PROCESS FOR THE CARBONYLATION OF ACETYLENICALLY UNSATURATED COMPOUNDS

Abstract: Process for the preparation of alpha,beta-olefinically unsaturated compounds by means of carbonylation of acetylenically unsaturated compounds with carbon monoxide in the presence of a hydroxyl-containing compound in the liquid phase, carried out in the presence of a catalytic system that can be formed from: (a) a palladium compound (b) a protonic acid (c) an organic phosphine according to the formula wherein R₁ represents a heterocyclic 5 or 6 atom ring, comprising at least nitrogen as hetero atom, which ring is optionally substituted and/or may form part of a larger condensed ring structure that is optionally substituted, and wherein R₂ and R₃ each have the afore­ said meaning of R₁ or may represent an optionally substituted aryl group, and organic phosphines and compositions comprising said phosphines as well as catalytic systems whereof said phosphines form part.

Description: The invention relates to a process for the carbonylation of an acetylenically unsaturated compound with carbon monoxide in the presence of a hydroxyl-containing compound in the liquid phase. It is known that acetylenically unsaturated compounds can be carbonylated in the presence of a hydroxyl-containing compound such as an alcohol, phenol, water or a carboxylic acid to produce alpha,beta-olefinically unsaturated esters, acids or anhydrides respectively. In all cases, the known methods exhibit low selectivity towards the desired compounds and a relatively low conversion rate and are therefore regarded as unattractive for use on a commercial scale. As a result of that opinion on the part of those skilled in the art, as, for example, transpires from column 2, lines 53-56, of US patent specification 3,887,595, those skilled in the art have not been primarily inclined to direct further research towards that type of reaction in the search for methods for the preparation of cheaper and attractive base materials desired for further organic syntheses. On the other hand, the demand for cheaper base materials desired for further organic chemical syntheses has been steadily growing over the years. It is remarked that US-A-4,257,973 discloses a process for carbonylation of aliphatically unsaturated compounds using a catalyst system composed of a dihalobis(phosphine)palladium complex and from 0.5 to 5 moles of a metal halide promoter. Suitable phosphine ligands are mentioned in columns 5 and 6 of this publication, and include phosphines having a N-piperidinyl or N-pyrrolidinyl group. Despite the use of metal halide promoters the selectivities and conversion rates are unattractive for commercial application. EP-A-259914 publication date 16.03.88 discloses a catalyst system comprising a palladium compound, an acid with a pKa of less than 2, and a phosphine having a group containing a nitrogen atom. These catalyst systems are used for a different reaction. EP-A-186,228 discloses the carbonylation of acetylenically unsaturated compounds using catalyst systems formed from a palladium compound, an organic phosphine and a protonic acid except hydrohalogenic acids. The disclosed organic phosphines comprise alkyl, cycloalkyl and/or aryl substituents, and no suggestion to the use of phosphines having an N-heterocyclic ring substituent can be derived from this document. Though good selectivities and activities are achieved with these known catalyst systems, further enhancement is still highly desirable in commercial application. The object of the present invention is therefore to provide an improved process for the preparation of alpha,beta-olefinically unsaturated esters, acids or anhydrides. As a result of extensive research and development, an improved process has now surprisingly been found for the preparation of alpha,beta-olefinically unsaturated compounds by means of the carbonylation of an acetylenically unsaturated compound with carbon monoxide in the presence of a hydroxyl-containing compound in the liquid phase, carried out in the presence of a catalytic system that can be formed from: (a) a palladium compound (b) a protonic acid, and (c) an organic phosphine according to the formula wherein R₁ represents a heterocyclic 5 or 6 atom ring comprising at least nitrogen as hetero atom, which ring is optionally substituted and/or may form part of a larger condensed ring structure that is optionally substituted, and wherein R₂ and R₃ each have the aforesaid meaning of R₁ or may represent an optionally substituted aryl group. Examples of heterocyclic rings according to the definitions of R₁, R₂ and R₃ are pyridyl, pyrazinyl, quinolyl, isoquinolyl, pyrimidinyl, pyridazinyl, indolizinyl, cinnolinyl, acridinyl, phenazinyl, phenanthridinyl, phenanthrolinyl, phthalazinyl, naphthyridinyl, quinoxalinyl