GB2245578A - Formaldehyde resin curing agents. - Google Patents

Abstract

A curing agent for curing formaldehyde-containing resins comprises (i) an ammonium salt and (ii) a Group II or Group III metal, or zinc or iron, salt and is used for curing resins having a ratio of formaldehyde to comonomer of no more than about 1.1:1. The combination of an ammonium and an aluminium salt is preferred and, when sulphate ions are present, can be used as a suitably concentrated, stable aqueous batch by including urea in the solution to improve the solubility of ammonium aluminium sulphate. The curing agent may be used to produce resin-bonded products such as moulded chipboard.

Description

Formaldehyde Resin Curing Agents The invention relates to salts that promote the curing of formaldehyde-containing resins, especially those having low molar ratios of formaldehyde to Co- monomer.

In recent years there has been rising concern over toxic formaldehyde emission from products containing formaldehyde resins, such as, for example, particleboards bonded with urea-formaldehyde (UF) resins. As a result, formaldehyde emission standards have become increasingly strict. In Europe there now exist three European Emission Classes, El, E2 and E3, as shown in Table 1 below: Table 1 Emission Emission Values in Total Extractable Class ppm HCHO Formaldehyde * (mg/100g dry board) El 0.1 < 10 E2 0.1 to 1.0 > 10 to 30 E3 1.0 to 2.3 > 30 to 60 * determined according to European Standard EN 120.

(European Committee for Standardisation, Brussels, January 1984.) (See also the Dangerous Substances Regulations (26th February 1986) and West German Regulations On The Emission Of Formaldehyde From Wood-based Panel Products May 1987.) West Germany is an example of one country that has already introduced legislation requiring that particleboards comply with the El Emission Standard.

That standard, however, presents resin manufacturers with particular difficulties. These difficulties are exacerbated when the product produced contains a high proportion of resin, as may be the case, for example, with moulded chipboard.

In the case of UF resins, for example, whereas resins with the lowest traditional formaldehyde:urea (F:U) molar ratios, of about 1.3:1, fulfil the E2 standard, it has been necessary to develop new resins with F:U molar ratios of as little as 1.05:1 in order to meet the El Standard. Such resins, however, do not cure easily because of the decreased availability of fo-mal- dehyde for reaction to form the cross-linked chain.

Traditional curing agents for formaldehyde resins are either acids or substances that liberate acids upon mixing with the resin, both being used in aqueous solution. Generally no other solvent is used. Typical acid curing agents include inorganic acids such as hydrochloric, nitric, phosphoric and sulphuric acids, and organic acids such as formic acid, oxalic acid and sulphonic acids, for example para-toluene sulphonic acid.

Typical acid-liberating curing agents include the amine and ammonium salts of such acids, such as, for example, triethylamine sulphate and ammonium nitrate, phosphate, chloride, sulphate and sulphamate.

The acid curing agents provide a very rapid rate of cure with the result that aqueous resin compositions incorporating such curing agents suffer from the problem of premature thickening and gelation, and hence have only a short usable pot life. In the case of the ammonium or other salts, acid is liberated by reaction with free formaldehyde already present in the resin and with formaldehyde generated subsequently during curing, the acid being liberated by the following mechanism:

Since the curing reaction is dependent on acidliberation, the acid-liberating curing agents have a slower rate of cure. Thus, ammonium salts, for example, are widely used as curing agents, to provide resin compositions with a higher ratio of pot-life to curing time than acid curing agents.

In the case of low-formaldehyde resins, however, not only is there the problem that there is less formaldehyde for cross-linking, but also the traditional ammonium salts are less able to catalyse the cross-linking reactions, because their catalytic activity depends on the presence of formaldehyde.

It is an object of this invention to provide a curing agent that is suitable for curing those formaldehyde-containing resins that contain low levels of formaldehyde.

We have found that the use of (i) an ammonium salt together with (ii) a metal salt that is a Group II or Group III salt or a zinc or iron salt is especially useful for curing those resins having a ratio of formaldehyde to comonomer of no more than about 1.1:1.

