PROCESS FOR THE PREPARATION OF ETHYLIDENE DIACETATE AND/OR ACETIC ACID ANHYDRIDE

Abstract: A process for the preparation of ethylidene diacetate and/or acetic acid anhydride by reacting methyl acetate and/or dimethyl ether with carbon monoxide or a mixture of carbon monoxide and hydrogen at elevated temperature and pressure characterized in that the reaction is carried out in the presence of a homogeneous catalyst system comprising a Group VIII noble metal compound, a bromide or iodide source, and a Group Va compound represented by the general formula in which X is a Group Va element having a valency above 3 selected from N, P, As or Sb; Y is a Group VIa element selected from O, S, or Se and either a, b and c are 0 or 1 and R¹, R² and R³ are similar or dissimilar optionally substituted hydrocarbon groups; or a and b are 0 and c is 0 or 1 and R¹ and R² form together with X a heterocyclic group; or a, b and c are 0 and R¹, R² and R³ form together with X a heterocyclic aromatic group.

Description: PROCESS FOR THE PREPARATION OF ETHYLIDENE DIACETATE AND/OR ACETIC ACID ANHYDRIDE The present invention relates to a process for the preparation of ethylidene diacetate and/or acetic acid anhydride by carbonylation of methyl acetate and/or dimethyl ether in the presence of a homogeneous Group VIII noble metal catalyst. Ethylidene diacetate and acetic acid anhydride are valuable chemicals which can be used as such for example as solvent or as intermediates for the preparation of chemicals. Ethylidene diacetate can be converted into vinyl acetate, ethyl acetate or acetic acid anhydride whereas acetic acid anhydride in its turn can be converted into ethylidene diacetate. The most important application of acetic acid anhydride is the use in the manufacture of cellulose acetate. In the search for suitable processes utilizing synthesis gas for the production of highly valuable chemicals it has previously been proposed to prepare ethylidene diacetate and acetic acid anhydride by carbonylation reactions catalyzed by Group VIII noble metal based catalysts. UK Patent Specification 1,538,782 discloses a process for the preparation of ethylidene diacetate by carbonylation of methyl acetate or dimethyl ether in the presence of hydrogen using a catalytic system comprising a Group VIII noble metal compound, a bromide and/or iodide source, an inorganic promotor such as for example a Group IVb metal (compound) or a Group VIb metal (compound), and/or an organic promotor such as for example a tertairy amine or phosphine. The presence of a promotor is considered essential as is demonstrated in the examples V and VIII. Processes for the preparation of acetic acid anhydride by carbonylation of methyl acetate using a Group VIII noble metal catalyst are described in UK Patent Specifications 1,468,940, 1,523,346 and 1,538,783. In UK Patent Specification 1,538,783 a catalytic system for this carbonylation reaction is described consisting of a Group VIII noble metal, a bromide or iodide, and a multiple promotor comprising at least one metal of Groups IVb, Vb and VIb, or a non-noble metal of Group VIII, and an organic compound of trivalent nitrogen or phosphorus. Recently it has been proposed to enhance the activity of Group VIII noble metal catalysts by using specific combinations of metal compounds as promotor. According to German Offenlegungsschrift 2,941,232 the activity of the Group VIII noble metal catalyst in the preparation of ethylidene diacetate from methyl acetate can be increased by carrying out the reaction in the presence of (an) iodine (compound), a heterocyclic aromatic compound having a quaternary nitrogen atom, an aliphatic carboxylic acid and a rhenium or manganese compound. In European Patent Application 0026,280 a similar multiple promotor system is proposed for the preparation of acetic acid anhydride by carbonylation of methyl acetate using, however, a zirconium compound instead of a rhenium or manganese compound. The-Dutch laid open Patent Applications 8,006,806 and 8,006,807 describe Group VIII noble metal catalyst systems having enhanced activity for the carbonylation of methyl acetate to acetic acid anhydride containing an iodide, a