and quinazolinyl. Of those groups, pyridyl, pyrazinyl and pyridazinyl are preferred. Said heterocyclic groups and the aforesaid aryl groups according to the definitions of R₁, R₂ and R₃ may be substituted with one or more electron-repelling or electron-attracting groups. Examples of electron-repelling substituents on the aforesaid groups are alkoxy groups and in particular those with not more than 5 carbon atoms, for example methoxy and ethoxy groups, alkyl groups with not more than 5 carbon atoms, such as methyl, ethyl, n-propyl, isopropyl-tert-butyl or dimethylamino and diethylamino groups. Examples of electron-attracting substituents on the aforesaid groups are halogenic such as chlorine and fluorine, trifluoromethyl, trichloromethyl, monochloromethyl and m-methoxy groups. The optionally substituted aryl groups of the definitions R₂ and R₃ contain not more than 18 carbon atoms in the ring system and may consist of anthryl, naphthyl and, preferably, phenyl. Phosphines according to the general formula I wherein R₁ represents a pyridyl and R₂ and R₃ represent an optionally substituted phenyl are preferred. According to a preferred embodiment of the present invention wherein diphenyl-2-pyridylphosphine is used, not only very high selectivities towards alpha,beta-olefinically unsaturated acids or esters, but also high yields can be obtained. Other examples of suitable phosphines are: di(p-methoxyphenyl) 2-pyridylphosphine di(p-tolyl) 2-pyridylphosphine di(o-methoxyphenyl) 2-pyridylphosphine di(o-chlorophenyl) 2-pyridylphosphine di(m-methoxyphenyl) 2-pyridylphosphine di(m-chlorophenyl) 2-pyridylphosphine di(p-methoxyphenyl) 3-pyridylphosphine di(p-tolyl) 3-pyridylphosphine di(o-methoxyphenyl) 3-pyridylphosphine di(o-chlorophenyl) 3-pyridylphosphine di(m-methoxyphenyl) 3-pyridylphosphine di(m-chlorophenyl) 3-pyridylphosphine di(p-methoxyphenyl) 4-pyridylphosphine di(p-tolyl) 4-pyridylphosphine di(o-methoxyphenyl) 4-pyridylphosphine di(o-chlorophenyl) 4-pyridylphosphine di(m-methoxyphenyl) 4-pyridylphosphine di(m-chlorophenyl) 4-pyridylphosphine diphenyl(3-methoxy-2-pyridyl) phosphine diphenyl(4-methoxy-2-pyridyl) phosphine diphenyl(4-chloro-2-pyridyl) phosphine diphenyl(2-methoxy-3-pyridyl) phosphine diphenyl(4-methoxy-3-pyridyl) phosphine diphenyl(4-chloro-3-pyridyl) phosphine diphenyl(3-methoxy-4-pyridyl) phosphine diphenyl(3-chloro-4-pyridyl) phosphine diphenyl(5-chloro-4-pyridyl) phosphine diphenyl(5-methoxy-4-pyridyl) phosphine di(p-tolyl)(3-methoxy-4-pyridyl) phosphine di(p-tolyl)(3-chloro-4-pyridyl) phosphine di(m-methoxyphenyl)(3-chloro-4-pyridyl) phosphine di(m-methoxyphenyl)(3-methoxy-4-pyridyl) phosphine di(m-chlorophenyl)(3-methoxy-4-pyridyl) phosphine di(p-tolyl)(3-methoxy-2-pyridyl) phosphine di(p-tolyl)(3-chloro-2-pyridyl) phosphine di(m-methoxyphenyl)(3-chloro-2-pyridyl) phosphine di(m-methoxyphenyl)(3-methoxy-2-pyridyl) phosphine di(m-tert.butoxyphenyl)(3-chloro-2-pyridyl) phosphine di(m-tert.butoxyphenyl)(3-methoxy-2-pyridyl) phosphine di(m-tert.butoxyphenyl)(3-chloro-4-pyridyl) phosphine di(m-tert.butoxyphenyl)(3-methoxy-4-pyridyl) phosphine di(m-tert.butoxyphenyl)(2-methoxy-3-pyridyl) phosphine di(m-tert.butoxyphenyl)(2-chloro-3-pyridyl) phosphine di(m-chlorophenyl)(2-methoxy-3-pyridyl) phosphine di(m-chlorophenyl)(2-chloro-3-pyridyl) phosphine di(o-chlorophenyl)(2-methoxy-3-pyridyl) phosphine di(p-methoxyphenyl) 2-pyrimidinylphosphine di(p-tolyl) 2-pyrimidinylphosphine di(o-methoxyphenyl) 2-pyrimidinylphosphine di(o-chlorophenyl) 2-pyrimidinylphosphine di(m-methoxyphenyl) 2-pyrimidinylphosphine di(p-methoxyphenyl) 2-pyridazinylphosphine di(p-tolyl) 2-pyridazinylphosphine di(o-methoxphenyl) 2-pyridazinylphosphine di(o-chlorophenyl) 2-pyridazinylphosphine di(n-methoxyphenyl) 2-pyridazinylphosphine di(p-methoxyphenyl)(3-methoxy-2-pyrimidinyl) phosphine di(p-tolyl)(3-methoxy-2-pyridinyl) phosphine di(o-chlorophenyl)(3-chloro-2-pyrimidinyl) phosphine di(m-methoxyphenyl)(3-chloro-2-pyrimidinyl) phosphine di(p-tolyl)(4-methoxy-3-pyridazinyl) phosphine di(p-methoxyphenyl)(4-methoxy-3-pyridazinyl) phosphine di(o-chlorophenyl)(4-methoxy-3-pyridazinyl) phosphine phenyl di(3-methoxy-2-pyridyl) phosphine phenyl di(4-methoxy-2-pyridyl) phosphine phenyl di(4-chloro-2-pyridyl) phosphine phenyl di(2-methoxy-3-pyridyl) phosphine phenyl di(4-methoxy-3-pyridyl) phosphine phenyl di(4-chloro-3-pyridyl) phosphine phenyl di(3-methoxy-4-pyridyl) phosphine phenyl di(3-chloro-4-pyridyl) phosphine phenyl di(5-chloro-4-pyridyl) phosphine phenyl di(5-methoxy-4-pyridyl) phosphine phenyl di(3-methoxy-2-pyrimidinyl) phosphine phenyl di(3-chloro-2-pyrimidinyl) phosphine phenyl di(4-methoxy-2-pyrimidinyl) phosphine phenyl di(4-methoxy-3-pyridazinyl) phosphine and phenyl di(4-chloro-3-pyridazinyl) phosphine. As protonic