POLYISOCYANATE COMPOSITIONS

Abstract: According to the invention, a polyisocyanate composition comprises a titanium, zirconium or hafnium composition, preferably a titanium or zirconium composition, said composition being a complex of at least one metal selected from the group consisting of titanium, zirconium and hafnium and an acetoacetate ester in which the molar ratio of Ti, Zr or Hf to acetoacetate ester is in the range 1 : 2.5 to 1 : 10 and said acetoacetate ester is an ester of an alcohol containing 1 to 6 carbon atoms. The invention also comprises a process for binding lignocellulosic material using such compositions.

Description: POLYISOCYANATE COMPOSITIONS This invention relates to polyisocyanate compositions and, in particular, to polyisocyanate compositions containing certain organometallic compositions based on Group IVB metals and which are useful in binding lignocellulosic material. The use of organic polyisocyanates as binders for lignocellulosic material in the manufacture of sheets or moulded bodies such as waferboard, chipboard, fibreboard and plywood is well known. In a typical process the organic polyisocyanate, optionally in the form of a solution, dispersion or aqueous emulsion, is applied to the lignocellulosic material which is then subjected to heat and pressure. One suitable polyisocyanate composition is disclosed in PCT Application WO 97/17388. This composition comprises a Group IVB metal compound, preferably a titanium chelate, optionally in combination with a compatibilising compound and/or conventional release agents. Although these compositions perform well as binders for lignocellulosic material and provide good release performance, it is desirable to develop a more economical composition which provides improved stability on storage before use, together with good curing properties and excellent bonding strength when applied to the lignocellulosic material. It has now been surprisingly found that certain polyisocyanate compositions containing certain compounds of Group IVB metals and acetoacetate esters are very stable on prolonged storage and economical when used for binding lignocellulosic material. According to the invention, a polyisocyanate composition comprises a titanium, zirconium or hafnium composition, preferably a titanium or zirconium composition, said composition being a complex of at least one metal selected from the group consisting of titanium, zirconium and hafnium and an acetoacetate ester in which the molar ratio of Ti, Zr or Hf to acetoacetate ester is in the range 1 : 2.5 to 1 :10 and said acetoacetate ester is an ester of an alcohol containing 1 to 6 carbon atoms. GONFIRMATiOM COPY The titanium, zirconium or hafnium composition used in the polyisocyanate composition of the invention is described herein as a "complex". It is believed that some of the acetoacetate ester will be chemically bound to the metal (Ti, Zr or Hf) but some can be described as "free" ester. The exact proportions which are bound and free will depend partly upon the exact molar ratios present in the complex and which metal, or metals, are used, but it has been shown that the "free" ester does influence the properties, particularly the stability on storage, of the polyisocyanate composition as a binder for lignocellulosic materials. The use of the word "complex" does not imply that said complex is necessarily separately prepared before addition to a polyisocyanate to form the compositions of the invention. The complex can be formed by preparing the inventive composition using several alternative methods as described hereinafter. The molar ratio of metal to acetoacetate ester in the complex is in the range 1 : 2.5 to 1 : 10. When the metal is titanium, the molar ratio is preferably in the range 1 : 2.5 to 1 : 8 and more preferably in the range 1 : 3 to 1 : 6. In agreement with conventional theories about the co-ordination chemistry of titanium, it is believed that two molecules of acetoacetate ester will be chemically bound to a titanium atom and the remainder will be "free". When the metal is zirconium or hafnium, the molar ratio is preferably 1 : 4.5 to 1 : 10 and more preferably 1 : 4.5 to 1 : 8, zirconium or hafnium to acetoacetate ester. For zirconium or hafnium, again in accordance with conventional theory, it is believed that, for complexes which contain 4 or more moles of acetoacetate ester, 4 molecules of acetoacetate ester are chemically bound to each atom of zirconium or hafnium and the remainder are "free". Preferably, the complex is a complex of at least one of titanium and zirconium. The preferred acetoacetate ester for preparing the complex is ethyl acetoacetate. The complex can be prepared from more than one acetoacetate ester but preferably only one acetoacetate ester is present in the complex. Typically, the complexes of titanium, zirconium or hafnium are prepared from titanium, zirconium or hafnium alkoxides having the general formula M(OR) 4 in which M is Ti, Zr or Hf and R is a substituted or unsubstituted, cyclic or linear, alkyl, alkenyl, aryl or alkyl-aryl group or mixtures thereof. Preferably, R contains up to 8 carbon