We have found that the combination of an ammonium salt and an aluminium salt, (e.g. ammonium chloride or sulphate and aluminium chloride or sulphate) is especially preferred, the combination of aluminium sulphate and either ammonium chloride or ammonium sulphate being especially effective, and that in the presence of urea these salts can be combined into a single aqueous solution that remains stable over an extended period of time.

Accordingly, the present invention provides an aqueous batch solution for curing a formaldehydecontaining resin containing ammonium, aluminium and sulphate ions, and urea or a urea derivative.

We have found that in the absence of urea the combination of an ammonium salt and an aluminium salt, at least one of which is a sulphate, can be used in only a limited concentration in aqueous solution, because the presence of sulphate ions leads to the formation of the complex salt ammonium aluminium sulphate, NH4Al(S04)2.12H20, which is relatively insoluble.

Anhydrous aluminium sulphate, A12(SO4)3, has a solubility in water at OOC of 31.3g and at 1000C of 98.lg, each expressed in terms of g per 100ml of solution. Ammonium sulphate has a solubility at the same temperatures of 70.6g and 103.8g per l00ml, respectively.

However, the solubility of the complex salt ammonium aluminium sulphate, NH4Al(S04)2.12H20, is only 15.0g per lOOml solution at 200C, or effectively 8.0g per lOOml solution when expressed in terms of the anhydrous salt.

The simple mixing of concentrated solutions of the two components results in the immediate precipitation of the much less soluble mixed salt. Such precipitation causes considerable problems. For example, it would not be possible to deliver the curing agent solution from jet sprays as is common during large-scale board manufacture, as the sprays would become blocked.

If, alternatively, the amount of complex salt used were restricted to the maximum soluble concentration (effectively 8g/lOOml in terms of the anhydrous salt, for a solution at 200C), it would be necessary for a larger volume of water to be present in order to provide a sufficient molar quantity of the individual aluminium and ammonium salts for curing. In the case of particleboard manufacture, the increased volume of water would give rise to longer pressing times and a reduction in mechanical properties of the resin-bonded product. Although the wood chips could be dried prior to incorporation in the resin binder, the product would still be likely to have inferior mechanical properties.

We have found that by the use of urea the solubility of the complex salt can be substantially improved, even at very low temperatures. For instance a mixture of lOg ammonium sulphate, log aluminium sulphate tetradecahydrate and 80g water would not remain in solution even when kept at 400C: substantial quantities of crystalline material were present. However, when half the quantity of the water above was replaced by an equal quantity of urea, the solution remained completely stable for long periods with no trace of zecipitation even at temperatures as low as 2 e If the solution were to be kept at 250C only 25g of the water would require replacement by urea.

Thus, the present invention enables the abovementioned problems to be substantially overcome by means of the addition of urea to the solution so as to increase the solubility of the complex salt and allow the curing agent solution to be used in the desired higher concentration.

French Patent Specification No. 2268 4 is concerned with the pot life of adhesives to which a hardener has been applied and with the difficulties of adjusting the hardener/adhesive ratio to compensate. It discloses a method of controlling pot life by adding to the resin two hardener components in aqueous solution, the first component being an ammonium or Group Ia or Group IIa metal salt and the second component being a copper, aluminium or iron salt. Although one or both of the hardener components may contain urea to enhance the strength of the bond formed between the components to which the adhesives is applied, those components are kept separately before adding to the resin, as opposed to being kept in a pre-prepared combined solution, so that there is no disclosure of preparing an aqueous curing batch containing the components of the present invention.

Furthermore, FR 2268044 is concerned only with the hardening of traditional urea formaldehyde resins so there is no appreciation of the particular problems associated with low formaldehyde resins and, since that specification does not combine ammonium, aluminium and sulphate ions into an aqueous curing batch, nor is there any appreciation of the problems of preparing an aqueous batch containing those particular ions.

The present invention also provides an ammonium salt and an aluminium salt, at least one of which is a sulphate, for curing a formaldehyde-containing resin, wherein the salts are used as an aqueous batch solution containing urea or a urea derivative that improves the solubility of the complex salt, ammonium aluminium sulphate.

If desired, the salts may be supplied to the resin in the form of one or more batches.

The present invention also provides a closable vessel, especially a closed vessel, containing an aqueous batch of the invention.

The invention also provides a process for curing a formaldehyde-containing resin, wherein there is used an aqueous batch of the invention.

