096 or DE-A-199 38 043 are subsequently subjected to heat treatment, it is found that this measure does not lead to the desired increase in strength, but in some cases even to a loss of strength. The present invention seeks to remedy this.

There is a growing interest in expanding the scope of the Resol CO 2 process. It was therefore an object of the present invention to provide a binder system for the resol-CO ₂ process, with which cores with increased strength can be produced.

This object was achieved by a CO ₂ -curable binder system comprising a resol resin, at least one oxyanion and at least one nitrogen-containing compound selected from the group consisting of urea, melamine, urea / formaldehyde resins and melamine / formaldehyde resins, preferably urea and urea / formaldehyde resins ,

Resoles containing the nitrogen compounds mentioned are known per se. Examples of such binders are described, for example, in US 3,306,864 and US 3,404,198. However, the binders specified there cannot be cured with CO ₂ . Either strong acids or salts of strong acids are required as reaction accelerators for curing. There are also heated molds necessary because the sand / binder mixtures must be cured at temperatures of approx. 150 ° C to approx. 250 ° C to achieve short curing times.

The invention further provides a method for producing a CO ₂ -curable binder system, comprising the steps of: providing a resole resin and mixing the resole resin with at least one oxyanion and at least one of the aforementioned nitrogen-containing compounds. The CO ₂ -curable binder system can also be produced by at least partially polymerizing the nitrogen-containing compound into the resole resin. Here, phenol and aldehyde are first condensed in the presence of the nitrogen-containing compound. The resol resin obtained is then mixed with at least one oxyanion. Another option is to add the nitrogen-containing compound to the sand separately only when the core is being produced, and not to dissolve it in the binder system beforehand.

The invention also relates to a molding composition comprising aggregates and an effectively binding amount of the binder system according to the invention.

Furthermore, the use of the binder system according to the invention for the production of a mold part is described, the production process comprising the steps:

(1) mixing aggregates with an effectively binding amount of the binder system according to the invention;

(2) placing the casting mixture obtained in step (1) into a mold; (3) curing the casting mixture in the mold to obtain a self-supporting shape; and (4) then removing the molded casting mixture from step (3) from the mold and further hardening to obtain a hard, solid, hardened mold part.

Essential to the invention is the addition of a nitrogen-containing compound to an oxyanion-containing, with C0 ₂ curable resole resin. This measure increases the strength of the foundry cores if they are subjected to a heat treatment after hardening. The nitrogen-containing compound can additionally lead to a reduction in viscosity in the resole resins which are curable with CO ₂ . High viscosities of the binder systems can have a negative effect on the flowability of the sand mixtures produced therewith, so that the molds cannot be filled completely or only at high pressures during core production. By adding the nitrogen-containing compound, the viscosity of the binder can be adjusted so that the sand mixture has a good flowability. Here, urea is particularly suitable as a nitrogenous compound.

Resole resins are made by condensing a phenolic component and an aldehyde component. Their manufacture has been known for a long time and is e.g. B. in A. Garziella, L.A. Pilato, A. Knop, Phenolic Resins; Springer Verlag (2000).

The resol resins described in EP-A-0 323 096 and in DE-A-199 38 043 are preferably used. The preferred aldehyde resole resins consist mainly of molecules in which the neighboring phenol groups are linked via methylene bridges between the ortho and para positions, since these molecules have a larger number of complexation sites for oxyanions. Molecules in which the phenol groups are linked via ortho-ortho-methylene bridges have very few complexation sites for oxyanions and it is therefore preferred that the content of such molecules is low or that no such molecules are contained in the resol resins. To achieve this goal, all available positions in the phenolic groups that are ortho to the phenolic hydroxy group should be protected as methylolate.

In addition to the particularly preferred phenol, substituted phenols such as, for. B. cresols or nonylphenol, or phenolic compounds, such as. B. bisphenol-A, optionally in combination with phenol. All aldehydes which are conventionally used for the production of resol resins can be used in the context of the invention. Examples of these are formaldehyde, butyraldehyde or glyoxal. Formaldehyde is particularly preferred.