atoms and, more preferably, up to 6 carbon atoms. Generally, all four OR groups will be identical but alkoxides derived from a mixture of alcohols can be used and mixtures of alkoxides can be employed when more than one metal is present in the complex. Suitable alkoxides include tetramethoxytitanium, tetra-ethoxytitanium, tetra-isopropoxytitanium, tetra-n-propoxytitanium, tetrabutoxytitanium, tetrakis(2-ethylhexoxy)titanium, tetrakis(2-ethoxyethoxy)titanium, tetracyclohexyloxytitanium, tetraphenoxy- titanium, tetrapropoxyzirconium, tetrabutoxyzirconium, tetra-n-propoxyhafnium and tetra-n-butoxyhafnium. Alternatively, the complex can be prepared from condensed alkoxides of titanium, zirconium or hafnium. These compounds can be represented by the general formula RO[M(OR) 2 O] x R, wherein M and R have the same meaning as discussed above and x is an integer. Generally, these condensed alkoxides consist of a mixture containing compounds of the above formula with x having a range of values. Preferably, x has an average value in the range 2 to 16 and, more preferably, in the range 2 to 8. A condensed alkoxide is usually prepared by the controlled addition of water to an alkoxide, followed by removal of alcohol which is displaced. Suitable condensed alkoxides include the compounds known as polybutyl titanate, polybutyl zirconate and polyisopropyl titanate. Complexes of condensed alkoxides can also be prepared by forming a complex of an acetoacetate ester with an alkoxide, adding water to the complex and removing any by-product alcohol. Other titanium, zirconium or hafnium compounds, such as titanium, zirconium or hafnium tetrachloride or alkoxides which have been substituted with, for example, glycol or phosphorus substituents can be used as raw materials for the formation of the complex used in the invention. The complex can be readily prepared by mixing, for example, an alkoxide or condensed alkoxide with an appropriate amount of acetoacetate ester. Alcohol from the alkoxide will be displaced by the acetoacetate ester and, preferably, the displaced alcohol is removed by, for example, distillation. In a preferred method, 2 moles of acetoacetate ester per atom of Ti or 4 moles of acetoacetate ester per atom of Zr or Hf are added to an alkoxide or condensed alkoxide and the displaced alcohol is removed by distillation. Any additional acetoacetate ester required is then added to the stripped product. This method is advantageous because it provides a consistent product of known stoichiometry. It is possible to add all the acetoacetate ester in one charge and subsequently remove all the displaced alcohol but some of the "free" acetoacetate ester is usually accidentally removed during this process, leading to inconsistent products and contamination of the displaced alcohol. Alternatively, a product containing, for example, 2 moles of acetoacetate ester per Ti atom or 4 moles of acetoacetate ester per Zr or Hf atom can be prepared according to the method outlined above and this can be mixed with a polyisocyanate. Any additional acetoacetate ester required to produce the polyisocyanate composition of the invention can be added to the polyisocyanate before or after the titanium, zirconium or hafnium compound has been added. Other methods of preparing the composition of the invention will be apparent to a person skilled in this art. The amount of titanium, zirconium or hafnium complex present in the polyisocyanate composition of the invention is usually in the range 0.01 to 20 % by weight, based on the polyisocyanate and, preferably, the amount is in the range 0.1 to 10 %. More preferably, the amount of complex present is in the range 0.2 to 7 % by weight with respect to polyisocyanate. When the complex is a complex of titanium, the most preferred amount of complex is in the range 0.2 to 5.0 % by weight and, when the complex is a complex of zirconium the most preferred amount of complex is in the range 0.2 to 3.5 % by weight based on the polyisocyanate. Polyisocyanates for use in the composition of the present invention may be any organic polyisocyanate compound or mixture of organic polyisocyanate compounds, provided said compounds have at least 2 isocyanate groups. Organic polyisocyanates include diisocyanates, particularly aromatic diisocyanates, and isocyanates of higher functionality. Examples of organic polyisocyanates which may be used in the composition of the present invention include aliphatic isocyanates such as hexamethylene diisocyanate; and aromatic isocyanates such as m- and p-phenylene diisocyanate, tolylene-2,4- and tolylene-2,6-diisocyanate, diphenyl- methane-4,4'-diisocyanate, chlorophenylene-2,4-diisocyanate, naphthylene- 1,5-diisocyanate, diphenylene-4,4'-diisocyanate, 4,4'-diisocyanate- 3,3'-dimethyl-diphenyl, 3-methyldiphenylmethane-4,4'-diisocyanate and diphenyl ether diisocyanate; and cycloaliphatic diisocyanates such as cyclohexane-2,4- and -2,3-diisocyanate, 1 -methylcyclohexyl-2,4- and -2,6-diisocyanate and mixtures thereof and bis-(isocyanatocyclohexyl)methane and triisocyanates such as 2,4,6-triisocyanatotoluene and 2,4,4-triisocyanatodiphenylether. Modified