PROCESS FOR MANUFACTURE OF A DENDRITIC POLYETHER

Abstract: A process for manufacture of a dendritic polyether comprising a core, derived from a compound having two or more hydroxyl groups, and at least one branching generation being built up from at least one hydroxyoxetane having one oxetane group and at least one hydroxyl group is disclosed. The process comprises ring opening addition to said core and ring opening polymerisation of said hydroxyoxetane. A mixture of the core compound and at least one cationic initiator is prepared and said hydroxyoxetane is fed to said mixture at a rate resulting in and/or maintaining a reaction temperature below onset at thermal degradation and in an amount resulting in at least one branching generation. The initiator is present in an amount of 0.1-0.5 % by weight calculated on said core and said oxetane, preferably in an amount giving a ratio hydroxyl groups to initiator of between 1:0.01 and 1:0.05. Yielded dendritic polyether is sebsequently neutralised by addition of at least one alkaline compound and optionally purified.

Description: PROCESS FOR MANUFACTURE OF A DENDRITIC POLYETHER The present invention refers to a process for manufacture of a dendritic polyether comprising a core and at least one branching generation. The process comprises mixing at least one compound having two or more hydroxyl groups and at least one cationic initiator and subjecting at least one hydroxyoxetane to ring opening addition and polymerisation. Said hydroxyoxetane is charged at a rate resulting in and maintaining a reaction below onset at thermal degradation and in an amount resulting in at least one branching generation. Dendritic polymers belong to a group of polymers, characterised by densely branched structures and a large number of end groups. They are obtained by the polymerisation of for instance AB X monomers, such as AB 2 monomers, giving branched structures, with an exponential growth, in both molecular weight and end group functionality, as a function of the degree of polymerisation. Dendritic polymers are either produced by homo or co-polymerisation of one or several monomers, optionally in the presence of a multifunctional core. Figures I and II below illustrate dendritic polymers with and without core. The use of a multifunctional core is of particular interest, since it allows a higher degree of freedom in the molecular design of dendritic structures. In "Surface Coatings Technology" Volume IN, Chapter N, Bo Pettersson et.al, John Wiley & Sons Ltd, it is taught that two sets of properties can be controlled by the use of a multifunctional core, namely i) the ability to control molecular weight and polydispersity, and ii) the physical properties at a given molecular weight. Examples are given of polydisperse dendritic polyesters, which have been produced with and without the use of a polyalcohol core and it was found that both the polydispersity at a given molecular weight as well as the bulk viscosity could be reduced when a trifunctional polyalcohol core was employed versus homo-polymerisation of the neat monomer 2,2-dimethylolpropionic acid. Dendritic polymers built up from multifunctional cores are often produced, according to a divergent growth pattern. In the divergent synthesis route, monomers such as AB X monomers (also called chain extenders) first react with a multifunctional core in stoichometric ratio with regard to the number of reactive groups of the core molecule and the number of A groups of the AB X monomer. Obtained reaction product will when AB 2 monomers are used have twice the functionality of the starting core molecule. The reaction product according to the first step can then in subsequent steps undergo reactions with further AB X monomers, until the desired molecular weight and/or end group functionality is obtained. The principle for a divergent synthesis route is illustrated in Figure III below. The term generation is often used for dendritic polymers to describe the number of repetitive steps involved in a synthesis and hence indirectly the molecular weight and end group functionality. In the case of polydisperse products, the term pseudo-generation is sometimes used to clarify that there is an uncertainty as to where exactly the AB X monomers are located within the dendritic structure. The term generation will herein be used as designation for generation as