acid a wide variety of acids or mixtures thereof may be used. Examples of such acids are: orthophosphoric acid, pyrophosphoric acid, sulphuric acid, hydrohalogenic acids, benzenephosphonic acid, benzenesulphonic acid, p-toluenesulphonic acid, naphthalenesulphonic acid, toluenephosphonic acid, chlorosulphonic acid, fluorosulphonic acid, monochloroacetic acid, dichloroacetic acid, trichloroacetic acid, trifluoroacetic acid, oxalic acid, terephthalic acid, perchloric acid, 2-hydroxypropane-2-sulphonic acid, trifluoromethanesulphonic acid or mixtures thereof. Of said acids, para-toluenesulphonic acid and benzenephosphonic acid are preferred. Hydrohalogenic acids can, in principle, be used but have the known drawback that they induce a corrosive effect. Both homogeneous as well as hetereogeneous palladium compounds may be used in the process according to the present invention. Homogeneous compounds are preferred. Suitable homogeneous compounds are palladium salts of nitric acid, sulphuric acid or alkanecarboxylic acids with not more 12 carbon atoms per molecule. Salts of hydrohalogenic acids may, in principle, be used as well but these have the drawback that the halide ion may induce a corrosive effect. Preferably, palladium acetate is used as catalyst component. Palladium complexes may also be used such as palladium acetylacetonate, tetrakis-triphenylphosphinepalladium, bis-tri-o-tolylphosphinepalladium acetate or bis-diphenyl-2-pyridylphosphinepalladium acetate, tetrakis-diphenyl-2-pyridylphosphinepalladium and bis-di-o-tolylpyridylphosphinepalladium acetate or bis-diphenyl-pyridylphosphinepalladium sulphate. The quantity of the palladium compound is not critical. Preferably, quantities are used within the range of 10⁻⁷ to 10⁻¹ gram atom palladium per mol acetylenically unsaturated compound. The molar ratio of the organic phosphine to palladium is not critical and may vary between wide limits. Very high selectivity, i.e. >98%, and high conversion rates, for example 10,000 - 40,000 mol/g atom Pd/hour are achieved if more than 2 and preferably less than 500 mol organic phosphine are used per gram atom palladium. In general, quantities of more than 1,000 mol organic phosphine per gram atom palladium are not necessary. The number of protonic acid equivalents used per organic phosphine equivalent is not critical and may vary between wide limits. Quantities in the range of 0.1 to 50 protonic acid equivalents per organic phosphine equivalent are preferably used. A separate solvent is not essential for the process according to the invention. A large excess of one of the reactants, mostly the alcohol, can often form a suitable liquid phase. In some cases, however, it may be desirable to use a separate solvent. Any inert solvent can be used for that purpose. Said solvent may, for example, comprise sulphoxides and sulphones, for example dimethylsulphoxide, diisopropylsulphone or tetrahydrothiophene-2,2-dioxide (also referred to as sulfolane), 2-methylsulfolane, 3-methylsulfolane, 2-methyl-4-butylsulfolane; aromatic hydrocarbons such as benzene, toluene, xylenes; esters such as methylacetate and butyrolactone; ketones such as acetone or methyl isobutyl ketone and ethers such as anisole, 2,5,8-trioxanone (also referred to as diglyme), diphenyl ether and diisopropyl ether. Particularly good results are obtained when N-methylpyrrolidone is used as main solvent or as co-solvent. It will be clear to those skilled in the art that the good effect of N-methylpyrrolidone must be regarded as highly surprising on account of the known retarding effect of NMP on other alkene conversions of this type. The method according to the present invention allows the use of very mild reaction conditions. Temperatures in the range of 20°C to 200°C and in particular from 20°C to 80°C are suitable. Pressure can vary over a wide range but will generally be lower than that employed in the hitherto known processes. Pressures from 5 to 70 bar are preferred. Pressures higher than 100 bar may be used, but are generally economically unattractive on account of special apparatus requirements. The molar ratio of the alcohol, phenol, water or carboxylic acid to the acetylenically unsaturated compounds may vary between wide limits and generally lies within the range of 0.01:1 to 100:1. The process according to the present invention can be accomplished with the use of a wide variety of acetylenically unsaturated compounds which under certain circumstances may carry one or more substituents that are inert under the reaction conditions in question, such as halogen atoms and cyano, ester, alkoxy and aryl groups. Moreover, the acetylenically unsaturated compounds may comprise one or more substituents that are not inert under the reaction conditions, for example hydroxy