polyisocyanates containing isocyanurate, carbodiimide or uretonimine groups may be employed as well. Further blocked polyisocyanates, like the reaction product of a phenol or an oxime and a polyisocyanate, may be used, having a deblocking temperature below the temperature applied when using the polyisocyanate composition. The organic polyisocyanate may also be an isocyanate-ended prepolymer made by reacting an excess of a diisocyanate or higher functionality polyisocyanate with a polyol. Water-emulsifiable organic polyisocyanates like those described in UK patent no. 1 444 933, in European patent publication no. 516 361 and in PCT patent publication no. 91/03082 can also be used. Mixtures of isocyanates may be used, for example a mixture of tolylene diisocyanate isomers such as the commercially available mixtures of 2,4- and 2,6-isomers and also the mixture of di- and higher polyisocyanates. Polyisocyanate mixtures may optionally contain monofunctional isocyanates such as p-ethyl phenylisocyanate. Such mixtures are well-known in the art and include the crude phosgenation products containing methylene bridged polyphenyl polyisocyanates, including diisocyanate, triisocyanate and higher polyisocyanates together with any phosgenation by-products. Preferred isocyanates to be used in the present invention are those wherein the isocyanate is an aromatic diisocyanate or polyisocyanate of higher functionality such as a pure diphenylmethane diisocyanate or a mixture of methylene bridged polyphenyl polyisocyanates containing diisocyanates, triisocyanates and higher functionality polyisocyanates. Methylene bridged polyphenyl polyisocyanates are well known in the art. They are prepared by phosgenation of corresponding mixtures of polyamines. For convenience, polymeric mixtures of methylene bridged polyphenyl polyisocyanates containing diisocyanate, triisocyanate and higher functionality polyisocyanates are referred to hereinafter as polymeric MDI. Suitable polyisocyanates include SUPRASEC™ DNR, SUPRASEC™ 2185, RUBINATE™ M and RUBINATE™ 1840, all avilable from Imperial Chemical Industries. Preferably the polyisocyanate is liquid at room temperature. Conventional release agents can be added to or used in combination with the polyisocyanate composition of the present invention containing a titanium, zirconium or hafnium complex of an acetoacetate ester. The conventional release agent is present in an amount varying between 0.2 and 10 %, preferably between 0.5 and 6 % and most preferably between 1 and 3 % by weight based on the polyisocyanate whereas the titanium, zirconium or hafnium complex of an acetoacetate ester is preferably present in an amount varying between 0.2 and 4 %, most preferably between 0.2 and 2 % by weight based on the polyisocyanate. Examples of conventional release agents include polysiloxanes, saturated or unsaturated fatty acids (such as oleic acid) or fatty acid amides or fatty acid esters and polyolefϊn waxes. Preferred conventional release agents to be used according to the present invention are polyolefϊn waxes or mixtures of polyolefin waxes, especially functionalised polyolefin waxes, which are dispersible in an aqueous medium to form an aqueous emulsion. More preferably, the polyolefin waxes are selected from oxidised polyethylene waxes and oxidised polypropylene waxes. A preferred method for using the release agent is to apply the emulsion to the surface of the polyisocyanate treated lignocellulosic material or to the press metal surface prior to hot pressing the combination. When used, the aqueous emulsion of the polyolefin wax should normally contain a sufficient amount of the polyolefin wax to provide a coverage of about 0.01 to about 1, and preferably about 0.02 to about 0.5 mg of the polyolefin wax per cm 2 of lignocellulosic material or press metal surface. Generally, lower levels of polyolefin wax are preferred as they are more cost effective. When taking the emulsifϊers into account, the aqueous emulsions will usually contain about 0.2 to about 10 %, preferably about 0.3 to about 5 % by weight of total solids. The emulsions are usually prepared at 30 to 40 % total solids, transported to the point of use and then diluted with water to the desired concentration. It has been found that the polyolefin wax emulsion, when used in combination with polyisocyanate compositions of the present invention, may be usefully applied to the lignocellulosic material or press metal surface in an amount equivalent to 8 to 14 mg per cm 2 . A particularly preferred polyethylene wax emulsion which can be used in a process in combination with a polyisocyanate composition of the present invention is Rubilon™ 603 or Rubilon™ 605 , both available from Imperial Chemical Industries. A particularly preferred polypropylene wax emulsion which can be used in the present process is ME 42040 available from Michelman Inc. of Cincinnati, Ohio. In order to further improve the storage stability of the polyisocyanate composition of the present invention a diluent may be added to the composition. Suitable diluents include plasticizers of the type mentioned in "Taschenbuch der