PROCESS FOR THE CARBONYLATION OF ETHYLENE AND CATALYST SYSTEM FOR USE THEREIN

Abstract: A catalyst system capable of catalysing the carbonylation of ethylene and a process which uses such a system wherein the catalyst system is obtainable by combining a metal of Group VIII, e.g. palladium, or a compound thereof and a bidentate phosphine, e.g. bis (di-t-butyl phosphino) - o - xylene.

Description: Process for the carbonylation of ethylene and catalyst system for use therein The invention relates to the carbonylation of ethylene using carbon monoxide in the presence of a catalyst system and to such a catalyst system The carbonylation of ethylene using carbon monoxide in the presence of an alcohol or water and a catalyst system comprising a Group VIII metal, e g palladium, and a phosphine ligand. e g an alkyl phosphine, cycloalkyl phosphine, aryl phosphine. pyπdyl phosphine or bidentate phosphine, has been described in numerous European patents and patent applications, e g EP-A-0055875. EP-A-04489472, EP-A-0106379, EP-A-0235864, EP-A-0274795, EP-A-0499329. EP-A-0386833, EP-A-0441 47, EP-A-0489472, EP-A-0282142, EP-A-0227160. EP-A-0495547 and EP-A-0495548 In particular, EP-A-0227160, EP-A-0495547 and EP-A-0495548 disclose that bidentate phosphine ligands provide catalyst systems which enable higher reaction rates to be achieved The main problem with the previously disclosed catalyst systems is that, although relatively high reaction rates can be achieved, the palladium catalyst dies off quickly which necessitates the frequent replenishment of the catalyst and hence results in a process which is industrially unattractive It has now been found that a particular group of bidentate phosphine compounds can provide remarkably stable catalysts which require little or no replenishment; that use of such bidentate catalysts leads to reaction rates which are significantly higher than those previously disclosed, that little or no impurities are produced at high conversions Accordingly, the present invention provides a process for the carbonylation of ethylene which process comprises reacting ethylene with carbon monoxide in the presence of a source of hydroxyl groups and of a catalyst system, wherein the catalyst system is obtainable by combining (a) a metal of Group VIII or a compound thereof; and (b) a bidentate phosphine of general formula (I) R 1 I I R 6 R 7 (I) wherein R° is a tertiary carbon atom each of R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R β , R 9 , R'°, R n and R 12 is independently a pendant optionally substituted organic group which carries a carbon atom through which the group is linked to the respective R°; each of L 1 and L 2 is independently a linking group selected from an optionally substituted lower alkylene chain connecting the respective phosphorus atom to the group X; and X is a bridging group comprising an optionally substituted aryl moiety to which the phosphorus atoms are linked on available adjacent carbon atoms. In a second aspect, the present provides a catalyst system capable of catalysing the carbonylation of ethylene, which catalyst system is formed from (a) a metal of Group VIII or a compound thereof; and (b) a bidentate phosphine of general formula (I) R' R' 2 R 7 (I) wherein R° is a tertiary carbon atom each of R\ R 2 , R 3 , R R 5 , R 6 , R 7 , R β , R 9 , R 10 , R" and R 12 is independently a pendant optionally substituted organic group which carries a carbon atom through which the group is linked to the respective R°, each of L 1 and L 2 is independently a linking group selected from an optionally substituted lower alkylene chain connecting the respective phosphorus atom to the group X, and X is a bridging group comprising an optionally substituted aryl moiety to which the phosphorus atoms are linked on available adjacent carbon atoms. The pendant optionally substituted organic groups, R', R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R $ , R 9 , R 10 , R 11 and R 12 , may be independently selected from a wide range of components Preferably, the pendant groups are optionally substituted lower alkyl, e g. C, .