The invention is of especial application where the formaldehyde-containing resin is a urea-formaldehyde resin having a ratio of formaldehyde to comonomer of no more than 1.1:1, more especially substantially 1.05:1 or below, each ratio calculated on the total quantity of urea present in the resin and the curing agent system.

The invention further provides a process for curing a formaldehyde-containing resin having a ratio of formaldehyde to comonomer of no more than 1.1:1, wherein there is used as curing agent a combination of (i) an ammonium salt and (ii) a metal salt that is a Group II or Group III salt or a zinc or iron salt.

If desired two or more ammonium salts and/or two or more of the specified metal salts may be used.

Preferably, the ratio by weight of ammonium salt: metal salt, more especially aluminium salt, is from 0.2:1 to 1.8:1, more especially substantially 1:1. With a resin having a low level of formaldehyde available for reaction with the ammonium salt, the proportion of ammonium salt should generally not be too high, and preferably should not exceed 1.2:1.

The ammonium salt may be, for example, ammonium chloride or ammonium sulphate.

The metal salt is preferably a salt of a strong acid, such as, for example, a chloride, nitrate or sulphate. Preferred metal salts are, not only aluminium, but also zinc or magnesium salts, although the aluminium salt, such as, for example, aluminium chloride or aluminium sulphate1 is especially preferred. An iron salt, such as, for example, ferric chloride may also be used, but is less preferred. These metal salts, which are water-soluble, form only weak bases upon reaction during curing, which bases do not adversely affect the rate of curing. The invention also contemplates, in place of or together with the or one of the metal salts specified, the use of a transition metal having similar aqueous solubility which forms a weakly basic hydroxide.

In contrast to the ammonium salts, which are able to promote curing at room temperature, the above-defined metal salts only undergo reaction so as to liberate free acid at elevated temperatures. Hydrolysis of magnesium chloride, for example, according to the reaction:

does not occur below about 100 C.

Suitable formaldehyde-containing resins include urea resins, e.g. urea formaldehyde resins, melamine resins and phenolic resins, including their co-condensed products, for example urea/melamine and urea/melamine/phenol resins, and mixtures of two or more such resins.

The formaldehyde-containing resin may be used, for example, to bond water-penetrable cellulosic particles, fibres or sheets, more especially to bond particleboard, for example chipboard, wafer board, medium density fibre board and oriented strandboard. Use for bonding particleboards that comply with the El Standard should especially be mentioned.

The invention further provides a resin-bonded product, for example extruded, flat-pressed or moulded particleboard, when produced by a process of the invention.

The amount of resin present in the product can vary and may be, for example, 7 to 8 %, or up to 10 %, by weight of the wood component. Amounts substantially larger than those may, however, also be used; for example, moulded chipboard may be prepared using 4 to 5 times that amount of resin.

Ultimately, the curing agent salts will form part of an aqueous binder comprising the resin, water, the particulate or fibrous material and one or more other additives such as, for example, alkali metal salts, for example sodium chloride, lubricants, waxes, adhesion promoters and scavengers for formaldehyde; the latter are compounds that are able to react with formaldehyde so as to minimize residual free formaldehyde, and include compounds such as, for example, ammonia and urea; these formaldehyde-scavengers are preferably added when the binder is added to the particulate or fibrous material.

The manner of application of the ammonium and metal salts, and of the resin and any other additives, will depend on the type of product being produced. The salts may be supplied either separately or together, in either case in powder or, more usually, in liquid form.

The present invention further provides the use of a composition which comprises (i) one or more ammonium salts and (ii) one or more metal salts selected from Group II and Group III salts and zinc and iron salts, for curing a formaldehyde-containing resin having a ratio of formaldehyde to comonomer of no more than 1.1:1.

As mentioned above, when component (ii) is an aluminium salt and the hardener-component contains sulphate ions, urea is desirably present, to provide a suitably concentrated stable aqueous solution.

The present invention also provides the use, for curing a formaldehyde-containing resin having a ratio of formaldehyde to comonomer of no more than 1.1:1, of a combined preparation which comprises as separate components for simultaneous or sequential addition to the resin (i) one or more ammonium salts and (ii) one or more metal salts selected from Group II and Group III salts and zinc and iron salts.