Kunststoff-Additive", Ed. by R. Gachter and H. Muller, Carl Hanser Verlag Munchen, third edition, 1989. Preferred diluents are phthalates, aliphatic carboxylates, fatty acid esters, linseed oil and soybean oil. A particularly preferred diluent is Priolube 1403 available from Unichema being methyloleate. These diluents are added in amounts of from 1 to 40 parts by weight per 100 parts by weight of polyisocyanate and preferably in amounts of from 1 to 15 parts by weight per 100 parts by weight of polyisocyanate. The composition further may comprise conventional additives like flame retardants, lignocellulosic preserving agents, fungicides, waxes, sizing agents, fillers, surfactants, thixotropic agents and other binders like formaldehyde condensate adhesive resins and lignin (optionally in combination with a lignin solvent such as described in PCT Patent Application No. EP96/00924). A particularly preferred additive to be used in the polyisocyanate composition of the present invention is a coupling agent such as an organofunctional silane (for example, Dynasylan AMEO, available from Huels). Adding such a coupling agent to the polyisocyanate composition leads to improved board properties. The organofunctional silane coupling agents are used in amounts ranging from 0.01 to 3 %, preferably from 0.1 to 2 % by weight based on the polyisocyanate. The polyisocyanate composition of the present invention can be made by simply mixing the ingredients at room temperature. The present invention is also concerned with a process for preparing lignocellulosic bodies by bringing lignocellulosic parts into contact with a polyisocyanate composition and by pressing this combination. Therefore the present invention also provides a process for binding lignocellulosic material comprising the steps of a) bringing said lignocellulosic material in contact with the present polyisocyanate composition comprising a titanium, zirconium or hafnium composition which is a complex of at least one metal selected from the group consisting of titanium, zirconium and hafnium and an acetoacetate ester in which the molar ratio ot Ti, Zr or Hf to acetoacetate ester is in the range 1 : 2.5 to 1 :10 and said acetoacetate ester is an ester of an alcohol containing 1 to 6 carbon atoms and b) subsequently allowing said material to bind. The lignocellulosic bodies are prepared by bringing the lignocellulosic parts into contact with the polyisocyanate composition by means such as mixing, spraying and/or spreading the composition with/onto the lignocellulosic parts and by pressing the combination of the polyisocyanate composition and the lignocellulosic parts, preferably by hot-pressing, normally at 150° C to 250°C and 2 to 6 MPa specific pressure. Such binding processes are commonly known in the art. In waferboard manufacture the lignocellulosic material and the polyisocyanate composition may be conveniently mixed by spraying the present polyisocyanate composition on the lignocellulosic material while it is being agitated. As described hereinbefore, in a preferred process according to the invention, a release agent, which is preferably an aqueous emulsion of a polyolefin wax, is applied to the surface of the polyisocyanate treated lignocellulosic material or to the press metal surface prior to hot pressing the combination. The lignocellulosic material after treatment with the polyisocyanate composition is placed on caul plates made of aluminium or steel which serve to carry the furnish into the press where it is compressed to the desired extent usually at a temperature between 150° C and 250° C. While the process is particularly suitable for the manufacture of waferboard known extensively as oriented strand board and will be largely used for such manufacture, the process may not be regarded as limited in this respect and can also be used in the manufacture of medium density fiberboard, particle board (also known as chipboard) and plywood. Thus the lignocellulosic material used can include wood strands, woodchips, wood fibres, shavings, veneers, wood wool, cork, bark, sawdust and like waste products of the wood working industry as well as other materials having a lignocellulosic basis such as paper, bagasse, straw, flax, sisal, hemp, rushes, reeds, rice hulls, husks, grass, nutshells and the like. Additionally, there may be mixed with the lignocellulosic materials other particulate or fibrous materials such as ground foam waste (for example, ground polyurethane foam waste), mineral fillers, glass fibre, mica, rubber, textile waste such as plastic fibres and fabrics. When the polyisocyanate composition is applied to the lignocellulosic material, the weight ratio of polyisocyanate/lignocellulosic material will vary depending on the bulk density of the lignocellulosic material employed. Therefore, the polyisocyanate compositions may be applied in such amounts to give a weight ratio of polyisocyanate/lignocellulosic material in the range of 0.1 : 99.9 to 20 : 80 and preferably in the range of 0.5 : 99.5 to 10 : 90. If desired, other conventional binding agents, such as formaldehyde condensate adhesive resins, may be used in