trivalent organo nitrogen, phosphorus or arsenic compound in combination with metallic zirconium or hafnium. It has now surprisingly been found that by carrying out the carbonylation of methyl acetate and/or dimethyl ether in the presence of certain compounds of elements of Group Va which will be specified below either in the absence or presence of other (known) promotors, the activity of the Group VIII noble metal catalyst can be considerably increased. The Group Va compounds are oxides, sulfides or selenides of organic Group Va compounds, in which the Group Va element has a valency above 3. The present invention therefore relates to a process for the preparation of ethylidene diacetate and/or acetic acid anhydride by reacting methyl acetate and/or dimethyl ether with carbon monoxide or a mixture of carbon monoxide and hydrogen at elevated temperature and pressure in the presence of a homo geneous catalyst system comprising a Group VIII noble metal compound, a bromide or iodide source, and a Group Va compound represented by the general formula EMI3.1 in which X is a Group Va element having a valency above 3 selected from N, P, As or Sb; Y is a Group VIa element selected from 0, S or Se and either a, b and c are 0 or 1 and R1, R2 and R3 are similar or dissimilar optionally substituted hydrocarbon groups; or a and b are 0 and c is O or 1 and R1 and R2 form together with X a heterocyclic group or a, b and c are 0 and R1, R2 and R3 form together with X a heterocyclic aromatic group. Normally the process of the invention will be carried out using methyl acetate as the starting material. It is also possible to use dimethyl ether or a mixture thereof with methyl acetate as starting material. It would appear that dimethyl ether will be converted under reaction conditions into methyl acetate by introduction of a CO moiety. If desired the process can be carried out in two or more stages when dimethyl ether is used as starting material. Firstly dimethyl ether will be (partially) converted into methyl acetate, which in its turn, in the same or in a different vessel, will be converted into the final products ethylidene diacetate and/or acetic acid anhydrideq It should be noted that the overall reactions when methyl acetate and dimethyl ether are converted into ethylidene diacetate and acetic acid anhydride can be expressed by the following chemical equations EMI3.2 in which AA - acetic acid, AAA - acetic acid anhydride, DME - dimethyl ether, EDA - ethylidene diacetate and MA - methyl acetate. Acetic acid appears to be the primary by-product but other compounds, for example acetaldehyde may also be produced. While the mechanism of the reactions occuring is not known it is not possible to indicate all factors which govern the composition of the reaction mixture. However, the amount of hydrogen present seems to influence this composition to a substantial measure in that higher amounts of hydrogen do increase the amount of ethylidene diacetate formed. It should be noted, however, that this does not necessarily mean that the ethylidene diacetate is formed via hydrogenation of the acetic acid anhydride formed by carbonylation. The Group VIII noble metal compounds which can be used in the process of the invention include especially rhodium and palladium compounds although other Group VIII noble metal compounds can also be used. Examples of rhodium compounds which may be used include rhodium oxide, rhodium (III) hydroxide, rhodium (III) chloride, rhodium (III) chloride trihydrate, rhodium (III) bromide, rhodium (III) iodide and the corresponding pyridine and phosphine complexes such as tris(pyridine) rhodium (III) chloride or dichloro bis(triphenylphosphine) rhodium, rhodium (III) formate, rhodium (III) acetate, rhodium (III) butyrate, rhodium (III) naphtenate, dirhodium octacarbonyl, tetrarhodium dodecacarbonyl, hexarhodium hexadecacarbonyl, rhodium dicarbonyl acetylacetonate and other organo rhodium complexes. Preference is given to the use of rhodium (III) chloride trihyrate. Examples of palladium compounds which may be used include palladium chloride, palladium chloride dihydrate, palladium bromide, palladium iodide, palladium oxide and organic