The salts may each be added to the resin binder immediately prior to curing, or may be pre-mixed and added together, for example as a batch solution.

Alternatively, they may, for example, be mixed with the particulate or fibrous material, which is then dried prior to the application of the resin and other additive(s). Methods for the production of resinbonded products are well known and are described in the literature; see, for example, the CIBA Information Manual No. BP.6a, June 1970.

If desired, urea or other formaldehyde-scavenger may be present as a separate component or present with the separate ammonium, and/or metal salts or, if desired or in the case of urea - if required, with a mixture of the salts.

Thus, urea may, for example, be added to the resin'binder mixture prior to the addition of the salts, or later, prior to or during the addition of water, or may be mixed with either or both of the salts or with a mixture of the salts prior to their being mixed with the resin.

As mentioned above, where an aqueous solution batch containing ammonium, aluminium and sulphate ions is made up, urea should be present to provide a suitably concentrated stable solution.

The present invention further provides a process for improving the water-solubility of complex salts, for example alums, more especially ammonium aluminium sulphate, by the incorporation of urea in the solution.

The present invention also provides solutions of such salts in the form of aqueous liquids of higher concentration than would be normally expected.

For many applications (and the use of these materials to promote the curing of certain resinous materials is only one such application) salts need to be dissolved in solvents in order to provide easier handling or dispensing, and to ensure more intimate mixing with other components used in formulations. Aqueous solutions have many advantages in that the solvent, water, is readily available, cheap, and non-flammable.

Many salts have good or even excellent solubility in water and if necessary can be used at high concentration.

However, in other cases it is impossible to achieve the desired concentration at the required temperature of use or storage, because of the poor inherent solubility of the salt in water. In other cases where it is desired to use a combination of two or more salts the solubility of the combination is often inferior to that of the individual components. We have found that by the use of urea the solubility of certain salts can be substantially improved.

Aluminium salts, for example, often have very good solubility in water especially when simple salts such as aluminium chloride or sulphate are used. However, as mentioned above, when aluminium salts are to be used in combination with other salts with which they can form complex salts, e.g. ammonium salts, difficulties often occur because the complex salt has only relatively poor water solubility.

The mechanism of action of the urea is not entirely clear. Its action may be at least partly attributable to breaking of hydrogen bonds. Accordingly, the use of urea derivatives or other hydrogen-bond-breaking compounds is also contemplated. Possible examples include formamide, dimethylformamide, acetamide, acrylamide, polyacrylamide and 4- or 5-hydroxypropyl urea.

Urea is a preferred hydrogen-bond-breaking compound, however, especially in the field of curing agents for formaldehyde-containing resins, because it may also act as a scavenger for formaldehyde. In that case the amount of urea present when the salts are present in solution must, of course, be sufficient to improve the water-solubility sufficiently so as to provide a curing agent solution with long-term stability, (i.e. preferably stable for more than six weeks). A suitable urea:water weight ratio may be, for example, 1.5:1 to 1:4, and a ratio of more than 1:1.5, advantageously about 1:1, should especially be mentioned.

In one embodiment of the present invention a curing agent solution comprises ammonium chloride or sulphate and aluminium sulphate in a weight ratio of approximately 1:1, and urea and water in a weight ratio of approximately 1:1. The ratio of the weight of combined salts to the weight of urea and water may be, for example, 1:2.5 to 1:3, e.g. 1:2.7. The solution may be added to a resin in a weight ratio of curing agent solution:resin of, for example, 1:25 to 3:25.

The invention is illustrated by the following Examples, in which all percentages are by weight.

Example 1 In this Example, the catalytic activity of a curing agent solution of the invention, comprising an ammonium and an aluminium salt (Solution C), was compared with that of solutions of the same amounts of the individual salts (Solutions A and B).

The curing agent solutions A, B, and C were prepared according to the compositions given in Table 2 below.

Urea was also present so as to prevent the precipitation of the complex salt ammonium aluminium sulphate. The solutions were each added to a urea-formaldehyde resin of F:U molar ratio 1.05:1 in amounts of 5 % and 10 % (relative to the weight of the resin). Six drops of each mixture were transferred to a 100mm by l0mm test-tube, which was then heated in a bath of boiling water. The gelation time was recorded for each of the six resin mixtures, and is given in Table 2 below.