conjunction with the polyisocyanate composition. More detailed descriptions of methods of manufacturing waferboard and similar products based on lignocellulosic material are available in the prior art. The techniques and equipment conventionally used can be adapted for use with the polyisocyanate compositions of the present invention. The polyisocyanate compositions of the present invention are extremely effective in minimising unwanted adhesion to caul plates, press plates and other surfaces with which the treated lignocellulosic material may come into contact. Their storage stability and release performance is improved compared to polyisocyanate compositions of the prior art, as well as the obtained board properties. The sheets and moulded bodies produced from the polyisocyanate compositions of the present invention have excellent mechanical properties and they may be used in any of the situations where such articles are customarily used. The invention is illustrated but not limited by the following examples. EXAMPLE 1 Preparation of Product A A reactor was charged with tetraisopropyl titanate (1400 kg, Tilcom ® TIPT from ICI Vertec). Ethylacetoacetate (1282 kg) was then added with stirring. The resulting product was a pale red liquid. The displaced alcohol (580 kg, isopropanol) was then removed by evaporation to leave a red liquid, PRODUCT A (2090 kg). Product A was then diluted by addition of various amounts of methylacetoacetate, ethylacetoacetate and cetylacetoacetate in the following molar ratios. TABLE 1 TABLE 2 TABLE 3 The products were evaluated by preparing a number of compositions comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and various amounts of the samples designated Test 1 to 12 (see Table 4 below). Each composition contained the same concentration of Product A. The compositions were then stored at 45° C and the viscosity tested by means of a Brookfield viscometer at various intervals. TABLE 4 As a comparison a number of compositions comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and various amounts of the samples designated Comparison 1 to 6 (see Table 5 below) were made up. All these compositions contained the same amount of Product A, this amount being the same as the amount of Product A in each of the compositions designated Test 1 to Test 12. These compositions were then stored at 45° C and the viscosity tested using a Brookfield viscometer at the same intervals. TABLE 5 The following results were obtained for the systems based on Product A with various added amounts of methylacetoacetate and ethylacetoacetate [all results are reported in Pa s]. <5 TABLE 6 Product A + Methylacetoacetate n.m. = not measured TABLE 7 Product A + Ethylacetoacetate n.m. = not measured The following results were obtained for the systems based on Product A with various added amounts of cetylacetoacetate [all results reported in Pa s]. TABLE 8 Product A + Cetylacetoacetate n. m. = not measured Generally, the most relevant period for storage stability at room temperature is the period 14 to 46 days after production of the polyisocyanate composition. From Tables 6 to 8 above, it can be seen that the optimum (generally, lowest) viscosity after 46 days at 45° C (an accelerated test) is achieved in Test 2 (2.2 moles methylacetoacetate), Test 8 (2.2 moles ethylacetoacetate) and Comparison 4 (6.6 moles cetylacetoacetate). The results demonstrate that the titanium complexes used in the composition of the invention provide a more economical means of stabilising the polyisocyanate composition. EXAMPLE 2 Preparation of Product B A flask was charged with tetra-n-propyl zirconate (43.7g, Tilcom ® NPZ - which contains 75% Zr(OnPr) 4 - from ICI Vertec) and placed in a cold water bath. Methylacetoacetate (46.5g) was added over a period of one hour whilst the mixture was stirred. The resulting product was a pale yellow liquid. The displaced alcohol (35.3g, n-propanol) was then removed on a rotary evaporator to leave a yellow oil (54.8g). The oil was then mixed with additional methylacetoacetate (11.6g) to yield PRODUCT B. To evaluate the product a composition comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and 2.09 parts by weight Product B was prepared in duplicate. The compositions were then stored at 45° C and the viscosity tested at various intervals using a Brookfield viscometer. Results are reported in Table 9 below in Pa s. TABLE 9 Preparation of Product C A flask was charged with tetra-n-propyl zirconate (43.7g, Tilcom ® NPZ - which contains 75% Zr(OnPr) 4 - from ICI Vertec) and placed in a cold water bath. Methylacetoacetate (46.5g) was added over a period of one hour whilst the mixture was stirred. The resulting product was a pale yellow liquid. The displaced alcohol (34.3g, n-propanol) was then removed on a rotary evaporator to leave a yellow oil (55.8g). The oil was then mixed with additional methylacetoacetate (23.2g) to yield PRODUCT C. To evaluate the product a composition comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and 2.48 parts by weight Product C was prepared in duplicate. The compositions were then stored at 45° C and the viscosity