well as pseudo-generation and is defined in accordance with equations 1-3 below. F = fx X n Eq. 1 N = f(X n - l) Eq. 2 MHBP = N fMe-M i l + μFCM t - M R zJ + M ϊ Eq. 3 Wherein n Number of generations or pseudo-generations. F End group functionality of dendritic polymer with n generations. N Equivalents of chain extenders per equivalent of dendritic polymer with a core functionality f and n generations or pseudo-generations. M HBP Molecular weight of end-capped dendritic polymer with n generations. M e Molecular weight of chain extender. RI Molecular weight of reaction product formed in reaction between groups A and B (which for polyesters is the molecular weight of H 2 O). μ Fraction of end groups capped with an end-capping group. M t Molecular weight of end-capping group. MR2 Molecular weight of reaction product formed in reaction between terminal groups and end-capping groups. M r Molecular weight of core molecule. Dendritic polyethers made by ring opening polymerisation have attracted some interest recently. Dendritic structures made from glycidol have been studied by Nandenberg, E.J., Pol. Sci, Part A: Polym. Chem., 1989, 27, 3113 and Sunder, A. et.al., Macromolecules, 1999, 32, 4240 and dendritc structures from and 3-ethyl-3-hydroxymethyloxetane (trimethylolpropaneoxetane) by Magnusson, H. et.al., Macromol. Rapid Commun., 1999, 20, 453-457. Ring opening polymerisation of oxetanes is per se lαiown in the art and disclosed and discussed in for instance a number of Patents. US Patent no. 4,988797 discloses polymerisation of cyclic ethers having 4 and 5 membered rings in the presence of an intiator consiting of an acid catalyst and an alcohol. The polymers are grown from the alcohol. The acid catalyst is employed at a level of between 0.05 and 0.5 relative to the hydroxyl functionalty of the alcohol. Exemplified polymers are starbranched polyethers. US Patent no. 6,100,375 teaches an improved method for synthesis of energetic polymers based on cyclic ethers having 4 and 5 member rings. Said polymers are produced in the presence of a solvent by employing a triethoxonium salt and an alcohol, both in co-catalytically amounts, as initiator. Disclosed cyclic ethers are monocyclic compounds having at least one (CFi 3 ) n X group, X being -N 3 , -H, -ONO 2 , -CL, -CN, -BR or -O(Cι-Cι 0 alkyl). Synthesis of ABA triblock polymers and A n B star polymers from cyclic ethers is described in US Patent no. 4,952,644. Dendritic polyethers obtained by ring opening polymerisation of hydroxy oxetanes (compounds having one oxetane group and at least one hydroxyl group) offer a rapid process yielding dendritic structures. Dendritic polyethers are furthermore, and contrary to dendritic polyesters, hydrolytically stable, which is of interest in applications wherein an aqeuous and alkaline environment is employed. It is of particular interest to study dendritic polyethers made by ring opening polymerisation of 3-ethyl-3-hydroxymethyloxetane, since the monomer is non-toxic and hence environmentally friendly. The 3-ethyl-3-hydroxymethyloxetane monomer is furthermore only possible to polymerise under cationic conditions, which allows the hydroxyl functionality to be modified under alkaline conditions prior to polymerisation. Said modified product can then be used as co-monomer with for instance neat 3-ethyl-3-hydroxymethyloxetane or other hydroxyoxetane and specific functionalities can thereby be incorporated in the inherent dendritic polymer backbone. Dendritic polymers made from hydroxyoxetanes offer interesting physical properties such as a glas transition temperatures (Tg) in the range of 30-45°C for polymers made from 3-ethyl-3-hydroxymethyloxetane and low melt viscosities at elevated temperatures. It has however been found that in order to produce dendritic polyethers from hydroxyoxetanes as defined above, it is difficult to control final molecular weights and obtained polymers differ significantly in properties and chemical conversion, depending on the reaction temperature during polymerisation. Surprisingly, it has been found that hydroxyoxetane based polymers can suffer from poor thermal stability in air atmosphere and if the reaction temperature is above the onset at thermal degradation, poor final properties will result with low final molecular weights and large amount of residual monomers. Onset is here and hereinafter defined as the left