The resole resins are prepared by condensing the phenol component and the aldehyde in the presence of a basic catalyst such as ammonium hydroxide or an alkali metal hydroxide. Alkali metal hydroxide catalysts such as sodium hydroxide and potassium hydroxide are preferably used. In order to obtain suitable resoles for curing by CO ₂ , ie those with a sufficient number of methylol groups ortho to the phenolic hydroxyl group, the polycondensation is generally carried out at relatively low temperatures (approx. 65 to 85 ° C) and with a Catalyst amount of about 2 to 3 wt.% Alkali metal hydroxide based on phenol. It may be expedient to vary the temperature within the specified range. It may also be advantageous to add further alkali metal hydroxide in the course of the reaction.

The molar ratio of aldehyde (given as formaldehyde) to phenol in the resole resin can vary in the range from 1: 1 to 3: 1, but is preferably in the range from 1.6: 1 to 2.5: 1.

In the context of this invention, oxygen-containing anions are referred to as oxyanions. Suitable oxyanions are the oxyanions described in EP-A-323 096 and DE-A-199 38 043, such as aluminates, borates and stannates. Aluminates, borates and mixtures thereof are preferably used. Borates and mixtures of borates with aluminates are particularly preferred.

The boron-containing and aluminum-containing oxyanions can be used directly in the form of their salts. The salts preferably contain alkali or alkaline earth metals as the cation, sodium and potassium salts being preferred because of their ready availability. However, it is also possible to produce the oxyanions in situ. So aluminates form when dissolving aluminum compounds, such as. As aluminum hydroxide or aluminum alcoholates, in alkali. Aluminum alcoholates have the formula AI (OR) ₃ , where R is a saturated or unsaturated, branched or unbranched hydrocarbon radical with 1 to 10 Can be carbon atoms. A solution of a boron compound, such as. B. boric acid or boric acid ester, in lye is suitable as a solution of the boron-containing oxyanion. The base is preferably the solution of a base in water, which is also used for mixing with the resol resin.

In the case of mixtures of aluminates and borates, the Al: B atomic ratio of the boron- and aluminum-containing oxyanions in the binder system according to the invention is preferably in the range from 0.05: 1 to 1: 1. Cores with particularly good strengths are obtained in this range with the binder system according to the invention exhibit. The particularly preferred range is between 0.1: 1 and 0.8: 1. The ratio of the sum of the boron and aluminum atoms in the boron-containing oxyanions and aluminum-containing oxyanions to the number of phenol groups in the resole resin is preferably between 0.1: 1, 0 and 1, 0: 1, 0, particularly preferably between 0.3: 1, 0 and 0.6: 1, 0.

Urea, urea / formaldehyde resins, melamine or melamine / formaldehyde resins are used as nitrogen-containing compounds, preferably urea or urea / formaldehyde resins. Examples of suitable urea / formaldehyde resins are the products from BASF AG known under the trade name Urecoll 118 (solids content 66.5%, nitrogen content 21-22%) and Urecoll 135 (solids content 65%, nitrogen content 18-20%). Particularly good results are achieved with urea.

The binder system according to the invention can also contain other conventional additives such as water and base. As the base alkali metal hydroxides, such as. As sodium hydroxide and potassium hydroxide used. The molar ratio of hydroxide ions to the phenol group in the binder system is preferably 0.5: 1 to 3.0: 1. Water is preferably present in an amount of 25 to 50% by weight, based on the weight of the binder system. The water serves to dissolve the base and possibly the oxyanions. In addition, it should give the binder an application-specific viscosity of 100 to 700 mPa-s, so that even mixing is guaranteed when mixed with the aggregate. The viscosity is determined using a Brookfield rotary viscometer. Further conventional additives such as alcohols, glycols and silanes can be contained in the binder system according to the invention in an amount of up to 25% by weight.

The nitrogenous compound can be used in a number of ways in the manufacture of foundry cores. It can be condensed in during the production of the resole resin, it can be added to the binder system or it can be added to the aggregates separately from the binder system directly during the production of the moldings. Of course, these options can be combined.