tested at various intervals using a Brookfield viscometer. Results are reported in Table 10 below in Pa s. TABLE 10 Preparation of Product D A flask was charged with tetra-n-propyl zirconate (87.3g, Tilcom ® NPZ - which contains 75% Zr(OnPr) 4 - from ICI Vertec) and placed in a cold water bath. Ethylacetoacetate (104g) was added over a period of one hour whilst the mixture was stirred. The resulting product was a pale yellow liquid. The displaced alcohol (67. lg, n-propanol) was then removed on a rotary evaporator to leave a yellow oil (124.3g). The oil was then mixed with additional ethyl acetoacetate (26g) to yield PRODUCT D. To evaluate the product a composition comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and 2.21 parts by weight Product D was prepared in duplicate. The compositions were then stored at 45° C and the viscosity of the compositions tested at various intervals using a Brookfield viscometer. Results are reported in Table 11 below in Pa s. TABLE 11 Preparation of Product E A flask was charged with tetra-n-propyl zirconate (87.3g, Tilcom ® NPZ - which contains 75% Zr(OnPr) 4 - from ICI Vertec) and placed in a cold water bath. Ethylacetoacetate (104g) was added over a period of one hour whilst the mixture was stirred. The resulting product was a pale yellow liquid. The displaced alcohol (70. Og, n-propanol) was then removed on a rotary evaporator to leave a yellow oil (121.4g). The oil was then mixed with additional ethylacetoacetate (52g) to yield PRODUCT E. To evaluate the product a composition comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and 2.56 parts by weight Product E was prepared in duplicate. The compositions were then stored at 45° C and the viscosity of the compositions tested at various intervals using a Brookfield viscometer. Results are reported in Table 12 below in Pa s. TABLE 12 The zirconium complexes (Products B, C, D E) show improved stability over a longer period of time than the titanium complexes of Comparison 1 to 6 (Table 8). EXAMPLE 3 Preparation of Product F A flask was charged with tetraisopropyl titanate (71g, Tilcom ® TIPT from ICI Vertec) and placed in a cold water bath. Ethylacetoacetate (65g) was added over a period of one hour whilst the mixture was stirred. Following addition of ethylacetoacetate, distilled water (l.lg, 0.25 moles per mole of Ti) was added to the mixture with thorough stirring. The resulting product was a pale red liquid. The displaced alcohol (43.4g, isopropanol) was then removed on a rotary evaporator to leave a red liquid (94.5g). This liquid was then mixed with additional ethyl acetoacetate (65g) to yield PRODUCT F. To evaluate the product a composition comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and 0.88 parts by weight Product F was prepared. The composition was then stored at 45° C and the viscosity of the composition tested at various intervals using a Brookfield viscometer. Preparation of Product G A flask was charged with tetraisopropyl titanate (71g, Tilcom ® TIPT from ICI Vertec) and placed in a cold water bath. Ethylacetoacetate (65g) was added over a period of one hour whilst the mixture was stirred. Following addition of ethylacetoacetate, distilled water (2.3g, 0.5 moles per mole of Ti) was added to the mixture with thorough stirring. The resulting product was a pale red liquid. The displaced alcohol (48.4g, isopropanol) was then removed on a rotary evaporator to leave a red liquid (93.3g). This liquid was then mixed with additional ethyl acetoacetate (65g) to yield PRODUCT G. To evaluate the product a composition comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and 0.88 parts by weight Product G was prepared. The composition was then stored at 45° C and the viscosity of the composition tested at various intervals using a Brookfield viscometer. Results are reported for Product F and Product G in Table 13 below in Pa s. TABLE 13 EXAMPLE 4 A flask was charged with tetraisopropyl titanate (71g, Tilcom ® TIPT from ICI Vertec) and placed in a cold water bath. tert-Butylacetoacetate (79. lg) was added over a period of one hour whilst the mixture was stirred. The resulting product was a pale yellow liquid. The displaced alcohol (30.0g, isopropanol) was then removed on a rotary evaporator to leave a red liquid (120.0g). This liquid was then mixed with additional ethyl acetoacetate (65g) to yield PRODUCT H. To evaluate the product a composition comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and 1.02 parts by weight Product H was prepared. The composition was then stored at 45° C and the viscosity of the composition tested at various intervals using a Brookfield viscometer. Results are reported in Table 14 below in Pa s. TABLE 14 EXAMPLE 5 Preparation of Product I A flask was charged with tetraisopropyl titanate (71g, Tilcom ® TIPT from ICI Vertec) and placed in a cold water bath. Ethylacetoacetate (65g) was added over a period of one hour whilst the mixture was stirred. Following addition of ethylacetoacetate, butyl acid phosphate (11.4g, 0.25 moles) was added to the mixture with thorough stirring. The resulting product was a pale red liquid. The