limit of exothermic degradation peak in air at a heating rate of at least 3°C/minute. A method to overcome above mentioned problems with control of molecular weight of dendritic polyethers from hydroxyoxetanes and the thermal degradation can now quite surprisingly be disclosed. It has been found that it is possible to produce dendritic polyethers from hydroxyoxetanes by employing a divergent synthesis approach, wherein a multifunctional alcohol is used as an initiator core. By using the same theoretical approach as has succesfully been demonstrated for dendritic polyesters made from 2,2-dimethylolpropionic acid and polyalcohol cores, it is possible to control both final molecular weight and polydispersity. It has furthermore been found that by using particular conditions during synthesis it is possible to reach very high chemical conversion and to control the polydispersity, final molecular weight and the like. Said conditions include that a cationic initiator is pre-mixed with an alcoholic core, that at least one hydroxyoxetane monomer is feeded continously to the reaction solution with strict temperature control and the reaction solution is kept at a certain temperature interval below onset at thermal degradation. It has also quite surprisingly been found that the thermal stability of obtained dendritic polyether, having one or more generations built up from at least one hydroxyoxetane and a polyalcohol core, can be significantly improved by neutralising the cationic initiator in stoichiometric amounts with a conventional alkaline species, such as NaOH and the like. Obtained dendritic polyether disclosed and produced according to the method of the present invention is hence superiour in terms of control of molecular weight and thermal stability compared to what previously have been demonstrated with oxetane monomers. The present invention accordingly refers to a process for manufacture of a dendritic polyether comprising a core, derived from a compound having two or more hydroxyl groups, and at least one branching generation, preferably at least two branching generations, being built up from at least one hydroxyoxetane having one oxetane group and at least one hydroxyl group. The process comprises ring opening addition to said core and ring opening polymerisation of said oxetane. A mixture of said compound having said two or more hydroxyl groups and at least one cationic initiator is prepared and optionally heated to 90-130°C and said at least one hydroxyoxetane is fed to said mixture at a rate resulting in and/or maintaining a reaction temperature, during said ring opening addition and said ring opening polymerisation, being below onset at thermal degradation as defined by DSC (Differential Scanning Calorimetry) in air and in an amount resulting in said at least one branching generation. The initiator is present in an amount of 0.1-0.5% by weight calculated on said core and said hydroxyoxetane, preferaby in an amount giving a ratio hydroxyl groups to initiator of between 1 :0.01 and 1 :0.05 preferably between 1:0.01 and 1:<0.05 . Yielded dendritic polyether is furthermore neutralised by addition of an alkaline compound and optionally purified. Said reaction temperature is preferably 110 ± 20°C, such as 100 ± 10°C and said hydroxyoxetane is preferably fed to said mixture during at least 30 minutes. Yielded dendritic polyether has a preferred polydispersity of less than 2, such as less than 1.8, less than 1.6 or even less than 1.4, a preferred thermal degradation point of more than 200°C, such as more than 250°C and a residual monomer content (prior to said optional purification) of less than 1%, such as less than 0.8% or less than 0.6% by weight. The compound (core compound) having said at least two hydroxyl groups is in preferred embodiments of the process of the present invention a di, tri or polyhydric alcohol, a di, tri or polyhydric ester or polyester or a di, tri or polyhydric ether or polyether, such as a 5,5-dihydroxyalkyl-l,3-dioxane, a 5,5-di(hydroxyalkoxy)-l,3-dioxane, a 5,5-di(hydroxy- alkoxyalkyl)-l,3-dioxane, a 2-alkyl-l,3-propanediol, a 2,2-dialkyl-l,3-propanediol, a 2-hydroxy-l,3-propanediol, a 2,2-dihydroxy-l,3-propanediol, a 2-hydroxy-2-alkyl-l,3- -propanediol, a 2-hydroxyalkyl-2-alkyl-l,3-propanediol, a 2,2-di(hydroxyalkyl)-l,3- -propanediol, a 2-hydroxyalkoxy-2-alkyl-l,3-propanediol, a 