palladium salts or complexes such as palladium formate, palladium acetate, palladium butyrate and palladium acetylacetonate. Preferred palladium compounds are palladium chloride, palladium chloride dihydrate and palladium acetate. In European Patent Application 0035860 a process for the preparation of ethylidene diacetate and/or acetaldehyde by carbonylation of methyl acetate or dimethyl ether has been described. The reaction is carried out in the presence of a catalyst consisting of palladium metal supported on a porous inorganic material, a halide and optionally a promotor. It is stated on page 4 that a catalyst consisting of metallic palladium, a halide and a promotor did not have catalytic activity, or in other words that the presence of a porous inorganic support is essential. As possible promotors a huge amount of nitrogen compounds, including pyridine oxide, are mentioned, but compounds of trivalent nitrogen are clearly preferred. It cannot be deduced from European Patent Application 0035860 that compounds having the above general formula I can advantageously be used as promotor in a process in which instead of palladium metal on an inorganic support a soluble Group VIII noble metal compounds are used as catalysts. The amount of Group VIII noble metal to be used in the process of the invention is not critical and any amount which: exerts catalytic activity can be used. Amounts as low as 0.001 Zw calculated on methyl acetate and/or dimethyl ether to be converted can be used, preference being given to amounts in the range from 0.005-10 Zw, most preferably between 0.01-5 Zw. Any iodide or bromide source or mixtures thereof may be used in the process according to the present invention. Suitable iodide and/or bromide sources are elemental iodine, elemental bromine, hydrogen iodide, hydrogen bromide and metal iodides or bromides. Examples of metal iodides or bromides comprise iodides or bromides of alkali metals, Group II metals and transition metals such as lithium iodide, sodium iodide, magnesium iodide, chromium (III) iodide, cobalt (11) iodide, cobalt (II) bromide, nickel (11) iodide, nickel (II) bromide, copper (II) iodide, copper (II) bromide, zinc iodide and zinc bromide. Combinations of metal salts which can give rise to in situ formation of iodides or bromides of Group II metals and transition metals can also be used, for example a mixture of zinc acetate and an alkali(ne earth) metal iodide or bromide. Further bromide or iodide sources which can be used conveniently comprise organic compounds having the general formula R(CO)n Hal wherein n - 0 or 1, Hal represents Br or J and R represents an alkyl group having from 1 to 12 carbon atoms or an aryl, aralkyl or alkaryl group having up to 12 carbon atoms. The use of iodide sources is preferred, in particular alkyl iodides or alkanoyl iodides. Most preference is given to the use of methyl iodide. The quantity of the iodide or bromide source added to the reaction mixture is not crucial. Suitably the number of moles of iodide and/or bromide source per gram atom of Group VIII noble metal is in the range of from 0.1:1 to 1000:1 preferably 1:1 to 500:1 and especially 10:1 to 300:1. As stated hereinbefore the process according to the present invention is carried out in the presence of a Group Va compound having the formula (I). The optionally substituted hydrocarbon groups represented by R1, R2 and R3 may be alkyl, cycloalkyl, aryl or alkaryl groups containing up to 30 carbon atoms. When R1 + R2 or R1 + R2 + R3 with X form a heterocyclic group, the hydrocarbon moiety of the heterocyclic group may contain up to 20 carbon atoms. Preferred Group Va compounds are represented by the general formula I in which a, b and c are 0, X is P, Y is O or S and R1, R2 and R3 are alkyl groups containing 1-4 carbon atoms or cycloalkyl, aryl or alkaryl groups containing 5-12 carbon atoms. Group Va compounds of this type having the general formula I in which Y is 0 are generally preferred. Other preferred Va compounds are represented by the genral formula I in which a, b and c are 0, X is N, Y is 0 and R1, R2 and R3 are alkyl groups containing 1-12 carbon atoms or cylcoalkyl, aryl or alkaryl