Table 2 Component Composition of Curing Agent Solution % by weight A B C Ammonium chloride 13.3 - 13.3 Aluminium sulphate - 13.3 13.3 Urea 36.7 36.7 36.7 Water 50.0 50.0 36.7 Gelation time (secs) 5 % addition 47 39 29 10 % addition 52 31 27 Curing agent Solution A, containing only an ammonium salt, gave the longest gelation time and did not improve the curing rate when present in a greater amount.

Solution B provided a faster curing rate, which rate decreased with an increase in volume of solution added.

Solution C, which contained the same amounts of ammonium chloride and aluminium sulphate as Solutions A and B, respectively, provided the fastest curing rate.

ExamPle 2 This Example illustrates how the solubility in an aqueous solution of ammonium aluminium sulphate increases when the hydrogen-bond-breaking compound urea is added to the solution.

Referring to Table 3 below, five aqueous solutions, A to E, each comprising an ammonium and an aluminium salt, were prepared in the quantities indicated. In each of solutions B,C and E, a significant amount of water was replaced by urea. Each solution was heated to a sufficient temperature to cause complete dissolution of the components. The stability of each solution was then monitored at three different temperatures.

Table 3 Component Composition of Solution % by weight A B C D E Aluminium Sulphate (A12(S04)314H20) 10 10 10 10 10 Ammonium Sulphate 10 10 10 -- - Ammonium Chloride -- -- -- 5 5 Water 80 60 40 85 65 Urea -- 20 40 -- 20 Curing Agent Stability at different temperatures OC Solution 2 20 40 A * * immediate crystallisation B * 6 weeks * C > 6 weeks > 6 weeks * D * immediate crystallisation E * > 6 weeks * * not tested Referring first to solutions A, B and C, each of which contains 10% (by weight) aluminium sulphate tetradecahydrate and 10 % ammonium sulphate, it will be noted that ammonium aluminium sulphate precipitates from Solution A, in which the solvent is pure water, even at the highest temperature of 400C.In Solutions B and C, however, the solubility of the complex salt improves with increasing t by weight of urea present in the aqueous solution.

A similar result is found for Solutions D and E, in which the ammonium sulphate is replaced with ammonium chloride.

Example 3 In this Example, two particleboards, A and B, were prepared from wood chips using a low formaldehyde content UF resin as a binder. Board A was cured using a curing agent comprising an aqueous solution of ammonium chloride and aluminium sulphate, in which the hydrogen-bondbreaking compound, urea, was also present. Board B was cured using a traditional ammonium salt curing agent.

Board A 25.1 kg of a UF resin having a F:U molar ratio of 1.05:1, and solids content of 65.0%, was mixed with 1.25 kg of an aqueous curing agent solution consisting of 13.33% ammonium chloride, 13.33% aluminium sulphate tetradecahydrate, 36.67% urea, the remainder being water, and with 3.15 kg wax emulsion, and 70.5 kg wood chips.

(The aqueous curing agent solution had been kept for 2 weeks at 100C to 200C, prior to use, and had remained a clear solution in which there was no precipitate.) A moulded particleboard was formed which was pressed for 2 minutes at 1600C.

Board B A similar board was made using 24.5 kg of the same UF resin, which was mixed with 2.48 kg of a curing agent solution containing 20% ammonium chloride, 3.12 kg wax emulsion and 70.0 kg wood chips. The board was pressed for 2 minutes at 1600C.

The boards were conditioned for 1 week at 680F (200C) and the total extractable formaldehyde determined using the iodometric method.

The results were as follows: Total extractable formaldehyde (mg/100 g dry board) Board A 4.8 Board B 7.6 Although both boards met the El classification, Board A contained the least residual free formaldehyde and was also found to have the better mechanical properties.

Claims (33)

CLAIMS:

1. An aqueous batch for curing a formaldehydecontaining resin, containing ammonium, aluminium and sulphate ions, and urea.

2. An aqueous batch as claimed in claim 1, wherein the ammonium ions are derived from ammonium chloride or ammonium sulphate.