2,2-di(hydroxyalkoxy)- -1,3-propanediol, a 2-hydroxyalkoxyalkyl-2-alkyl-l,3-propanediol or a 2,2-di(hydroxy- alkoxyalkyl)- 1 ,3 -propanediol. Further preferred embodiments of said compound having said at least two hydroxyl groups include dimers, trimers and polymers of a 5,5-dihydroxyalkyl-l,3-dioxanes, 5,5-di(hydroxy- alkoxy)-l,3-dioxanes, 5,5-di(hydroxyalkoxyalkyl)-l,3-dioxanes, 2-alkyl-l,3-propanediols, 2,2-dialkyl- 1 ,3 -propanediols, 2-hydroxy- 1 ,3-propanediols, 2,2-dihydroxy- 1 ,3 -propanediols, 2-hydroxy-2-alkyl-l,3-propanediols, 2-hydroxyalkyl-2-alkyl-l,3-propanediols, 2,2-di- (hydroxyalkyl)-l,3-propanediols, 2-hydroxyalkoxy-2-alkyl-l,3-propanediols, 2,2-di(hydroxy- alkoxy)-l,3-propanediols, 2-hydroxyalkoxyalkyl-2-alkyl-l,3-propanediols and 2,2-di(hydroxy- alkoxyalkyl)- 1 ,3-propanediols. In above disclosure, alkyl is preferably C -C 24 , such as C 1 -C 12 or Ci-Cg, linear or branched alkanyl or alkenyl and alkoxy is preferably ethoxy, propoxy, butoxy, phenylethoxy nominally comprising 0.2-20 alkoxy units or is a combination of two or more of said alkoxy nominally comprising 0.2-10 units of respective alkoxy and nominally comprising a total of 0.2-20 alkoxy units. Yet further embodiments of said compound having said at least two hydroxyl groups include monoallyl or mono(methallyl) ethers of glycerol, trimethylolethane and trimethylolpropane, monoallyl, diallyl, mono(methallyl) or di(methallyl) ethers of di(trimethylolethane), di(trimethylolpropane) and pentaerythritol as well as l,ω-diols, such as mono, di, tri and polyethylene glycols, mono, di, tri and polypropylene glycols, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,6-cyclohexanedimethanol and alkyl, alkoxy, alkylalkoxy and alkoxyalkyl substituted species and derivatives thereof. Alkyl and alkoxy is here preferably as previously disclosed. Especially preferred embodiments of said compound having said at least two hydroxyl groups are advantegously selected from the group consisting of 5,5-dihydroxymethyl-l,3-dioxane, 2-methyl- 1 ,3 -propanediol, 2-methyl-2-ethyl- 1 ,3-propanediol, 2-ethyl-2-butyl- 1 ,3-propanediol, neopentyl glycol, dimethylpropane, glycerol, trimethylolethane, trimethylolpropane, diglycerol, di(trimethylolethane), di(trimethylolpropane), pentaerythritol, di(pentaerythritol), anhydroenneaheptitol, sorbitol and mannitol. The hydroxyoxetane employed in the process of the present invention is preferably a 3-alkyl-3-(hydroxyalkyl)oxetane, a 3,3-di(hydroxyalkyl)oxetane, a 3 -alky 1-3 -(hydroxy alkoxy)- oxetane, a 3-alkyl-3-(hydroxyalkoxyalkyl)oxetane or a dimer, trimer or polymer of a 3-alkyl-3-(hydroxyalkyl)oxetane, a 3,3-di(hydroxyalkyl)oxetane, a 3-alkyl-3-(hydroxyalkoxy)- oxetane or a 3-alkyl-3-(hydroxyalkoxyalkyl)oxetane. Alkyl is here preferably C 1 -C 24 , such as C 1 -C 12 or Cj-Cg, linear or branched alkanyl or alkenyl and alkoxy preferably ethoxy, propoxy, butoxy, phenylethoxy nominally comprising 0.2-20 alkoxy units or is a combination of two or more of said alkoxy nominally comprising 0.2-10 units of respective alkoxy and nominally comprising a total of 0.2-20 alkoxy units. Said at least one hydroxyoxetane is in especially preferred embodiments 3 -methyl-3 -(hydroxymethyl)oxetane, 3 -ethyl-3 -(hydroxymethyl)oxetane, 3 ,3 -di(hydroxy- methyl)oxetane or a combination and/or mixture of two or more of said hydroxyoxetanes. Said at least one cationic initiator is suitably and preferably at least one Lewis acid, such as AICI 3 , BF 3 , TiCl 4 , Znl 2 , SiF 4 , SbF 5 , PF 5 , AsF 5 or SbCl 5 and/or at least one halogenated acid, such as FSO 3 H, CISO 3 H, HCIO 4 , HIO 4 or CF 3 SO 3 H. The alkaline compound added for neutralisation of yielded product is advantegously selected from the group consisting of hydroxides and carbonates of at least one alkali metal or alkaline earth metal. Further suitable alkaline compounds include ammonia and amines. Without further elaboration, it is believed that one skilled in the art can, using the preceding description, utilise the present invention to its fullest extent. The following preferred specific embodiments are, therefore, to be construed as merely illustrative and not limitative of the remainder of the disclosure in any way whatsoever. In the following, Example 1 (Reference) disclose cationic polymerisation, outside the scope of the present invention, of a hydroxyoxetane, Examples 2-4 refer to embodiments