groups containing 5-12 carbon atoms or K1 and R2 form together with X a heterocyclic group containing 4-12 carbon atoms; or R1, R2 and R3 form together with X a heterocyclic aromatic group containing 5-12, preferably 5-7 carbon atoms. The optional substituents of the hydrocarbon groups should be substantially inert in the reaction medium. Suitable substituents are for example chlorine, alkoxy groups, carboxylic acid (ester) groups or sulphone or sulphoxide groups. Examples of suitable Group Va compounds having formula I are oxides of tertiary amines such as trimethylamine oxide, triethylamine oxide, N,N-dimethyl phenylamine oxide, N,N-dimethyl p-methylphenylamine oxide, Methyl piperidine oxide, dimethyl octylamine oxide and dimethyl dodecylamine oxide; oxides, sulfides or selenides of tertiary phosphines, arsines or stibines such as trimethylphosphine oxide, triethylphosphine oxide, tri-n-butylphosphine oxide, triphenylphosphine oxide, tri-p-tolylphosphine oxide, tricyclohexylphosphine oxide, diphenyl ethylphosphine oxide, tris( 1-naphthyl)phosphine oxide, 1¯phenylphos- pholane oxide, 1-phenylphosphorinane oxide, trimethylphosphine sulfide, tri-4-chlorophenylphosphine sulfide, triphenylphosphine sulfide, tricyclohexylphosphine sulfide, tri-n-butylphosphine sulfide, triphenylphosphine selenide, tris(1-naphtyl)phosphine selenide, triethyl arsine oxide, triphenyl arsine oxide, triphenyl stibine oxide and triphenyl arsine sulfide. Triphenylphosphine oxide and triphenylphosphine sulfide are preferred. Further examples of suitable Group Va compounds having formula I comprise alkyl and aryl esters of phosphoric, phosphonic and phosphinic acids and their arsenic or antimony analogues such as trimethyl phosphate, triethyl phosphate, tri-n-butyl phosphate, triphenyl phosphate, dimethyl methyl phosphonate, 1, 5-dimethylbicyclo(3. 2. 1 )octyl octyl phosphonate, diethyl methyl phosphonate and methyl diphenyl phosphonate. Preference is given to the use of phosphonates. Still further examples of suitable Group Va compounds having formula I are oxides of aromatic heterocyclic N-compounds such as pyridine-N-oxide, quinoline-Noxide, isoquinoline-N-oxide, 1, 10-phenantroline-N-monoxide, pyrazine-N-monoxide and the alkyl substituted derivatives thereof for example alpha-picoline-N-oxide. Pyridine-N-oxide is preferred. It should be noted that the Group Va compounds having formula I may contain two or more moieties represented by the general formula I. Examples of such compounds are N,N,N',N' tetramethylethylene diamine-N,N'-dioxide, tetraphenyl trimethylene diphosphine dioxide, tetraphenyl trimethylene diphosphine dioxide, 2,2'bipyridyl-N,N'-dioxide, 1,10 phenanthroline-N,N'dioxide and pyrazine-N-N'-dioxide. It will be appreciated that in the reaction mixture salts or complexes may be formed by the reaction of the oxide, sulfide or selenide of the tertiary N, P, As or Sb compounds with the iodine or bromine compound present or with hydrogen bromide or hydrogen iodide formed therefrom in situ. Examples of such salts and complexes are alkoxy pyridinium salts for example methoxy pyridinium iodide from pyridine oxide and methyl iodide and the complexes t(C6H5)3Po-H-oP(C6H5)3]+I3 or [(C2H5)3AsO-H-OAs(C2Hs)3]+I¯ Consequently the use of such salts or complexes when prepared separately is within the scope of the present invention. Furthermore, it will be appreciated that the oxides of the Group Va compounds having formula I which are oxides can be formed in situ. For example a phosphine oxide can be formed in situ from a phosphine by carrying out the reaction in the presence of molecular oxygen or hydrogen peroxide. The amount of the Group Va compound having formula I to be used in the process of the invention is not critical and may vary from 0.01:1 to 200:1 mol Group Va compound per gram atom Group VIII noble metal. As stated hereinbefore the Group Va compound having formula I can be used either in the absence or presence of other (known) promotors. It has been found that best results are often achieved by using the Group Va compound having formula I in combination with co-promotors such as, for example, metals of Group Ias IIa, IIIa, IVb or VIb in the