groups. The behaviour of such groups will depend on the precise reaction conditions. One or more acetylenically unsaturated bonds may be present in any position in the carbon chain. Very good results are obtained with unsubstituted alkynes and in particular with those with up to 20 carbon atoms per molecule, and more particularly with acetylene, propyne and phenylacetylene. Other examples of suitable alkynes are: 1-butyne, 2-butyne, 1-pentyne, 1-hexyne, 1-heptyne, 1-octyne, 2-octyne, 4-octyne, 5-methyl-3-heptyne, 4-propyl-2-pentyne, 1-nonyne, benzylethyne and cyclohexylethyne. Alkynes can be used in pure form or in mixtures with alkenes. It has been found that the alkenes are inert under the reaction conditions. An extensive series of hydroxyl compounds can be used as reagents in the process according to the present invention. For example, the alcohol used may be aliphatic, cycloaliphatic or aromatic and may carry one or more inert substituents. A suitable alcohol may comprise up to 20 carbon atoms per molecule. One or more hydroxyl groups may be present, in which case several products may be formed, depending on the molar ratio of the reagents used. For example, a polyvalent alcohol, in particular lower sugars such as glucose, fructose, mannose, galactose, sucrose, aldoxose, aldopentose, altrose, allose, talose, gulose, idose, ribose, arabonose, xylose, lyxose, erythrose and threose can be allowed to react with a small quantity of an acetylenically unsaturated compound in order to form a monoester, or with a large quantity of an acetylenically unsaturated compound in order to form a polyvalent ester. The choice of alcohol will therefore depend solely on the product desired. The use of water produces, in the first instance, alpha, beta-unsaturated carboxylic acids. The use of alcohols produces alpha,beta-unsaturated esters and these can naturally be the polyesters described hereinbefore. Alkanols such as methanol, ethanol, propanol or 2,2-dihydroxymethyl-1-butanol, and alcohols comprising ether bridges, such as, for example, tri-ethylene glycol, all yield valuable products. According to a preferred embodiment of the process according to the present invention, lower sugars can be selectively converted to form monomers which can be further converted into attractive water-soluble polymers. Selectivity towards the product desired can be achieved by temporarily protecting hydroxyl groups which must not take part in the reaction, thus allowing to react exclusively primary or secondary hydroxyl groups. The process according to the present invention can be carried out using a wide variety of carboxylic acids. For example, the carboxylic acids may be aliphatic, cycloaliphatic or aromatic and may carry one or more inert substituents, such as those named in connection with the acetylenically unsaturated compounds. Carboxylic acids suitable for use contain up to 20 carbon atoms. One or more carboxylic acid groups may be present, thus allowing various products as desired, depending on the molar ratio of the reactants used. The carboxylic acids may, for example, be alkanecarboxylic acids or alkenecarboxylic acids. Examples of suitable carboxylic acids are: formic acid, acetic acid, propionic acid, n-butyric acid, isobutyric acid, pivalic acid, n-valeric acid, n-caproic acid, caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, benzoic acid, o-phthalic acid, m-phthalic acid, terephthalic acid and toluic acid. Examples of alkenecarboxylic acids are acrylic acid, propiolic acid, methacrylic acid, crotonic acid, isocrotonic acid, oleic acid, maleic acid, fumaric acid, citraconic acid and mesaconic acid. If an alkenecarboxylic acid with n+1 carbon atoms per molecule reacts with an alkyne with n carbon atoms per molecule, a symmetrical anhydride is produced. In other cases, a composite anhydride is produced in the first instance, possibly followed by transesterification. If, for example, an excess of acetic acid is allowed to react according to the present invention with propyne and carbon monoxide, a mixture of acetic anhydride and methacrylic acid will finally be formed. If it is desired to produce a special acid by means of the method according to the present invention, it may, for example, be favourable to allow one mol of the acid in question to react with the corresponding alkyne having one carbon atom less in order to form the symmetrical anhydride, to hydrolyze the anhydride in order to form two mols of the acid and to recycle one mol of that acid to the first stage of the process. Depending on the presence of further compounds, further reactions may take place. For example, if the process according to the present invention is carried out in the presence of an amine, that amine may react with the carboxylic anhydride to form a