„, and which may be branched or linear Particularly preferred is when the organic groups, R\ R 2 , R 3 , R 4 , R 5 , R β , R 7 , R β , R 9 , R 10 , R" and R' 2 , when associated with their respective R° carbon atom form composite groups which are at least as sterically hindering as t-butyl Steric hindrance in this context is as discussed at page 14 et seq of "Homogeneous Transition Metal Catalysis - A Gentle Art", by C Masters, published by Chapman and Hall, 1981 The linking groups, U and L 2 , are independently selected from an optionally substituted, particularly lower alkyl, e.g. C, to C 4 , substituted, lower alkylene. e g C, to C< chain Especially preferred is when both L and L 2 are methylene The bridging group X is an aryl moiety, e g a phenyl group, which may be optionally substituted, provided that the two phosphorus atoms are linked to adjacent carbon atoms, e g at the 1 and 2 positions on the phenyl group Optional substitution of the aryl moiety may be by other organic groups e g alkyl particularly C, β aryl alkoxy carbalkoxy halo nitro tπhalomethyl and cyano Furthermore the aryl moiety may be a fused polycyclic group, e g naphthalene biphenylene or mdene Examples of suitable bidentate ligands are bis (di-t-butyl phosphino) - o - xylene (also known as 1 2 bis (di-t-butylphosphmomethyl) benzene), bis (di-t-neopentyl phosphino) - o - xylene and bis 1 2 (di-t-butyl phosphino) naphthalene Additionally, the bidentate phosphine may be bonded to a suitable polymeric substrate via at least one of the bridging group X the linking group L 1 or the linking group L' e g bis (di-t-butyl phosphino) - o - xylene may be bonded via the xylene group to polystyrene to give an immobile heterogeneous catalyst The amount of bidentate ligand used can vary within wide limits Preferably, the bidentate ligand is present in an amount such that the ratio of the number of moles of the bidentate ligand present to the number of moles of the Group VIII metal present is from 1 to 50, e g 1 to 10 and particularly from 1 to 5 mol per mol The carbon monoxide may be used in the presence of other gases which are inert in the reaction Examples of such gases include hydrogen, nitrogen, carbon dioxide and the noble gases such as argon The process of the present invention is preferably carried out at a temperature from 20 to 250 β C, in particular from 40 to 150 β C and especially from 70 to 120 β C The process may be conducted under a total pressure of from 1 x 10* to 100 x 10 s N m : and in particular from 5 x 10 s to 50 x 10 5 N m 2 Suitable Group VIII metals include cobalt, nickel, palladium, rhodium and platinum 5 Particularly preferred is palladium Suitable compounds of such Group VIII metals include salts of such metals with, or compounds comprising weakly co-ordinated anions derived from, nitric acid, sulphuric acid, lower alkanoic (up to C,- ) acids such as acetic acid and propionic acid, sulphonic acids such as methane sulphonic acid, chlorosulphonic acid, fluorosulphonic acid, trifluoro methane sulphonic acid, benzene sulphonic acid, naphthalene sulphonic acid, 0 toluene sulphonic acid, e g p-toluene sulphonic acid, t-butyl sulphonic acid and 2-hydroxypropane sulphonic acid, sulphonated ion exchange resins perhalic acid such as perchloric acid, perfluororated carboxylic acid such as trichloroacetic acid and tπfiuoroacetic acid orthophosphonc acid phosphonic acid such as benzene phosphonic acid and acids derived from interactions between Lewis acids and Broensted acids Other sources which 5 may provide suitable anions include the tetraphenyl borate derivatives Additionally, zero valent palladium compounds with labile ligands. e g tri (dibenzy deneacetone) dipalladium, may be used The catalyst system of the present invention may be used homogeneously or heretogeneously Preferably the catalyst system is used homogeneously The catalyst system of the present invention is preferably constituted in the liquid phase which may be formed by one or more of the reactants or by the use of a suitable solvent Suitable solvents that may be used in conjunction with the catalyst system include one or more aprotic solvents such as ethers, e g diethyl ether, dimethyl ether dimethyl ether of diethylene glycol anisole and diphenyl ether, aromatic compounds, including halo variants of such compounds, e g benzene toluene, ethyl benzene o-xylene, m-xylene, p-xylene, chlorobenzene o-dichlorobenzene m-dichlorobenzene and p-dichlorobenzene alkanes, including halo variants of such compounds, e g hexane heptane 2, 2, 3- tπmethylpentane, methylene chloride and carbon tetrachloπde, nitπles, e g benzonitnle and acetonitπle. esters, e g methyl benzoate, methyl acetate and dimethyl phthalate. sulphones. e