form of finely divided metals or in the form of inorganic or organic compounds. The metal compounds include oxides, hydroxides, halides, oxyhalides, hydrides, carbonyls, alkoxides, nitrates, nitrites, phosphates, phosphites, carboxylates of alkyl, aralkyl or aryl monocarboxylic acids such as acetates, butyrates, stearates and benzoates, chelates, associate compounds and enol-salts. The use of Group IVb and Group VIb metal compounds, in particular Zr or Cr compounds such as ZrOC12.8H20 or Cr(C0)6 is preferred. The amount of these metal compound promotors may vary within wide limits but amounts of 0.1:1 to 10:1 of mol promotor per gram atom Group VIII noble metal are preferred. Other compounds which can suitably be used as co-promotor in combination with the Group Va compound comprise trivalent Group Va compounds. Examples of these compounds are trivalent nitrogen compounds, for example amines, such as alkyl, cycloalkyl, aryl and aralkyl amines containing up to 30 carbon atoms such as trimethylamine, triethylamine, tetramethylethylene diamine, and especially amines in which the nitrogen atom is part of a heterocyclic ring such as pyrrole, alkyl-substituted pyrroles, pyrrolidine, alkyl-substituted pyrrolidines, pyridine, alkyl-substituted pyridines, piperidines, alkyl-substituted piperidines, pyrimidine, alkyl-substituted alkylpyrimidines, pyrazine, benzatriazole, 1. 10-phenanthroline, alkyl-substituted 1.10 phenanthrolines, morpholine and alkyl-substituted morpholines. Preference is given to the use of pyridine and the alkyl-substituted pyridines such as the various picolines for example alpha-picoline. Further examples of trivalent Group Va compounds include trivalent phosphorus compounds such as alkyl, cycloalkyl, aryl or alkaryl phosphines having up to 30 carbon atoms, for example trimethylphosphine, triphenylphosphine and tributylphosphine, phosphorus compounds containing two or more phosphine groups, for example tetraphenyl dimethylene diphosphine and tetraphenyl trimethylene diphosphine and heterocyclic phosphorus compounds such as, for example, 1-phenylphospholane and 1-phenylphosphorinane. Also included are trivalent arsenic and antimony compounds such as triphenylarsine, triethylarsine, triphenylstibine or triethylstibine. Another group of suitable trivalent Group Va compounds are the phosphites such as triphenyl phosphite. The amount of trivalent Group Va compound to be used as co-promotor may vary from 0.1:1 to 100:1 mol per gram atom Group VIII metal. The process according to the present invention can be carried out using a wide range of temperatures. Temperatures up to 3000C can be suitably applied. Preference is given to temperatures in the range of from 500C to 2000C, most preferred temperatures are in the range between 140"C and 1900C. The process can be carried out using low pressures, for example pressures as low as 5 bar. Pressures in the range of from 20 to 100 bar are preferred. Higher pressures, for example pressures as high as 1000 bar can be applied, but they are generally not economical because of the investment and energy costs involved. According to the chemical equations presented hereinbefore 1 molecule of carbon monoxide is consumed per molecule methyl acetate in the conversion of methyl acetate into acetic acid anhydride and 2 molecules carbon monoxide and 1 molecule hydrogen in the conversion of methyl acetate into ethylidene diacetate. It has been found, however, that without any substantial disadvantage a wide range of molar ratios of hydrogen to carbon monoxide, for example from 0 to 10 can be applied. As stated earlier the formation of the amount of ethylidene diacetate is largely influenced by the amount of hydrogen present. Thus the process of the invention can flexibly be adapted to a wide variety of product compositions regarding acetic acid anhydride and ethylidene diacetate. For the preparation of acetic acid anhydride preference is given to a molar ratio of hydrogen to carbon monoxide from 0 to 0.1. The preferred range of molar ratios of hydrogen to carbon monoxide for the production of ethylidene diacetate as main product is from 10:1 to 1:10. The reaction time is not critical and will