carboxylic acid and an amine carboxylate. For example, in the reaction of propyne with carbon monoxide and methacrylic acid in the presence of piperidine a high yield of 1-methacryloylpiperidine is obtained. The carbon monoxide required for the process according to the present invention may be used in a practically pure form or diluted with some inert gas, for example nitrogen. The presence of more than small quantities of hydrogen in the gas stream is undesirable on account of the hydrogenation of the acetylenically unsaturated compound that will then occur under the reaction conditions. In general, it is preferred that the quantity of hydrogen in the gas stream supplied is less than 5 vol%. The selectivity towards alpha,beta-olefinically unsaturated compounds, expressed as a percentage, is defined as a / b x 100 wherein "a" is the quantity of acetylenically unsaturated compound converted into alpha,beta-olefinically unsaturated compound and "b" is the total quantity of acetylenically unsaturated compound that has been converted. Organic phosphines according to the present invention can suitably be mixed with appropriate quantities of a palladium compound and/or a protonic acid, as defined hereinbefore, optionally dissolved or suspended in a separate solvent, preferably comprising dimethyl sulphoxide, diisopropyl sulphone, sulfolane, benzene, toluene, xylenes, methyl acetate, butyrolactone, acetone, methyl isobutyl ketone, anisole, diglyme, diphenyl ether, diisopropyl ether, and N-methylpyrrolidone. Preferably, the molar ratio of phosphine to palladium ranges from 2 to 500 mol phosphine per gram atom palladium, and the number of protonic acid equivalents per phosphine equivalent ranges from 0.1 to 50. The present invention further relates to a catalyst system comprising: (a) a palladium compound, (b) a protonic acid, (c) an organic phosphine according to the formula wherein R₁ represents a heterocyclic 5 or 6 atom ring, comprising at least nitrogen as hetero atom, which ring is optionally substituted and/or may form part of a larger condensed ring structure that is optionally substituted and wherein R₂ and R₃ each have the aforesaid meaning of R₁ or may represent an optionally substituted aryl group. The heterocyclic rings in the definitions of R₁, R₂ and R₃ suitably comprise pyridyl, pyrazinyl, quinolyl, isoquinolyl, pyrimidinyl, pyridazinyl, indolizinyl, cinnolinyl, acridinyl, phenazinyl, phenanthridinyl, phenanthrolinyl, phthalazinyl, naphthyrindinyl, quinoxalinyl and quinazolinyl. Of those groups pyridyl, pyrazinyl and pyridazinyl are preferred. A catalyst system, wherein R₂ and/or R₃ represent phenyl, or wherein R₁ represents pyridyl, R₂ pyridyl or phenyl and R₃ phenyl is preferred. Preferably, the molar ratio of the phosphine to palladium ranges from 2 to 500 mol phosphine per gram atom palladium, and the number of protonic acid equivalents per phosphine equivalents ranges from 0.1 to 50. The invention will now be illustrated by the following Examples. Example 1 A 300 ml magnetically stirred Hastelloy ® (Hastelloy is a Registered Trade Mark) autoclave was successively filled with 0.025 mmol palladium (II) acetate, 1 mmol diphenyl-2-pyridylphosphine, 2 mmol paratoluenesulphonic acid and 50 ml methanol. Air was evacuated from the autoclave, whereupon propyne was added to a pressure of 2 bar. Subsequently, carbon monoxide was added to a pressure of 60 bar. The autoclave was sealed and heated to a temperature of 45°C. After a reaction time of two hours at 45°C a specimen of the contents was analysed by means of gas liquid chromatography. The selectivity of the conversion of propyne to methyl methacrylate was found to be 99% while the mean conversion rate was calculated to be 20,000 mol propyne/g.atPd/hour. Example 2 The experiment as described in Example 1 was repeated in a virtually analogous manner with the same reactants and catalyst system except that 10 ml propylene was also added, while the reaction was performed at 55°C. By means of gas liquid chromatographical analysis, it was found that propyne had been converted to methyl methacrylate with a selectivity of 99%, while the product obtained was found to comprise less than 0.2% butyrate as by-product, which indicates that there was hardly any conversion of the admixed propylene under the reaction conditions selected according to the present invention. Mean reaction rate was calculated to be 20,000 mol propyne/g.atPd/hour. Example 3 The experiment as described in Example 1 was repeated in a virtually analogous manner except that as extra solvent 30 ml N-methylpyrrolidone was added simultaneously with the methanol, while the reaction was performed at 40°C with a reaction time of 1 hour. The selectivity of propyne to methyl methacrylate conversion amounted to 