of the process of the present invention and Example 5 (Comparative) refer to a process for preparation of a dendritic polyether similar to Examples 2-4, the synthesis being performed at a temperature above onset at thermal degradation. Graphs 1-5 present the GPC (general purpose chromatography) profiles of the products obtained in Examples 1-5 and Graph 6 and 7 present DSC (differential scanning calorimetry) and TGA (thermal gravimetric analysis) measurements of a neutralised and a non-neutralised sample of the product obtained in Example 2. Graph 8 present a comparison between products obtained in Example 3 (Embodiment) and Example 5 (Compartive) with regard to residual monomer (hydroxyoxetane) content). Example 1 (Reference) A dendritic polyether without core was prepared from a hydroxyoxetane by ring opening polymerisation. 1.0 g of a solution (50% in diethylether) of BF 3 was at room temperature charged to a reactor equipped with a mechanical stirrer, a cooler and a heating system with adequate heating control. The temperature was increased to 120°C and 500.0 g of 3-ethyl-3-(hydroxymethyl)oxetane (TMPO, Perstorp Specialty Chemicals, Sweden) was fed continuously to the reactor during 30 minutes in order to control the exothermic character of the reaction. The strong exotherm was seen as a result of the ring opening polymerization of the oxetane monomer. Once the exotherm faded, the reaction mixture was kept at 120°C under stirring for a further 3.5 hours. The reaction mixture was then cooled to room temperature and the final product was recovered. The obtained dendritic polyether exhibited following characteristics: Hydroxyl value, mg KOH/g: 482 Molecular weight average (Mw), g/mole: 8 297 Polydispersity: 11.4 Low molecular weight compounds (<400 g/mole), %: 3.8 Nominal hydroxyl functionality: 56 Chemical conversion, %: * 99.1 Viscosity (110°C, 30s- 1 ), Pa.s: 52 * with regard to residual monomer content The GPC profile of yielded product is given in Figure 1. Example 2 A dendritic polyether comprising a core and-three-branching generations was prepared from a tetrahydric alcohol and a hydroxyoxetane by ring opening addition and polymerisation. 49.18 g of an ethoxylated pentaerythritol (Polyol PP50, Perstorp Specialty Chemicals, Sweden) was at room temperature mixed with 1.00 g of a solution (50% in diethylether) of BF 3 , giving a ratio OF£:BF 3 of 1:0.013, and charged to a reactor equipped with a mechanical stirrer, a cooler and a heating system with adequate heating control. The mixture was heated to 110°C and 450.00 g of 3-ethyl-3-(hydroxymethyl)oxetane (TMPO, Perstorp Specialty Chemicals, Sweden) was continuously fed to said mixture at a rate of 12.85 g/min (feeding time 35 minutes). Heating was during feeding not necessary because of the exotherm and cooling was used during said feeding time and for a further 30 minutes. Heating was then necessary in order to maintain a temperature of 110°C. The reaction was allowed to continue under stirring for a further 3.5 hours. The reaction mixture was then cooled to room temperature and the final product was recovered. The obtained dendritic polyether exhibited following characteristics: Hydroxyl value, mg KOH/g: 504 Peak molecular weight, (GPC) g/mole: 2 857 Polydispersity: 1.41 Low molecular weight compounds (< 400 g/mole), %: 1.8 Nominal hydroxyl functionality: 25.6 Chemical conversion, %: * 99.7 Viscosity (110°C, 30s- 1 ), Pa.s: 3.6 Glass transition temperature, °C: 32 * with regard to residual monomer content The GPC profile of yielded product is given in Figure 2. 100 g of obtained dendric polyether was heated to 110°C in a reactor equipped with a mechanical stirrer. 0.4g of an aqueous solution of NaOH (41%) was added to the melt and stirred for 10 minutes. A small sample was tested in a DSC Mettler TA8000 between room temperature and 320°C in air. Heating rate was 10°C/min. The neutralised sample was compared to a sample collected before neutralisation. The result is given in enclosed Graph 6 (DSC) and Graph 7 (TGA) evidencing the improved stability of the neutralised sample. The onset at degradation is increased with 80-100°C by addition of a small amount of a base. Example 3 A dendritic polyether comprising a core and four branching generations was prepared from a tetrahydric alcohol and a hydroxyoxetane by ring opening addition and polymerisation. 