g diethyl sulphone and tetrahydrothiophene 1 , 1 - dioxide; amides, including halo variants of such compounds, e g dimethyl formamide and N-methyl pyrrolidone The catalyst system of the present invention is particularly suited to the carbonylation of ethylene Surprisingly, propene has been found to be difficult to carbonylate to the extent that the present catalyst system may be viewed as not being able to carbonylate propene The end product of the reaction is determined at least in part by the source of hydroxyl groups that is used The use of water gives rise to the corresponding carboxylic acid whereas the use of an alkanol leads to the corresponding ester Suitable alkanols include C, -o alkanols, optionally substituted with one or more substituents such as halogen atoms, cyano. carbonyl, aikoxy or aryl groups Suitable alkanols include methanol. ethanol. propanol, 2-propanol, 2-butanol, t-butyl alcohol and chlorocapryl alcohol Particularly useful are methanol and ethanol The molar ratio of the amount of ethylene used in the reaction to the amount of 0 hydroxyl providing compound is not critical and may vary between wide limits, e g from 0 001 1 to 100 1 mol/mol The product of the reaction may be separated from the other components by any suitable means However, it is an advantage of the present catalyst system that significantly fewer by-products are formed thereby reducing the need for further purification after the initial 5 separation of the product as may be evidenced by the generally significantly higher selectivity A further advantage is that the other components which contain the catalyst system which may be recycled and/or reused in further reactions with minimal supplementation of fresh catalyst The following Examples further illustrated the present invention Example 1 In this example methyl propionate was prepared from carbon monoxide and ethylene using methanol as the hydroxyl group source A mechanically stirred autoclave of 2 litre capacity was evacuated of air and then charged with a catalyst system consisting of methanol 300 cm 3 palladium acetate 0 1 mmol bidentate * 0 3 mmol methane sulphonic acid 0 24 mmol * - bis (di-t-butylphosphino) - o - xylene Carbon monoxide and ethylene on an equimoiar basis was introduced until a pressure of 30 x 10 s N m : was reached The temperature of the reactor was raised to and maintained at 100°C As the reaction proceeded sufficient additional methanol was introduced to compensate for that which had been consumed and additional carbon monoxide and ethylene was added (on an equimoiar basis) to maintain the pressure No palladium precipitation was observed Example 2 - Comparative Example 1 was repeated except that the propane analogue of the o-xylene bidentate was used Precipitation of palladium, with consequent deactivation of the catalyst, was observed within two hours 5 The reaction rate (expressed as mole ethylene per mole of palladium per hour), selectivity to methyl propionate (% by gas chromatography) and turn over number based on phosphine (expressed as mole methyl propionate per mole of phosphine) for each of the catalyst systems described in Examples 1 and 2 is shown in Table 1 below TABLE 1 PHOSPHINE REACTION SELECTIVITY TURN OVER LIGAND RATE NUMBER bis (di-t-butyl 40000 99 95 >50000 phosphino) - o - xylene bis (di-t-butyl 15000 98 00 1700 phosphino) - propane It can thus be seen that the catalyst system of the present invention is more stable, more reactive and more selective than the conventional bidentate system Example 3 The catalyst system from Example 1 was extracted at the end of the procedure and reused with fresh methanol and methane sulphonic acid The activity of the reused catalyst was the same as that of the original The catalyst system of Example 2 was unable to be reused due to the precipitation of the palladium Example 4 Example 1 was repeated using the 4-nιtro substituted analogue of the bidentate ligand which was prepared via the phosphonium salt produced from the reaction of the appropriate secondary phosphine with the corresponding aromatic dihalide Example 5 Example 4 was repeated using the 4-methoxy substituted analogue The results of Example 4 and 5 were as follows PHOSPHINE REACTION SELECTIVITY TURN OVER LIGAND RATE NUMBER 4-nιtro 36000 99 9 >25000 4-methoxy 37000 99.9 >25000 Example 6 Example 1 was repeated except that an alternative source of palladium was used The