depend on the temperature and the pressure applied. Reaction times of from 0.25 to 20 hours are sufficient, preference being given to reaction times in the range of from 5 to 15 hours. Shorter or longer reaction times are not excluded, however. The process according to the present invention can be carried out in the liquid phase or in the gaseous phase. Preference is given to the liquid phase which enables a convenient introduction of carbon monoxide and hydrogen into the reaction vessel. If desired carbon monoxide and hydrogen can be introduced together into the reaction vessel. The process according to the present invention may be carried out in the presence of a solvent. Suitable solvents include carboxylic acids such as acetic acid and propanoic acid, carboxylic acid esters such as methyl acetate (being used as solvent as well as starting material) and cyclic esters such as butyrolacton. Ethers can also be used as solvent, for example dimethyl ether (used both as solvent and as starting material) diethyl ether, methyl-t-butyl ether, diglyme and tetraglyme, and cyclic ethers such as tetrahydrofuran, 1,4-dioxane, 1,3-dioxane and the dioxalanes. Other compounds which can be used as solvent include sulphones and sulphoxides . Examples of such compounds are dimethyl sulphone, diethyl sulphone, methyl ethyl sulphone, methyl butyl sulphone, sulpholane, 2-methylsulpholane, 3-methyl-suipholane, 2-methyl-4-butyl sulpholane, dimethyl sulphoxide and diethyl sulphoxide. Preference is given to the use of alkanoic acids especially acetic acid as solvent. It has been found that the mild conditions used in the process of the invention even tolerate the presence of some water in the reaction medium. Although the presence of water is not preferred, amounts of up to 15X, based on total solvent may be present. The process according to the invention can be carried out batch wise, semi-continuously or continuously. The reaction section may comprise one or more autoclaves or one or more reactor tubes the walls of which are made of or coated with inert materials. The reaction products may be worked up by techniques known in the art. For instance, the reaction product mixure comprising ethylidene diacetate, acetic acid anhydride and unconverted methyl acetate may be subjected to one or more (fractional) distillations to separate the main products ethylidene diacetate and acetic acid anhydride. The process according to the present invention is also of interest in that it can be integrated with known processes for the production of the starting materials (i.e. methyl acetate and dimethyl ether) and/or for the conversion of the acetic acid anhydride or ethylidene diacetate produced into other products. For instance, when the present process produces ethylidene diacetate, it can be integrated with a process for the preparation of methyl acetate and acetic acid by carbonylation of methanol and with a process for the preparation of vinyl acetate by decomposition of ethylidene diacetate into vinyl acetate and acetic acid. The acetic acid produced may be internally recycled and converted into methyl acetate by reaction with methanol. So an integrated process can be obtained producing vinyl acetate from methanol and synthesis gas. The following examples illustrate the invention: Example I The experiments 1-8 in this example were carried out using the same technique. The conditions and results of these examples are given in Table A. A Hastelloy C (Trade mark) 300 ml magnet driven autoclave was charged with methyl acetate, acetic acid and the necessary catalyst components. The vessel was flushed with carbon monoxide and then pressurized with carbon monoxide or carbon monoxide and hydrogen. The autoclave was then heated to a fixed temperature and kept at this temperature during a certain reaction time. The pressure was maintained constant during this reaction time by feeding in carbon monoxide and hydrogen at a ratio corresponding with the partial pressures. After the reaction the reaction mixture was analyzed by gas-liquid chromatography. The experiments 1-8 show the strong promotive effect of promotors according to the invention on Rh catalysts in absence