Basically, the binder system is produced by mixing the resole resin with base, water and the oxyanions. It is possible to first mix the resole resin with an aqueous solution of a base and then the oxyanions, e.g. B. as a solid or also in the form of an aqueous solution. It is also possible to first mix the oxyanions with base and water and mix this mixture with the resol resin. Subsequently, further base and, if necessary, further water are mixed in.

If the nitrogen-containing compound is to be at least partially condensed into the resole resin, the starting materials of the resole resin such as phenol, aldehyde, possibly further monomers and the nitrogen-containing compound (for example urea) are mixed together and polymerized at an alkaline pH. In general, the amount of urea is 0.1 to 15% based on the total amount of the binder. The resole resin obtained in this way is then optionally used in combination with other customary additives such as water and base as a binder system.

In another embodiment, the nitrogen-containing compound is added to the resole resin after the polymerization. The resole, the nitrogen-containing compound and other additives are mixed in order to obtain the binder system according to the invention. The amount of nitrogen-containing compound should be in the range from 0.1 to 15%, preferably from 0.5 to 12.5%, based on the total amount of the binder. The binder system according to the invention can be used in combination with units for the production of molding compositions which are used for the production of moldings. The mold parts are z. B. used in the casting of metal. The aggregates used and the process steps used are conventional and z. B. from EP-A-0 183 782 known. The binder system is mixed with sand or a similar aggregate to produce a molding compound. Alternatively, the aggregate can first be mixed with the nitrogen-containing compound and then the binder can be added. The molding composition contains an effectively binding amount of up to 10% by weight of the binder system according to the invention (or the sum of binder and separately added nitrogen-containing compound), based on the weight of the aggregates. Methods to achieve a uniform mixture of the binder system and the aggregate are known to the person skilled in the art. The mixture may additionally contain other conventional ingredients such as iron oxide, ground flax or wood fibers, pitch and mineral additives. In order to produce casting mold parts from sand, the aggregate should have a sufficiently large particle size. As a result, the molded part has sufficient porosity and volatile compounds can escape during the casting process. The average particle size of the aggregate is generally between 200 and 400 μm.

For standard casting mold parts, sand is preferably used as the aggregate material, with at least 70% by weight and preferably more than 80% by weight of the sand being silicon dioxide. Zircon, olivine and chromite sand are also suitable as aggregate materials.

The aggregate material is the main component of mold parts. In sand mold parts for standard applications, the proportion of the binder system is generally up to 10% by weight, often between 0.5 and 7% by weight, based on the weight of the aggregate. 0.6 to 5% by weight of binder, based on the weight of the aggregate, is particularly preferably used. The mold part is hardened so that it retains its outer shape after removal of the mold. Conventional liquid or gaseous hardening systems can be used to harden the binder system according to the invention.

So z. B. gaseous CO _{2 are passed} through the casting. However, cold hardening with a liquid catalyst is possible. Examples are the acetic and carbonic acid esters known from the water glass ester and resol ester processes.

After removing the mold parts from the mold, their strength increases and reaches their final value after about 5 to 10 hours of storage at room temperature. Increased final strengths are obtained if mold parts which have been produced with the binder according to the invention are subjected to a heat treatment after removal from the mold. A residence time of approx. 15 to 60 minutes at approx. 120 to 200 ° C in a conventional oven is generally sufficient.

Microwave ovens are equally suitable for heat treatment, with the residence times being shorter than in a conventional oven (e.g. about 5 to 20 minutes with an irradiated energy of about 200 to 1000 watts). The optimal conditions depend on the core size and core geometry.

In order to obtain a smooth casting surface, mold parts are often coated with a so-called size. These are aqueous or alcoholic slurries of refractory minerals. The carrier liquids, i.e. Water or volatile alcohols such as Ethanol or isopropanol are then volatilized in conventional ovens or microwave ovens, so that the refractory minerals are deposited as a fine layer on the mold parts. Cast moldings that were produced with the binder according to the invention show the same advantages in terms of strength as in heat treatment without size coating.

By pouring liquid metal in or around this mold part, cooling and solidifying the metal, and then separating the cast one An object can be cast from metal from the mold part.

The invention is further illustrated by the following examples.