catalyst was prepared by mixing the bidentate phosphine, tπs(dιbenzylιdeneacetone) dipalladium known as dba and sulphonic acid in a molar ratio of 2 1 3 The phosphine and dba were mixed together prior to the addition of the acid The reaction was conducted using an equimoiar mixture of methanol and methyl propionate at a total pressure of 15 barg (using a 1 1 mixture of carbon monoxide and ethylene) The reaction temperature was 80°C Example 7 Example 6 was repeated except that in the ligand one of the t-butyl groups on each phosphorous atom was replaced by cyclohexyl groups Example 8 Example 6 was repeated except that in the ligand the t-butyl groups were replaced by cyclohexyl groups Example 9 Example 6 was repeated except that in the ligand the t-butyl groups were replaced by isopropyl groups Example 10 Example 6 was repeated except that in the ligand the t-butyl groups were replaced by phenyl groups Example 11 Example 6 was repeated except that the linking methylene groups were both replaced by oxygen atoms The phosphinite was synthesised from an aromatic diol and chloro dι(t-butyl) phosphine Example 12 Example 11 was repeated except that the 4 t-butyl substituted analogue of the ligand was used The results of Examples 6 to 12 were as follows PHOSPHINE REACTION SELECTIVITY TURN OVER LIGAND RATE NUMBER Example 6 12000 99.95 >250000 Example 7 500 30 >1500 Example 8 200 25 >600 Example 9 200 20 500 Example 10 400 20 >1200 Example 11 100 30 <300 Example 12 100 30 <300

Claims: Claims 1 A process for the carbonylation of ethylene which process comprises reacting ethylene with carbon monoxide in the presence of a source of hydroxyl groups and of a catalyst system, wherein the catalyst system is obtainable by combining (a) a metal of Group VIII or a compound thereof: and (b) a bidentate phosphine of general formula (I) R 1 R 12 R β R 7 (I) wherein R° is a tertiary carbon atom each of R\ R 2 , R 3 , R\ R 5 , R β , R 7 , R β , R 9 , R 10 , R" and R 12 is independently a pendant optionally substituted organic group which carries a carbon atom through which the group is linked to the respective R°; each of L' and L 2 is independently a linking group selected from an optionally 5 substituted lower alkylene chain connecting the respective phosphorus atom to the group X, and X is a bridging group comprising an optionally substituted aryl moiety to which the phosphorus atoms are linked on available adjacent carbon atoms 2. A catalyst system capable of catalysing the carbonylation of an ethylene, which 0 catalyst system is formed from (a) a metal of Group VIII or a compound thereof, and (b) a bidentate phosphine of general formula (I) R 1 R 12 I I (I) wherein R° is a tertiary carbon atom each of R 1 R 2 , R 3 , R 4 , R 5 , R«, R 7 , R β , R 9 , R 10 , R 11 and R 12 is independently a pendant optionally substituted organic group which carries a carbon atom through which the group is linked to the respective R°, each of L 1 and L 2 is independently a linking group selected from an optionally substituted lower alkylene chain connecting the respective phosphorus atom to the group X, and X is a bridging group comprising an optionally substituted aryl moiety to which the phosphorus atoms are linked on available adjacent carbon atoms 3 A process or catalyst system as claimed in claim 1 or claim 2 wherein the pendant optionally substituted organic groups, R 1 , R 2 , R 3 , R 4 , R s , R β , R 7 , R β , R 9 , R'°, R" and R 12 , are independently selected from optionally substituted lower alkyl 4 A process or catalyst system as claimed in any one of the preceding claims wherein the organic groups, R 1 , R 2 , R 3 , R 4 , R 5 , R β , R 7 , R β , R 9 , R 0 , R 1 and R' 2 , are associated with their respective R° carbon atom so as to form composite groups which are at least as sterically hindering as t-butyl 5 A process or catalyst system as claimed in any one of the preceding claims wherein both L 1 and L 2 are methylene

Inventors: EASTHAM GRAHAM RONALD, TOOZE ROBERT PAUL, WANG XIAO LAN, WHISTON KEITH, EASTHAM, GRAHAM, RONALD, TOOZE, ROBERT, PAUL, WANG, XIAO, LAN, WHISTON, KEITH
Applicants: EASTHAM GRAHAM RONALD, ICI PLC, TOOZE ROBERT PAUL, WANG XIAO LAN, WHISTON KEITH, EASTHAM, GRAHAM, RONALD, IMPERIAL CHEMICAL INDUSTRIES PLC, TOOZE, ROBERT, PAUL, WANG, XIAO, LAN, WHISTON, KEITH
Application year: 1995
Main classification: C07C67
IPC codes: B01J31, C07B61, C07C67, C07C69, C07F9