as well as presence of prior art promotors. The experiments 1,4 and 7 are comparative experiments not according to the invention. Example II The experiments of this example were carried out using the same technique as in the experiments of Example I. The conditions and results are given in Table B. The experiments show that triphenyl phosphine oxide and pyridine oxide promote catalytic systems comprising Pd and prior art promotors. The experiment 9 and 11 are comparative experiments not according to the invention. Example Ill The experiments of this example were carried out using the same technique as for the experiments of Example I. The conditions and results are tabulated in Table C. The experiments show the use of a number of Group Va compounds as promotors for Rh based catalytic systems. Experiment 14 is not according to the invention and is included as comparative experiment. TABLE A Exp. Catalyst components mmol Iodide Charge, CO H2 Reaction Reaction production rate Group VIII Promoter Promoter ml partial partial temp time g/g metal/ metal compound of the MeOAc AcOH pressure pressure C h g iodide/h invention bar bar EDA AAA 1 RhCl3.3H2O CH3I 45 5 50 5 160 5 0.1 0.5 (0.25) 60 2 RhCl3.3H2O pyridine CH3I 45 5 50 5 160 5 0.2 17.6 (0.25) oxide (4) 60 3 RhCl3.3H2O ZrOCl2#8H2O pyridine CH3I 45 5 50 5 160 5 0.9 21.4 (0.25) (2) oxide (4) 60 4 RhCl3.3H2O ZrOCl2#8H2O CH3I 40 10 50 0 160 5 0 4.7 (0.25) (2) 60 5 RhCl3.3H2O Ph3P=O CH3I 40 10 50 0 160 5 0 8.8 (0.25) (4) 60 6 RhCl3.3H2O ZrOCl2#8H2O Ph3P=O CH3I 40 10 50 0 160 5 0 9.9 (0.25) (2) (4) 60 7 RhCl3.3H2O Ph3P=O CH3I 40 10 30 30 175 5 10.5 3.3 (0.25) (0.75) 60 8 RhCl3.3H2O Ph3P=O Ph3P=O CH3I 40 10 30 30 175 5 11.2 10.9 (0.25) (0.75) (4) 60 EDA = ethyldiene diacetate AAA = acetic acid anhydride MeOAc = methyl acetate AcOH = acetic acid TABLE B Exp. Catalyst components mmol Iodide Charge, CO H2 Reaction Reaction production rate Group VIII Promoter Promoter ml partial partial temp time g/g metal/ metal compound of the MeOAc AcOH pressure pressure C h g iodide/h invention bar bar EDA AAA 9 Pd(OAc)2 ZrOCl2.8H2O CH3I 45 5 50 5 150 5 0 0.45 (1) (2) 60 Ph3P (3) 0 Pd(OAc)2 ZrOCl2.8H2O Ph3P=0 CH3I 45 5 50 5 150 5 0 0.62 (1) (2) (4) 60 Ph3P (3) 1 Pd(OAc)2 Cr(CO)6 CH3I 45 5 30 15 155 5 0.6 2.3Cr (1) (2) 60 precipitate Ph3P after (3) reaction 2 Pd(OAc)2 Cr(CO)6 pyridine CH3I 45 5 30 15 155 5 2.1 2.3 (1) (2) oxide 60 Ph3P (4) (3) 3 Pd(OAc)2 Cr(CO)6 pyridine CH3I 45 5 30 15 155 5 3.1 0 0.6 acet (1) (0.5) oxide 60 aldehyde Ph3P (4) (3) EDA = ethyldiene diacetate AAA = acetic acid anhydride MeOAc = methyl acetate AcOH = acetic acid TABLE C EMI16.1 Exp. <SEP> Catalyst <SEP> components <SEP> mmol <SEP> Iodide <SEP> Charge, <SEP> CO <SEP> H2 <SEP> Reaction <SEP> Reaction <SEP> production <SEP> rate <tb> <SEP> Group <SEP> VIII <SEP> Promoter <SEP> Promoter <SEP> ml <SEP> partial <SEP> partial <SEP> temp <SEP> time <SEP> g/g <SEP> metal/ <tb> <SEP> metal <SEP> compound <SEP> of <SEP> the <SEP> MeOAc <SEP> AcOH <SEP> pressure <SEP> pressure <SEP> C <SEP> h <SEP> g <SEP> iodide/h <tb> <SEP> invention <SEP> bar <SEP> bar <SEP> EDA <SEP> AAA <tb> 14 <SEP> RhCl3.3H2O <SEP> CH3I <SEP> 45 <SEP> 5 <SEP> 20 <SEP> 40 <SEP> 160 <SEP> 5 <SEP> 0.6 <SEP> 0.5 <tb> <SEP> (0.25) <SEP> 60 <tb> 15 <SEP> RhCl3.3H2O <SEP> PH3P=O <SEP> CH3I <SEP> 45 <SEP> 5 <SEP> 30 <SEP> 30 <SEP> 160 <SEP> 5 <SEP> 7.4 <SEP> 4.3 <tb> <SEP> (0.25) <SEP> (4) <SEP> 60 <tb> 16 <SEP> RhCl3.3H2O <SEP> (PH3P=O)2HI3 <SEP> CH3I <SEP> 45 <SEP> 5 <SEP> 30 <SEP> 15 <SEP> 175 <SEP> 5 <SEP> 7.9 <SEP> 16.4 <tb> <SEP> (0.25) <SEP> (1) <SEP> 60 <tb> 17 <SEP> RhCl3.3H2O <SEP> ZrOCl2.8H2O <SEP> CH3-P-(OCH3)2 <SEP> CH3I <SEP> 40 <SEP> 5 <SEP> 50 <SEP> 5 <SEP> 160 <SEP> 5 <SEP> 0.3 <SEP> 11.2 <tb> <SEP> # <tb> <SEP> O <SEP> (4) <SEP> 60 <tb> 18 <SEP> RhCl3.3H2O <SEP> Ph3P <SEP> PH3P=S <SEP> CH3I <SEP> 25 <SEP> 25 <SEP> 20 <SEP> 40 <SEP> 175 <SEP> 5 <SEP> 17.0 <SEP> 0.4 <tb> <SEP> (0.25) <SEP> (0.75) <SEP> (4) <SEP> 60 <tb> 19 <SEP> RhCl3.3H2O <SEP> Ph3P <SEP> PH3P=O <SEP> CH3I <SEP> 25 <SEP> 25 <SEP> 20 <SEP> 40 <SEP> 175 <SEP> 5 <SEP> 15.5 <SEP> 0.3 <tb> <SEP> (0.25) <SEP> (0.75) <SEP> (4) <SEP> 60 <tb> 20 <SEP> RhCl3.3H2O <SEP> ZrOCl2.(H2O <SEP> PH3P=S <SEP> CH3I <SEP> 41 <SEP> 10 <SEP> 50 <SEP> 0 <SEP> 175 <SEP> 2 <SEP> 0 <SEP> 21.6 <tb> <SEP> (0.25) <SEP> (0.75) <SEP> (4) <SEP> 60 <tb> EDA = ethyldiene diacetate AAA = acetic acid anhydride MeOAc = methyl acetate AcOH = acetic acid