EXAMPLES

Unless otherwise stated, all quantities are given in parts by weight. The viscosity was measured with a Brookfield viscometer and is given in mPa-s. The flexural strength was determined by the "Georg Fischer" method and is given in N / cm ² .

Example 1 Subsequent addition of urea to commercially available resol-CO ₂ binders

1.1 Manufacture of the binders

With good stirring, the amounts of urea listed in Table 1 are added to the commercially available resol-CO ₂ binders at room temperature. The mixture is stirred until a homogeneous solution is obtained.

Table 1

a) Ashland-Südchemie-Kernfest GmbH (containing borate) b) Ashland-Südchemie-Kernfest GmbH (containing borate and aluminate) It can be seen from Table 1 that the addition of urea to a commercially available alkaline phenolic resin curable with CO ₂ lowers its viscosity.

1.2 Production and testing of the molding material / binder mixture

2.5 parts by weight of the binders listed in Table 1 are added to 100 parts by weight of quartz sand H 32 (Quarzwerke GmbH, Frechen) and mixed intensively in a laboratory mixer. These mixtures are used to produce test specimens in accordance with DIN 52 401, which are cured by gassing with CO ₂ (30 seconds, 2 liters of CO ₂ per minute).

The strengths of the test specimens are determined using the "Georg Fischer" method. The flexural strength of the test specimens is checked 30 seconds after their production (immediate strength) and after 24 hours. To determine the resistance to high air humidity, the cores are placed in a humidity chamber (98% rel. Humidity) immediately after they are manufactured and stored there for 24 hours. The strength test is then carried out.

To determine the influence of the heat treatment, proceed as follows:

Conventional oven: The cores are stored in a forced air oven at 150 ° C for 30 minutes 10 minutes after they are made. After cooling to room temperature, the bending strengths are checked.

Microwave oven: The cores are exposed to microwave radiation for 3 minutes 10 minutes after their production. The radiated energy was gradually increased from 200 watts to 700 watts (1 minute 200 watts, 1 minute 500 watts, 2 minutes 700 watts). After cooling to room temperature, the bending strengths are checked.

The result of the strength test is given in Table 2. Table 2

Table 2 shows that the addition of urea to a commercially available, CO ₂ -curable alkaline phenolic resin in the cores produced with these binders causes an increase in strength if, after CO ₂ curing, the cores are additionally heated in a conventional oven or in a microwave oven be charged.

Example 2 Adding urea as a separate component to the molding material / binder mixture

2.1 Manufacture and testing of the chemical / chemical binder mixtures

2.5 parts by weight of NOVANOL 180 are added to 100 parts by weight of H 32 quartz sand (Quarzwerke GmbH, Frechen) and mixed intensively in a laboratory mixer. Then 0.15 parts by weight of urea in solid form or 0.375 parts by weight of an aqueous 40% urea solution are added to this molding material / binder mixture and these are also mixed thoroughly. Then, as described under 1.2, it is cured with CO ₂ and the strength tests are carried out.

The result of the strength tests is given in Table 3. Table 3

a) Ashland-Südchemie-Kernfest GmbH (containing borate and aluminate)

It can be seen that the addition of urea as a separate component increases the strength when the cores are heated in a conventional oven or a microwave oven.

Example 3 Addition of the urea at the start of the condensation of the resole resin

3.1 Manufacture of the binders

3.1.1 Comparative example

440 g of phenol, 220 g of water, 80 g of glycol, 260 g of paraformaldehyde and 10 g of 30% sodium hydroxide solution are mixed and heated to 65 ° C. After the exotherm has subsided, a further 20 g of 30% sodium hydroxide solution are added and the product temperature is increased to 80 ° C. This temperature is kept constant until the Product viscosity is approximately 100 mPa-s. A total of 400 g of 50% potassium hydroxide solution are then added in portions and the batch is stirred at 80 ° C. until the viscosity has risen to approximately 300 mPa · s. Then you cool the resol. The CO ₂ -curable binder Novanol 180 is produced from this resole by adding further potassium hydroxide solution, oxyanions (borate-Z-aluminate), glycols and silane.