23.97 g of an ethoxylated pentaerythritol (Polyol PP50, Perstorp Specialty Chemicals, Sweden) was at room temperature mixed with 0.98 g of a solution (50% in diethylether) of BF 3 , giving a ratio OH:BF 3 of 1:0.012, and charged to a reactor equipped with a mechanical stirrer, a cooler and a heating system with adequate heating control. The mixture was heated to 110°C and 470.00 g of 3-ethyl-3-(hydroxymethyl)oxetane (TMPO, Perstorp Specialty Chemicals, Sweden) was continuously fed to said mixture at a rate of 13.4 g/min (feeding time 35 minutes). Heating was during feeding not necessary because of the exotherm and cooling was used during said feeding time and for a further 30 minutes. Heating was then necessary in order to maintain a temperature of 110°C. The reaction was allowed to continue under stirring for a further 3.5 hours. The reaction mixture was then cooled to room temperature and the final product was recovered. The obtained dendritic polyether exhibited following characteristics: Hydroxyl value, mg KOH/g: 496 Peak molecular weight, (GPC) g/mole: 3 763 Polydispersity: 1.59 Low molecular weight compounds (< 400 g/mole), %: 3.2 Nominal hydroxyl functionality: 33.3 Chemical conversion, %: * 99.8 Viscosity (110°C, 30s" 1 ), Pa.s: 8.6 Glass transition temperature, °C: 38 * with regard to residual monomer content The GPC profile of yielded product is given in Figure 3. Obtained dendritic polyether was neutralised as in Example 2. Example 4 A dendritic polyether comprising a core and three branching generations was prepared from a trihydric alcohol and a hydroxyoxetane by ring opening addition and polymerisation. 26.10 g of an trimethylolpropane (Perstorp Specialty Chemicals, Sweden) was heated to 120°C and mixed with 0.99 g of a solution (50% in diethylether) of BF 3 , giving a ratio OH:BF 3 of 1 :0.013, and charged to a reactor equipped with a mechanical stirrer, a cooler and a heating system with adequate heating control. 470.00 g of 3-ethyl-3-(hydroxymethyI)oxetane (TMPO, Perstorp Specialty Chemicals, Sweden) was continuously fed to the mixture at a rate of 13.4 g/min (feeding time 35 minutes). Heating was during feeding not necessary because of the exotherm and cooling was used during said feeding time and for a further 30 minutes. Heating was then necessary in order to maintain a temperature of 110°C. The reaction was allowed to continue under stirring for a further 3.5 hours. The reaction mixture was then cooled to room temperature and the final product was recovered. The obtained dendritic polyether exhibited following characteristics: Hydroxyl value, mg KOH/g: 524 Peak molecular weight, (GPC) g/mole: 2 892 Polydispersity: 1.61 Low molecular weight compounds (< 400 g/mole), %: 4.1 Nominal hydroxyl functionality: 27 Chemical conversion, %: * 99.9 Viscosity (110°C, 30s- 1 ), Pa.s: 10.3 Glass transition temperature, °C: 43 * with regard to residual monomer content The GPC profile of yielded product is given in Figure 4. Obtained dendritic polyether was neutralised as in Example 2.

Claims: Example 5 (Comparative) A dendritic polyether comprising a core and tliree branching generations was prepared from a tetrahydric alcohol and a hydroxyoxetane by ring opening addition and polymerisation. The reaction temperature was kept above onset at thermal degradation. 49.18 g of an ethoxylated pentaerythritol (Polyol PP50, Perstorp Specialty Chemicals, Sweden) was at room temperature mixed with 1.00 g of a solution (50% in diethylether) of BF 3 , giving a ratio OHBF 3 was 1:0.013, and charged to a reactor equipped with a mechanical stirrer, a cooler and a heating system with adequate heating control. The mixture was heated to 130°C and 450.00 g of 3-ethyl-3-(hydroxymethyl)oxetane (TMPO, Perstorp Specialty Chemicals, Sweden) was continuously fed to said mixture at a rate of 12.9 g/min (feeding time 35 minutes). Heating was during feeding not necessary because of the exotherm and cooling was used during said feeding time and for a further 30 minutes. Heating was then necessary in order to maintain a temperature of 130°C. The reaction was allowed to continue under stirring for a further 3.5 hours. The reaction mixture was then cooled to room temperature and the final product was recovered. The obtained dendritic polyether exhibited following characteristics: Hydroxyl value, mg KOH/g: 499 Peak molecular weight, (GPC) g/mole: 2 679 Polydispersity: 