Claims: CLAIMS 1. A process for the preparation of ethylidene diacetate and/or acetic acid anhydride by reacting methyl acetate and/or dimethyl ether with carbon monoxide or a mixture of carbon monoxide and hydrogen at elevated temperature and pressure characterized in that the reaction is carried out in the presence of a homogeneous catalyst system comprising a Group VIII noble metal compound, a bromide or iodide source, and a Group Va compound represented by the general formula EMI17.1 in which X is a Group Va element having a valency above 3 selected from N, P, As or Sb; Y is a Group VIa element selected from 0, S, or Se and either a, b and c are 0 or 1 and R1, R2 and R3 are similar or dissimilar optionally substituted hydrocarbon groups; or a and b are 0 and c is O or 1 and R1 and R2 form together with X a heterocyclic group; or a, b and c are 0 and R1, R2 and R3 form together with X a heterocyclic aromatic group.. 2. A process according to claim 1 characterized in that the Group Va compound is represented by the general formula I in which a, b and c are 0, X is P, Y is O or S and R1, R2 and R3 are alkyl groups containing 1-4 carbon atoms or cycloalkyl, aryl or alkaryl groups containing 5-12 carbon atoms. 3. A process according to claim 2 characterized in that the Group Va compound is represented by the general formula I in which Y is O. 4. A process according to claim 3 characterized in that the Group Va compound is triphenyl phosphine oxide or triphenyl phosphine sulphide. 5. A process according to claim 1 characterized in that the Group Va compound represented by the general formula I is a phosphonate. 6. A process according to claim 1 characterized in that the Group Va compound is represented by the general formula I in which a, b and c are 0, X is N, Y is 0 and R1, R2 and R3 are alkyl groups containing 1-12 carbon atoms or cycloalkyl, aryl or alkaryl groups containing 5-12 carbon atoms, or R1 and R2 form together with X a heterocyclic group containing 4-12 carbon atoms or R1, R2 and R3 form together with X a heterocyclic aromatic ring containing 5-12 carbon atoms, preferably 5-7 carbon atoms. 7. A process according to claim 6 characterized in that the Group Va compound is pyridine oxide. 8. A process according to claims 1-7 characterized in that one or more Group Ia, IIa, lila, IVb or VI b metals or metal compounds are present in the reaction mixture as co-promotor. 9. A process according to claim 8 characterized in that a group IVb metal compounds is present in the reaction mixture. 10. A process according to claim 9 characterized in that the Group IVb metal compound is a zirconium compound. 11. A process according to claim 8 characterized in that a chromium compounds is present in the reaction mixture. 12. A process according to claim 1 characterized in that a trivalent Group Va compound is present in the reaction mixture as co-promotor. 13. A process according to claim 12 characterized in that the trivalent Group Va compound is a phosphine. 14. A process according to claim 13 characterized in that the phosphine is triphenyl phosphine. 15. A process according to claims 1-14 characterized in that the Group Va compound represented by the general formula I is present in an ratio of 0.01:1 to 200:1 mole Group Va compound per gram atom Group VIII of nobel metal. 16. A process according to claims 1-15 characterized in that the reaction is carried out at a temperature in the range of 50 C to 2000C and preferably between 1400C and 190 C. 17. A process according to claims 1-16 characterized in that the process is carried out using a pressure in the range of from 20 to 100 bar. 18. A process according to claims 1-17 characterized in that the process is carried out in the presence of an alkanoic acid as solvent.

Inventors: DRENT, EIT
Applicants: SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1983
Main classification: C07C69
IPC codes: B01J31, C07C53, C07C27, C07C67, C07B61, C07C51, C07C69