3.1.2 Resole containing urea (according to the invention)

The approach described under 3.1.1 is repeated with the difference that at the beginning 6% urea, based on the total amount of the binder, is added.

The remaining components, their relationship to one another and the reaction conditions remain unchanged.

3.2 Production and testing of the binder mixtures

The production and testing of the molding material / binder mixtures is carried out as described in 1.2.

The result of the strength test is given in Table 4.

Table 4

a) NOVANOL 180, Ashland-Südchemie-Kernfest GmbH (containing borate and aluminate) b) contains 6% urea

It has been found that by adding the urea at the start of the condensation of the alkaline phenolic resin, CO ₂ -curable binders are obtained, from which cores can be produced which, when heated in a conventional oven or a microwave oven, have higher strengths than cores with a Binder were made that does not contain urea.

Example 4 Subsequent Addition of Urea Resins to Commercially Available Resole CO ₂ Binders! N

4.1 Manufacture of the binders

The binders are prepared as described under 1.1, instead of urea, the amount of urea / formaldehyde resins given in Table 5 is mixed into the commercially available resol-CO ₂ binder.

Table 5

a) Ashland-Südchemie-Kernfest GmbH (containing borate and aluminate) b) Urea / formaldehyde resin from BASF AG

4.2 Production and testing of the form material / binder mixtures

The production and testing of the molding material / binder mixtures is carried out as described under 1.2. The result of the strength test is shown in Table 6. Table 6

From Table 6 it can be seen that the addition of urea resins to a commercially available, with C0 ₂ hardenable alkaline resole resin in the cores produced with these binders causes an increase in strength when the cores are subsequently exposed to heat in a conventional oven or in a microwave oven.

Claims

1. A CO ₂ curable binder system comprising: (a) a resole resin, and (b) at least one oxyanion, characterized in that the binder system further comprises at least one nitrogen-containing compound selected from the group consisting of urea, urea-Z-formaldehyde resins, melamine and

Contains melamine / formaldehyde resins.

2. A binder system according to claim 1, wherein the nitrogen-containing compound is urea and urea Zformaldehyde resins.

3. A binder system according to claim 1 or 2, wherein the at least one oxyanion is aluminate, borate or a mixture thereof.

4. A method for producing a CO ₂ -curable binder system comprising the steps:

(1) providing a resole resin; (2) Mixing the resole resin with at least one oxyanion and at least one nitrogen-containing compound selected from the group consisting of urea, urea / formaldehyde resins, melamine and melamine / formaldehyde resins.

5. A method for producing a CO ₂ curable binder system comprising the steps:

(1) Providing a resole resin by condensing phenol and aldehyde in the presence of a nitrogen-containing compound selected from the group consisting of urea, urea / formaldehyde resins, melamine and MelamiπZformaldehyde resins.

(2) Mixing the resole resin with at least one oxyanion.

6. Molding composition comprising aggregates, an oxyanion, a nitrogen-containing compound selected from the group consisting of urea, urea-Z-formaldehyde resins, melamine and melamine-Z-formaldehyde resins and an effectively binding amount of a resol resin resilient with CO ₂ .

7. Molding composition comprising aggregates and an effectively binding amount of a binder system according to one of claims 1 to 5.

8. Use of a binder system according to one of claims 1 to 5 for the production of a casting mold part, the production method comprising the steps:

(1) mixing aggregates with an effectively binding amount of the binder system according to one of claims 1 to 3 or of the binder system obtainable according to one of the methods according to claim 4 or 5; (2) placing the casting mixture obtained in step (1) into a mold;

(3) curing the casting mixture in the mold to obtain a self-supporting shape; and

(4) then removing the molded casting mixture of step (3) from the mold and further hardening, whereby a hard, solid, hardened casting mold part is obtained.

9. The method of claim 8, wherein the casting mixture is cured by treating the casting mixture with gaseous carbon dioxide.

10. The method according to claim 8, wherein the casting mixture is hardened by admixing an acetic acid ester or carbonic acid ester to the casting mixture.

11. Use according to one of claims 8 to 10, in which the further hardening is carried out by heat treatment, if necessary after coating with size.