99%, while the mean conversion rate was calculated to be 40,000 mol propyne/g.atPd/hour. Example 4 The experiment as described in Example 1 was repeated in a virtually analogous manner with a catalyst system composed of 0.025 mmol palladium(II) acetate, 1 mmol phenyl di(2-pyridyl)phosphine and 2 mmol paratoluenesulphonic acid, a reaction temperature of 75°C and a reaction time of 2 hours. The selectivity of propyne to methyl methacrylate conversion amounted to 98%, while the mean conversion rate was calculated to be 10,000 mol propyne/g.atPd/hour. Example 5 The experiment as described in Example 1 was repeated in a virtually analogous manner with a catalyst system composed of 0.025 mmol palladium(II) acetate, 1 mmol tri(pyridyl)phosphine and 2 mmol paratoluenesulphonic acid, a reaction temperature of 80°C and a reaction time of 5 hours. The selectivity of propyne conversion to methyl methacrylate amounted to 97% and the mean conversion rate was 1500 mol propyne/g.atPd/hour. Example 6 The experiment as described in Example 1 was performed in a virtually analogous manner with a catalyst system composed of 0.025 mmol palladium(II) acetate, 1 mmol diphenyl(2-pyridyl)phosphine and 2 mmol benzenephosphonic acid. The reaction temperature was 50°C and the reaction time 5 hours. Propyne was converted into methyl methacrylate with a selectivity of 99%, while the mean conversion rate amounted to 4000 mol propyne/g.atPd/hour. Example 7 An experiment as described in Example 1 was performed in a virtually analogous manner with a catalyst system composed of 0.2 mmol palladium(II) acetate, 2 mmol diphenyl-2-pyridylphosphine and 2 mmol benzenephosphonic acid, except that as reactant 10 ml methacrylic acid and 50 ml anisole as solvent were added prior to evacuation of the reactor. Reaction temperature was 115°C and reaction time 1 hour. Propyne was converted to methacrylic anhydride with a selectivity of 98%, while the mean conversion rate amounted to 1500 mol propyne/g.atPd/hour. Example 8 The experiment of Example 7 was repeated with 3 mmol diphenyl-2-pyridylphosphine, 10 g phenol and 50 ml anisole. Reaction temperature was 90°C and reaction time 1 hour. Propyne was converted into phenyl methacrylate with a selectivity of 98%, while the mean conversion rate was 2000 mol propyne/g.atPd/hour. Example 9 In a virtually analogous manner as described in Example 1, an experiment was performed with a catalyst system composed of 0.025 mmol palladium(II) acetate, 1 mmol diphenyl-2-pyridylphosphine and 2 mmol paratoluenesulphonic acid, acetylene instead of propyne with an acetylene pressure of 1.4 bar, 30 ml methanol and as extra solvent N-methylpyrrolidone (30 ml). The reaction temperature was 40°C and the reaction time 1 hour. The selectivity of conversion of acetylene into methylacrylate was about 100%, while the calculated conversion rate was 2500 mol acetylene/g.atPd/hour. Example 10 In a virtually analogous manner as in Example 1, the reaction was performed with the same catalyst system as in Example 9, 20 ml phenylethyne, 30 ml methanol and 30 ml N-methylpyrrolidone. The reaction temperature was 40°C and the reaction time 1 hour. Phenylethyne was converted into methyl phenylacrylate with a selectivity of 98%, while the mean conversion rate was found to be 5500 mol phenylethyne/g.atPd/hour. Example 11 A virtually analogous experiment as in Example 10 was performed, except that now a catalyst system composed of 0.025 mmol palladium(II)-acetate, 1 mmol phenyl di(2-pyridyl)phosphine and 2 mmol paratoluenesulphonic acid was used. The reaction temperature was 60°C and the reaction time 2 hours. The selectivity of conversion of phenylethyne into methyl phenylacrylate was 98% and the mean conversion rate was 3000 mol phenylethyne/g.atPd/hour. Example 12 With the same catalyst system as in Examples 9 and 10, propyne was converted with carbon monoxide and glucose (10 gram) in 50 ml N-methylpyrrolidone in 1 hour at 40°C. The selectivity of conversion of propyne into the glucose ester of methacrylic acid was 95% and the mean conversion rate was 1300 mol propyne/g.atPd/hour. Example 13 With the same catalyst system as in Examples 9, 10 and 12, propyne was converted with carbon monoxide, water (10 ml) and N-methylpyrrolidone (40 ml) in 1 hour at 50°C. The selectivity of conversion into methacrylic acid was 98% and the mean conversion rate was 20,000 mol propyne/g.atPd/hour. Example 14 The same catalyst system as used in Examples 9, 10, 12 and 13 was used in an experiment for converting propyne with carbon monoxide and di-acetone-d-glucose (10 gram) in toluene (80 ml) in 1 hour at 40°C. The selectivity of the conversion of propyne into di-acetone-d-glucose ester of methacrylic acid was >98% and the mean conversion rate was 1000 mol propyne/g.atPd/hour.