displaced alcohol (38.2g, isopropanol) was then removed on a rotary evaporator to leave a red liquid (109.2g). This liquid was then mixed with additional ethyl acetoacetate (65g) to yield PRODUCT I. To evaluate the product a composition comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and 0.97 parts by weight Product I was prepared in duplicate. The compositions were then stored at 45° C and the viscosity of the compositions tested at various intervals using a Brookfield viscometer (see Table 15). Preparation of Product J A flask was charged with tetraisopropyl titanate (71g, Tilcom ® TIPT from ICI Vertec) and placed in a cold water bath. Ethylacetoacetate (65g) was added over a period of one hour whilst the mixture was stirred. Following addition of ethylacetoacetate, butyl acid phosphate (22.8g, 0.5 moles) was added to the mixture with thorough stirring. The resulting product was a pale red liquid. The displaced alcohol (40.8g, isopropanol) was then removed on a rotary evaporator to leave a red liquid (118.0g). This liquid was then mixed with additional ethyl acetoacetate (65g) to yield PRODUCT J. To evaluate the product a composition comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and 1.02 parts by weight Product J was prepared. The composition was then stored at 45° C and the viscosity of the composition tested at various intervals using a Brookfield viscometer. Results are reported for Product I and Product J in Table 15 below in Pa s. TABLE 15 EXAMPLE 6 A sample of Product A, prepared as described in Example 1 was mixed with ethylacetoacetate in the ratio of 4 moles ethylacetoacetate to 1 mole of Product A (Test). A comparative sample was prepared from 1 mole titanium acetylacetonate (Tyzor AA 105, available from DuPont de Nemours) and 3 moles cetylacetoacetate (Comparison). To evaluate these products a number of compositions comprising 100 parts by weight of polyisocyanate (polymeric MDI, SUPRASEC DNR, available from Imperial Chemical Industries) and 1 part by weight of product were made up (see Table 16 below). TABLE 16 These compositions were used to bind softwood strands at 9 % binder loading based on dry wood. Boards of 12 x 450 x 450 mm and density 720 kg/m 3 were made using the above compositions and also containing a sizing wax emulsion (SPG 60 available from Condea Chemie) at 1 % loading (solid wax) based on dry wood. The prepressing moisture content was 10 % and the press temperature 170° C. The following properties were obtained using the binder compositions listed above. TABLE 17 The average standard deviations were 200 kPa for IB, 80 kPa for VI 00 IB and 2 % for thickness swell. EXAMPLE 7 Boards were also made using Product A and ethylacetoacetate in various proportions (Table 18) to determine the release performance of polyisocyanate compositions in combination with an external spray of polyolefin release agent (Rubilon™ 603, available from Imperial Chemical Industries). For the experiment the concentration of wax in the release agent emulsion was adjusted by addition of water. In order to reproduce the failure mode all spray of release agent was stopped from the 7th repeat onwards. It is considered that a release rating (see below) of 3 will cause a catastrophic failure under plant conditions. Results are summarised in Table 19 below. TABLE 18 The release rating is given a value from 1 to 5 having the following significance: 1 complete sticking, board can not be removed without destruction of the board 2 sticking with wood failure higher than 50 % 3 sticking with wood failure less than 25 % but higher than 5 % 4 sticking with wood failure less than 5 %. Little force needed to remove board. 4.5 sticking without wood failure, hanging board. No effort needed to remove board. 5 perfect release, the board releases spontaneously. The results of Table 19 show that an amount of Product A of 0.5 parts by weight based on the isocyanate can allow a dilution of the release agent emulsion by up to 10 times.

Claims: CLAIMS 1. A polyisocyanate composition comprising a titanium, zirconium or hafnium composition, which is a complex of at least one metal selected from the group consisting of titanium, zirconium and hafnium and an acetoacetate ester in which the molar ratio of Ti, Zr or Hf to acetoacetate ester is in the range 1 : 2.5 to 1 :10 and said acetoacetate ester is an ester of an alcohol containing 1 to 6 carbon atoms. 2. A polyisocyanate composition according to claim 1 in which the complex is a complex of titanium having a molar ratio of Ti to acetoacetate ester in the range 1 : 2.5 to 1 : 8. 3. A polyisocyanate composition according to claim 2 in which the molar ratio of Ti to acetoacetate ester is in the range 1 : 3 to 1 : 6. 4. A polyisocyanate composition according to claim 1 in which the complex is a complex of hafnium having a molar ratio of Hf to acetoacetate ester in the range 1 : 4.5 to 1 : 10. 5. A polyisocyanate composition according to claim 4 in which the molar ratio of Zr or Hf to acetoacetate ester is in the range 1 : 4.5 to 1 : 8. 6. A polyisocyanate composition according to any one of the preceding claims in which the acetoacetate ester is ethyl acetoacetate. 