1.42 Low molecular weight compounds (< 400 g/mole), %: 4.8 Nominal hydroxyl functionality: 23.8 Chemical conversion, %: * 92.5 Viscosity (110°C, 30s- 1 ), Pa.s: 2.6 * with regard to residual monomer content The GPC profile of yielded product is given in Figure 5. CLAIMS 1. A process for manufacture of a dendritic polyether comprising a core, derived from a compound having two or more hydroxyl groups, and at least one branching generation being built up from at least one hydroxyoxetane having one oxetane group and at least one hydroxyl group, said process comprising ring opening addition to said core and ring opening polymerisation of said oxetane characterised in, that a mixture of said compound having said two or more hydroxyl groups and at least one cationic initiator is prepared and optionally heated to 90-130°C, that said hydroxyoxetane is fed to said mixture at a rate resulting in and/or maintaining a reaction temperature, during said ring opening addition and said ring opening polymerisation, being below onset at thermal degradation and in an amount resulting in said at least one branching generation, that said initiator is present in an amount of 0.1-0.5% by weight calculated on said core and said hydroxyoxetane, preferably in an amount giving a ratio hydroxyl groups to initiator of between 1:0.01 and 1:0.05, and that yielded dendritic polyether is neutralised by addition of at least one alkaline compound and optionally purified. 2. A process according to Claim 1 c h a r a c t e r i s e d i n, that said reaction temperature is 110 ± 20°C, such as 100 ± 10°C. 3. A process according to Claim 1 or 2 c h a r a c t e r i s e d i n, that said hydroxyoxetane is fed to said mixture during at least 30 minutes. 4. A process according to any of the Claims 1-3 characterised in,- that yielded dendritic polyether comprises at least two branching generations. 5. A process according to any of the Claims 1-4 characterised in, that yielded dendritic polyether has a polydispersity of less than 2, preferably less than 1.8 and most preferably less than 1.6. 6. A process according to any of the Claims 1-5 characterised in, that yielded dendritic polyether has thermal degradation point of more than 200°C, preferably more than 250°C. 7. A process according to any of the Claims 1-6 characterised in, that yielded dendritic polyether has a residual monomer content of less than 1%, preferably less than 0.8%) and most preferably less than 0.6% by weight. 8. A process according to any of the Claims 1-7 characterised in, that said compound having said at least two hydroxyl groups is a di, tri or polyhydric alcohol, a di, tri or polyhydric ester or polyester or a di, tri or polyhydric ether or polyether. . A process according to any of the Claims 1-7 characterised in, that said compound having said at least two hydroxyl groups is a 5,5-dihydroxyalkyl-l,3-dioxane, a 5,5-di(hydroxyalkoxy)-l,3-dioxane, a 5,5-di(hydroxyalkoxyalkyl)-l,3-dioxane, a 2-alkyl-l,3-propanediol, a 2,2-dialkyl-l,3-propanediol, a 2-hydroxy-l,3-propanediol, a 2,2-dihydroxy-l,3-propanediol, a 2-hydroxy-2-alkyl-l,3-propanediol, a 2-hydroxyalkyl- -2-alkyl-l,3-propanediol, a 2,2-di(hydroxyalkyl)-l,3-propanediol, a 2-hydroxy- alkoxy-2-alkyl-l,3-propanediol, a 2,2-di(hydroxyalkoxy)-l,3-propanediol, a 2-hydroxyalkoxyalkyl-2-alkyl-l,3-propanediol or a 2,2-di(hydroxyalkoxyalkyl)-l,3- -propanediol 10. A process according to any of the Claims 1-7 characterised in, that said compound having said at least two hydroxyl groups is a dimer, trimer or polymer of a 5,5-dihydroxyalkyl-l,3-dioxane, a 5,5-di(hydroxyalkoxy)-l,3-dioxane, a 5,5-di(hydroxy- alkoxyalkyl)-l,3-dioxane, a 2-alkyl-l,3-propanediol, a 2,2-dialkyl-l,3-propanediol, a 2-hydroxy-l,3-propanediol, a 2,2-dihydroxy-l,3-propanediol, a 2-hydroxy-2-alkyl- -1,3-propanediol, a 2-hydroxyalkyl-2-alkyl-l,3-propanediol, a 2,2-di(hydroxyalkyl)-l,3- -propanediol, a 2-hydroxyalkoxy-2-alkyl-l,3-propanediol, a 2,2-di(hydroxyalkoxy)- -1,3-propanediol, a 2-hydroxyalkoxyalkyl-2-alkyl-l,3-propanediol or a 2,2-di(hydroxy- alkoxyalkyl)- 1 ,3-propanediol. 11. A process according to Claim 9 or 10 characterised in, that said alkyl is C 1 -C 24 , such as C 1 -C 12 or Ci-Cs, linear or branched alkanyl or alkenyl and that said alkoxy is ethoxy, propoxy, butoxy, phenylethoxy nominally comprising 0.2-20 alkoxy units or is a combination of two or more of said alkoxy nominally comprising 0.2-10 units of respective alkoxy and nominally comprising a total of 0.2-20 alkoxy units. 