Claims: Claims for the following Contracting States : BE, DE, FR, GB, IT A process for the preparation of alpha,beta-olefinically unsaturated compounds by means of carbonylation of acetylenically unsaturated compounds with carbon monoxide in the presence of a hydroxylated co-reactant and of a liquid phase, and in the presence of a catalytic system comprising a palladium compound and an organic phosphine, characterized in that the catalytic system is obtainable from the combination of: (a) a palladium compound (b) a protonic acid (c) an organic phosphine according to the formula wherein R₁ represents a heterocyclic 5 or 6 atom ring comprising at least nitrogen as hetero atom, which ring is optionally substituted and/or may form part of a larger condensed ring structure that is optionally substituted, and wherein R₂ and R₃ each have the aforesaid meaning of R₁ or may represent an optionally substituted aryl group. A process according to claim 1, characterized in that the heterocyclic rings in the definitions of R₁, R₂ and R₃ comprise pyridyl, pyrazinyl, quinolyl, isoquinolyl, pyrimidinyl, pyridazinyl, indolizinyl, cinnolinyl, acridinyl, phenazinyl, phenanthridinyl, phenanthrolinyl, phthalazinyl, naphthyrindinyl, quinoxalinyl and quinazolinyl. A process according to claim 1 or 2, characterized in that the heterocyclic and/or aryl groups are substituted with one or more electron-repelling groups. A process according to claim 3, characterized in that the substituents comprise alkoxy groups with not more than 5 carbon atoms, alkyl groups with not more than 5 carbon atoms, dimethylamino and diethylamino groups. A process according to claim 1 or 2, characterized in that the heterocyclic and aryl groups are substituted with one or more electron-attracting groups. A process according to claim 5, characterized in that the substituents comprise chlorine, fluorine, trifluoromethyl, trichloromethyl, monochloromethyl and m-methoxy groups. A process according to any one of claims 1-6, characterized in that a phosphine is used according to formula I wherein R₁ represents pyridyl, R₂ pyridyl or phenyl and R₃ phenyl. A process according to any one of claims 1-7, characterized in that as protonic acid p-toluenesulphonic acid and benzenephosphonic acid are used. A process according to any one of claims 1-8, characterized in that palladium acetate is used as a component of the catalyst system. A process according to any one of claims 1-9, characterized in that a quantity of palladium compound is used from 10⁻⁷ to 10⁻¹ gram atom palladium per mol acetylenically unsaturated compound. A process according to any one of claims 1-10, characterized in that the molar ratio of the organic phosphine to palladium ranges from 2 to 500 mol organic phosphine per gram atom palladium. A process according to any one of claims 1-11, characterized in that the number of protonic acid equivalents per organic phosphine equivalent ranges from 0.1 to 50. A process according to any one of claims 1-12, characterized in that an extra solvent is used. A process according to claim 13, characterized in that N-methylpyrrolidone is used as main solvent or co-solvent. A process according to any one of claims 1-14, characterized in that the molar quantity of the alcohol, phenol, water or carboxylic acid per mol acetylenically unsaturated compound ranges from 0.01 to 100. A process according to any one of claims 1-15, characterized in that acetylene, propyne or phenylacetylene is converted. A process according to any one of claims 1-16, characterized in that as hydroxyl group containing reactant a lower sugar is used. Catalytic system obtainable from the combination of: (a) a palladium compound (b) a protonic acid with a pKa of not less than 2 (c) an organic phosphine according to formula I of claim 1, wherein R₁ represents a heterocyclic 5 or 6 atom ring, comprising at least nitrogen as hetero atom, which ring is optionally subsituted and/or may form part of a larger condensed ring structure that is optionally substituted, and wherein R₂ and R₃ each have the afore-mentioned meaning of R₁ or may represent an optionally substituted aryl group. Catalytic system according to claim 18, wherein the heterocyclic rings in the definitions of R₁, R₂ and R₃ comprise pyridyl, pyrazinyl, quinolyl, isoquinolyl, pyrimidinyl, pyridazinyl, indolizinyl, cinnolinyl, acridinyl, phenazinyl, phenanthridinyl, phenanthrolinyl, phtalazinyl, naphthyrindinyl, quinoxalinyl and quinazolinyl. Catalytic system according to claim 19, wherein R₁ represents pyridyl, R₂ pyridyl or phenyl, and R₃ phenyl. Catalytic system according to any one of claims 18-20, further comprising N-methyl pyrrolidone. Claims for the following Contracting State : NL A process for the