3. An aqueous batch as claimed in claim 1 or claim 2, wherein the aluminium ions are derived from aluminium chloride or aluminium sulphate.

4. An aqueous batch as claimed in any one of claims 1 to 3, wherein the ratio by weight of the ammonium salt to aluminium salt is from 0.2:1 to 1.8:1.

5. An aqueous batch as claimed in any one of claims 1 to 4, wherein the ratio by weight of urea to water is in the range of from 1: to 1.5:1.

6. An aqueous batch as claimed in claim 5, wherein the ratio by weight of urea to water is more than 1:1.5.

7. An aqueous batch as claimed in claim 5, wherein the ratio by weight of urea to water is substantially 1:1.

8. An aqueous batch as claimed in claim 1, which is substantially as described herein.

9. A process for preparing - aqueous batch for curing a formaldehyde-containing resin as claimed in any one of claims 1 to 8, the process comprising combining with water, to form a stable solution, predetermined quantities of an ammonium salt, an aluminium salt, and urea, each of which is initially in solid form, and wherein at least one of the specified salts is a sulphate and/or a further salt which is a sulphate is present.

10. A process as claimed in claim 9, wherein the ammonium salt, aluminium salt and urea are added to the water as a mixed powder.

11. An aqueous batch as claimed in claim 1, whenever prepared by a process as claimed in claim 9 or claim 10.

12. A closed vessel containing a batch as claimed in any one of claims 1 to 8 and 11.

13. A process for curing a formaldehyde-containing resin, wherein there is used as curing agent an aqueous batch as claimed in any one of claims 1 to 8 and 11.

14. A process as claimed in claim 13, wherein the resin has a ratio of formaldehyde to comonomer that does not exceed 1.1:1.

15. A process for the production of a formaldehydecontaining resin-bonded product, wherein curing of the resin is carried out as specified in claim 13.

16. A process as claimed in claim 15, wherein the resin is as specified in claim 14.

17. A process as claimed in claim 15 or claim 16, wherein the resin-bonded product is particleboard.

18. A process as claimed in claim 15, carried out substantially as described herein.

19. A resin-bonded product whenever produced by a process as claimed in any one of claims 15 to 18.

20. The use of an aqueous batch as claimed in any one of claims 1 to 8 and 11, for curing a resin having a ratio of formaldehyde to comonomer that does not exceed 1.1:1.

21. An ammonium salt and an aluminium salt, at least one of which is a sulphate, for curing a formaldehyde-containing resin, wherein the salts are used as an aqueous batch solution containing urea or a urea derivative that improves the solubility of the complex salt, ammonium aluminium sulphate.

22. The use of an ammonium salt and an aluminium salt, at least one of which is a sulphate, together with urea, for the manufacture of an aqueous solution that is stable over an extended period of time, for curing a formaldehyde-containing resin.

23. The use of urea for the manufacture of an aqueous solution that is stable over an extended period of time, containing ammonium, aluminium and sulphate ions and urea, for curing a formaldehyde-containing resin.

24. A process for improving the water-solubility of ammonium aluminium sulphate which comprises the addition of urea.

25. An aqueous batch for curing a formaldehydecontaining resin, which contains ammonium aluminium sulphate and a hydrogen-bond-breaking compound.

26. A process for curing a formaldehyde-containing resin wherein there is used an aqueous batch as claimed in claim 25.

27. A process for curing a formaldehyde-containing resin having a molar ratio of formaldehyde to comonomer of no more than 1.1:1, wherein there is used as curing agent (i) an ammonium salt and (ii) a metal salt that is a Group II or Group III salt or a zinc or iron salt.

28. A process as claimed in claim 27, wherein the ratio by weight of ammonium salt:metal salt is from 0.2:1 to 1.8:1.

29. A process as claimed in claim 27 or claim 28, wherein the ammonium salt is ammonium chloride or ammonium sulphate.

30. A process as claimed in any one of claims 27 to 29, wherein the metal salt is an aluminium, zinc or magnesium salt.

31. A process as claimed in claim 30, wherein the metal salt is an aluminium salt.

32. A process as claimed in claim 31, wherein the aluminium salt is aluminium chloride or aluminium sulphate.

33. A process as claimed in any one of claims 27 to 32, wherein curing is carried out in the presence of urea.