7. A polyisocyanate composition according to any one of the preceding claims in which the complex has been prepared from a titanium, zirconium or hafnium alkoxide having the general formula M(OR) 4 in which M is Ti, Zr or Hf and R is a substituted or unsubstituted, cyclic or linear, alkyl, alkenyl, aryl or alkyl-aryl group. 8. A polyisocyanate composition according to claim 7 in which R contains up to 6 carbon atoms. 9. A polyisocyanate composition according to any one of claims 1 to 6 in which the complex has been prepared from a condensed titanium, zirconium or hafnium alkoxide having the general formula RO[M(OR) 2 O] x R in which M is Ti, Zr or Hf, x is an integer and R is a substituted or unsubstituted, cyclic or linear, alkyl, alkenyl, aryl or alkyl-aryl group. 10. A polyisocyanate composition according to claim 9 in which the average value of x is in the range 2 to 16. 11. A polyisocyanate composition according to any one of the preceding claims in which the complex is prepared from an alkoxide or condensed alkoxide and displaced alcohol is removed. 12. A polyisocyanate composition according to any one of the preceding claims in which the complex is present in an amount in the range 0.01 to 20 % by weight based on the polyisocyanate. 13. A polyisocyanate composition according to claim 12 in which the amount of complex is in the range 0.5 to 7 % by weight based on the polyisocyanate. 14. A polyisocyanate composition according to any one of the preceding claims in which the polyisocyanate is diphenylmethane diisocyanate or a mixture of methylene bridged polyphenyl polyisocyanates. 15. A polyisocyanate composition according to any one of the preceding claims additionally comprising a release agent. 16. A polyisocyanate composition according to claim 15 in which the complex is present in an amount in the range 0.2 to 4 % by weight based on the polyisocyanate and the release agent is present in an amount in the range 0.2 to 10% by weight based on the polyisocyanate. 17. A polyisocyanate composition according to claim 15 or 16 in which the release agent is a polysiloxane, a saturated fatty acid, an unsaturated fatty acid, a fatty acid amide, a fatty acid ester or a polyolefin wax. 18. A polyisocyanate composition according to any one of claims 15 to 17 in which the release agent is an oxidised polyethylene wax or an oxidised polypropylene wax. 19. A polyisocyanate composition according to any one of the preceding claims additionally comprising a diluent. 20. A polyisocyanate composition according to claim 19 in which the diluent is a phthalate, an aliphatic carboxylate, a fatty acid ester, linseed oil or soybean oil. 21. A polyisocyanate composition according to claim 20 in which the diluent is present in an amount in the range 1 to 40 parts by weight per 100 parts by weight of polyisocyanate. 22. A process for binding lignocellulosic material comprising the steps of (a) bringing lignocellulosic material into contact with a polyisocyanate composition comprising a titanium, zirconium or hafnium composition which is a complex of at least one metal selected from the group consisting of titanium, zirconium and hafnium and an acetoacetate ester in which the molar ratio ot Ti, Zr or Hf to acetoacetate ester is in the range 1 : 2.5 to 1 : 10 and said acetoacetate ester is an ester of an alcohol containing 1 to 6 carbon atoms and (b) subsequently allowing said material to bind. 23. A process according to claim 22 in which the polyisocyanate composition is brought into contact with the lignocellulosic material and the combination thereby formed is hot-pressed between metal plates at a temperature in the range 150° C to 250° C and a specific pressure in the range 2 to 6 MPa. 24. A process according to claim 22 or 23 in which the polyisocyanate composition is applied in such an amount as to give a weight ratio of polyisocyanate to lignocellulosic material in the range 0.1 : 99.9 to 20 : 80. 25. A process according to any one of claims 22 to 24 in which a release agent is applied to the surface of the polyisocyanate treated lignocellulosic material or to the press metal plate surface before hot pressing the combination. 26. A process according to claim 25 in which the release agent is an aqueous emulsion of a polyolefin wax or a mixture of polyolefin waxes. 27. A process according to claim 26 in which the polyolefin wax is an oxidised polyethylene wax or an oxidised polypropylene wax. 28. A process according to claim 26 or 27 in which the emulsion of polyolefin wax has a total solids content of 0.2 to 10% by weight. 29. A process according to any one of claims 25 to 28 in which the release agent is a polyolefin wax and is applied in an amount sufficient to provide coverage of 0.01 to 1 mg polyolefin wax per cm 2 of lignocellulosic material or press metal surface.

Inventors: SKINNER CHRISTOPHER JOHN, SKINNER, CHRISTOPHER, JOHN
Applicants: HUNTSMAN ICI CHEM LLC, SKINNER CHRISTOPHER JOHN, HUNTSMAN ICI CHEMICALS LLC, SKINNER, CHRISTOPHER, JOHN
Application year: 1999
Main classification: C08G18
IPC codes: B27N3, C07C69, C07F7, C08G18, C08K5, C08L75