12. A process according to any of the Claims 1-7 characterised in, that said compound having said at least two hydroxyl groups is 5,5-dihydroxymethyl-l,3-dioxane, 2-methyl-l,3-propanediol, 2-methyl-2-ethyl-l,3-propanediol, 2-ethyl-2-butyl-l,3- -propanediol, neopentyl glycol, dimethylpropane, glycerol, trimethylolethane, trimethylolpropane, diglycerol, di(trimethylolethane), di(trimethylolpropane), pentaerythritol, di(pentaerythritol), anhydroenneaheptitol, sorbitol or mannitol. 13. A process according to any of the Claims 1-7 characterised in, that said compound having said at least two hydroxyl groups is a monoallyl or mono(methallyl) ether of glycerol, trimethylolethane or trimethylolpropane. 14. A process according to any of the Claims 1-7 characterised in, that said compound having said at least two hydroxyl groups is a monoallyl, diallyl, mono(methallyl) or di(methallyl) ether of di(trimethylolethane), di(trimethylolpropane) or pentaerythritol. 15. A process according to any of the Claims 1-7 characterised in, that said compound having said at least two hydroxyl groups is a l,ω-diol. 16. A process according to Claim 15 characterised in, that said l,ω-diol is a mono, di, tri or polyethylene glycol, a mono, di, tri or polypropylene glycol or an alkyl, alkoxy or alkoxyalkyl substituted species thereof. 17. A process according to Claim 15 characterised in, that said l,ω-diol is 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,6-cyclohexanedimethanol or an alkyl, alkoxy or alkoxyalkyl substituted species thereof. 18. A process according to Claim 16 or 17 characterised in, that said alkyl is C 1 -C 24 , such as C 1 -C 12 or Ci-Cs, linear or branched alkanyl or alkenyl and that said alkoxy is ethoxy, propoxy, butoxy, phenylethoxy nominally comprising 0.2-20 alkoxy units or is a combination of two or more of said alkoxy nominally comprising 0.2-10 units of respective alkoxy and nominally comprising a total of 0.2-20 alkoxy units. 19. A process according to any of the Claims 1-18 characterised in, that said hydroxyoxetane is a 3-alkyl-3-(hydroxyalkyl)oxetane, a 3,3-di(hydroxyalkyl)oxetane, a 3-alkyl-3-(hydroxyalkoxy)oxetane or a 3-alkyl-3-(hydroxyalkoxyalkyl)oxetane. 20. A process according to any of the Claims 1-18 characterised in, that said hydroxyoxetane is a dimer, trimer or polymer of a 3-alkyl-3-(hydroxyalkyl)oxetane, a 3,3-di(hydroxyalkyl)oxetane, a 3 -alky 1-3 -(hydroxy alkoxy)oxetane or a 3-alkyl-3-(hydroxyalkoxyalkyl)oxetane. 21. A process according to Claim 19 or 20 characterised in, that said alkyl is Cι-C 24 , such as C 1 - 2 or Cj-Cs, linear or branched alkanyl or alkenyl and that said alkoxy is ethoxy, propoxy, butoxy, phenylethoxy nominally comprising 0.2-20 alkoxy units or is a combination of two or more of said alkoxy nominally comprising 0.2-10 units of respective alkoxy and nominally comprising a total of 0.2-20 alkoxy units. 22. A process according to any of the Claims 1-21 characterised in, that said hydroxyoxetane is 3-methyl-3-(hydroxymethyl)oxetane, 3-ethyl-3-(hydroxymethyl)- oxetane or 3,3-di(hydroxymethyl)oxetane. 23. A process according to any of the Claims 1-22 characterised in, that said at least one cationic initiator is a Lewis acid, such as AICI 3 , BF 3 , TiC^, Znl 2 , SiF 4 , SbFs, PF 5 , AsF 5 or SbCl 5 . 24. A process according to any of the Claims 1-22 characterised in, that said at least one cationic initiator is a halogenated acid, such as FSO 3 H, CISO 3 H, HCIO 4 , HIO 4 or CF 3 SO 3 H. 25. A process according to any of the Claims 1-24 characterised in, that said alkaline compound is a hydroxide and/or carbonate of at least one alkali metal and/or alkaline earth metal. 26. A process according to any of the Claims 1-23 characterised in, that said alkaline compound is ammonia or an amine.

Inventors: BJOERNBERG HAAKAN, JAMES DAVID, MIDELF BIRGER, PETTERSSON BO, REHNBERG NICOLA, BJOERNBERG, HAAKAN, JAMES, DAVID, MIDELF, BIRGER, PETTERSSON, BO, REHNBERG, NICOLA
Applicants: BJOERNBERG HAAKAN, JAMES DAVID, MIDELF BIRGER, PERSTORP SPECIALTY CHEM AB, PETTERSSON BO, REHNBERG NICOLA, BJOERNBERG, HAAKAN, JAMES, DAVID, MIDELF, BIRGER, PERSTORP SPECIALTY CHEMICALS AB, PETTERSSON, BO, REHNBERG, NICOLA
Application year: 2001
Main classification: C08G83
IPC codes: C08G65, C08G83