preparation of alpha,beta-olefinically unsaturated compounds by means of carbonylation of acetylenically unsaturated compounds with carbon monoxide in the presence of a hydroxylated co-reactant and of a liquid phase, and in the presence of a catalytic system comprising a palladium compound and an organic phosphine, characterized in that the catalytic system is obtainable from the combination of: (a) a palladium compound (b) a protonic acid (c) an organic phosphine according to the formula wherein R₁ represents a heterocyclic 5 or 6 atom ring comprising at least nitrogen as hetero atom, which ring is optionally substituted and/or may form part of a larger condensed ring structure that is optionally substituted, and wherein R₂ and R₃ each have the aforesaid meaning of R₁ or may represent an optionally substituted aryl group. A process according to claim 1, characterized in that the heterocyclic rings in the definitions of R₁, R₂ and R₃ comprise pyridyl, pyrazinyl, quinolyl, isoquinolyl, pyrimidinyl, pyridazinyl, indolizinyl, cinnolinyl, acridinyl, phenazinyl, phenanthridinyl, phenanthrolinyl, phthalazinyl, naphthyrindinyl, quinoxalinyl and quinazolinyl. A process according to claim 1 or 2, characterized in that the heterocyclic and/or aryl groups are substituted with one or more electron-repelling groups. A process according to claim 3, characterized in that the substituents comprise alkoxy groups with not more than 5 carbon atoms, alkyl groups with not more than 5 carbon atoms, dimethylamino and diethylamino groups. A process according to claim 1 or 2, characterized in that the heterocyclic and aryl groups are substituted with one or more electron-attracting groups. A process according to claim 5, characterized in that the substituents comprise chlorine, fluorine, trifluoromethyl, trichloromethyl, monochloromethyl and m-methoxy groups. A process according to any one of claims 1-6, characterized in that a phosphine is used according to formula I wherein R₁ represents pyridyl, R₂ pyridyl or phenyl and R₃ phenyl. A process according to any one of claims 1-7, characterized in that as protonic acid p-toluenesulphonic acid and benzenephosphonic acid are used. A process according to any one of claims 1-8, characterized in that palladium acetate is used as a component of the catalyst system. A process according to any one of claims 1-9, characterized in that a quantity of palladium compound is used from 10⁻⁷ to 10⁻¹ gram atom palladium per mol acetylenically unsaturated compound. A process according to any one of claims 1-10, characterized in that the molar ratio of the organic phosphine to palladium ranges from 2 to 500 mol organic phosphine per gram atom palladium. A process according to any one of claims 1-11, characterized in that the number of protonic acid equivalents per organic phosphine equivalent ranges from 0.1 to 50. A process according to any one of claims 1-12, characterized in that an extra solvent is used. A process according to claim 13, characterized in that N-methylpyrrolidone is used as main solvent or co-solvent. A process according to any one of claims 1-14, characterized in that the molar quantity of the alcohol, phenol, water or carboxylic acid per mol acetylenically unsaturated compound ranges from 0.01 to 100. A process according to any one of claims 1-15, characterized in that acetylene, propyne or phenylacetylene is converted. A process according to any one of claims 1-16, characterized in that as hydroxyl group containing reactant a lower sugar is used. Catalytic system obtainable from the combination of: (a) a palladium compound (b) a protonic acid (c) an organic phosphine according to formula I of claim 1, wherein R₁ represents a heterocyclic 5 or 6 atom ring, comprising at least nitrogen as hetero atom, which ring is optionally subsituted and/or may form part of a larger condensed ring structure that is optionally substituted, and wherein R₂ and R₃ each have the afore-mentioned meaning of R₁ or may represent an optionally substituted aryl group. Catalytic system according to claim 18, wherein the heterocyclic rings in the definitions of R₁, R₂ and R₃ comprise pyridyl, pyrazinyl, quinolyl, isoquinolyl, pyrimidinyl, pyridazinyl, indolizinyl, cinnolinyl, acridinyl, phenazinyl, phenanthridinyl, phenanthrolinyl, phtalazinyl, naphthyrindinyl, quinoxalinyl and quinazolinyl. Catalytic system according to claim 19, wherein R₁ represents pyridyl, R₂ pyridyl or phenyl, and R₃ phenyl. Catalytic system according to any one of claims 18-20, further comprising N-methyl pyrrolidone.

Inventors: DRENT, EIT
Applicants: SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1987
Main classification: C07C67
IPC codes: C07B61, C07C51, C07C67, C07F9, C07C57, B01J31, C07B41, C07C69