PROCESS FOR THE PREPARATION OF ORGANIC ISOCYANATES

Abstract: Process for the preparation of organic isocyanates by reacting an aromatic nitro compound with carbon monoxide in the presence of (a) Pd or a Pd compound, (b) a ligand of formula in which X and Y are the same or different bridging groups each of which has 3 or 4 atoms in the bridge, of which atoms at least two are carbon atoms and which groups X and Y may be bound to each other, and (c) one or more protonic acids, except hydrohalogenic acids.

Description: The invention relates to a process for the preparation of organic isocyanates by reacting an aromatic nitro compound with carbon monoxide in the presence of a catalytic system based on palladium and/or a palladium compound and a group 5A ligand. Organic isocyanates are valuable and versatile starting materials, for example for the production of polyurethanes and related compounds. Numerous attempts have been made over the years to find alternative routes to the well-known preparation of isocyanates (or their precursors the carbamates), especially the most important ones such as toluenediisocyanate (TDI) and methylene-4,4′-di­ phenyldiisocyanate (MDI) via the so-called "phosgene route". Reference is made in this respect to "Recent Advances in Isocyanate Chemistry" by S. Ozaki-Chem. Rev., 72 (1972) 457-496. According to US patent specification 3,914,268 organic isocyanates are prepared by contacting an aromatic nitro compound with carbon monoxide in the presence of a catalyst system comprising a platinum group metal compound, an aromatic nitrogenous heterocyclic compound and a component selected from water, hydrogen, hydrogen halides, boric acids, formic acid, oxalic acid and formaldehyde. A disadvantage of this known process is that carbon monoxide usually has to be applied at an extremely high partial pressure. It has now surprisingly been found that organic isocyanates can be produced at a relatively low pressure, with a high reaction rate and with high selectivity when the process described in the beginning of this specification is carried out in the presence of a distinct type of ligand and of an acid. This favourable effect of the addition of an acid only occurs when the reaction is carried out with the distinct type of ligand used according to the invention, and not with ligands such as, for example, triphenyl­ phosphine or pyridine. Accordingly, the present invention provides a process for the preparation of organic isocyanates by reacting an aromatic nitro compound with carbon monoxide, which process is carried out in the presence of a catalytic system prepared by combining:- a) palladium and/or a palladium compound, b) a ligand having the general formula I in which X and Y are the same or different bridging groups each of which has 3 or 4 atoms in the bridge, of which atoms at least two are carbon atoms and which groups X and Y may be bound to each other, and c) one or more protonic acids, except hydrohalogenic acids. The process according to the present invention is not only advantageous in that the aromatic nitro compound can be converted into the appropriate isocyanate with selectivities above 90%, but also because corrosion problems are of little significance. Furthermore, the recovery of palladium is not very cumbersome. Another important feature of the process of the invention is that it enables the preparation of isocyanates from aromatic nitro compounds and CO under moderate conditions in good yield and with a high reaction rate. In view of this the process is of great practical interest. The bridging groups X and Y in formula I are connected with each other via the two carbon atoms shown in the formula. Apart from the connection as shown there may exist a second connection between the bridging groups, as is the case in 1,10-phenanthroline and derivatives thereof. Any atoms in the bridging groups X and Y other than carbon atoms are preferably nitrogen atoms. Furthermore, X and Y are preferably the same. Examples of suitable bidentate ligands of formula I are 2,2′-bipyridyl and derivatives thereof, for example 4,4′-dimethyl-­ 2,2′-bipyridyl, 4,4′-dichlorobipyridyl, 4,4′-dimethoxybipyridyl, 4,4′-dicarboxybipyridyl and 2,2′-biquinolyl. Other examples of suitable bidentate ligands of formula I are 1,10-phenanthroline and derivatives thereof, for example 5-chloro­ phenanthroline, 4,7-diphenylphenanthroline, 4,7-dimethylphenanthro­ line, 2,9-dichlorophenanthroline, 1,10-phenanthroline-5-sulphonic acid and the 4,7-diphenyl-1,10-phenanthroline-disulphonic acids. Further examples of suitable bidentate ligands of formula I are 2-(2-pyridyl)benzimidazole, 3-(2-pyridyl)-5,6-diphenyl-1,2,4-­ triazine and the monosodium salt of 3-(2-pyridyl)-5,6-diphenyl-­ 1,2,4-triazine-p,p′-disulphonic acid. The bidentate ligand preferably present in the catalytic system is 2,2′-bipyridyl or a derivative thereof or 1,10-phenan­ throline or a derivative thereof. Particularly preferred are 2,2′-bipyridyl and 1,10-phenanthroline. According to a preferred embodiment of the present invention use is made of one or more protonic acids having the general formula II RQ (II) in which R represents an optionally substituted aromatic group and Q represents an SO₃H, OH or C(O)OH group. The aromatic group represented by R may be, for example, a 1-naphthyl, 2-naphthyl, 1-,2- or 9-anthryl, 4-phenanthryl, or, what is preferred, an optionally substituted phenyl group. The aromatic group may be substituted with, for example, alkyl, cycloalkyl, phenyl, alkoxy, cycloalkoxy, phenoxy and, what is preferred, halogen atoms, i.e. iodine, bromine, chlorine and fluorine atoms. Very good results have been obtained with chlorinated aromatic groups. Preferred acids are 2,4,5-trichlorobenzenesulphonic acid, pentachlorophenol, 2,6-dichlorobenzoic acid and p-toluenesulphonic acid. Other examples of suitable acids of formula II are benzenesulphonic acid, 2,6-dichlorobenzenesulphonic acid, 2,6-dibromobenzenesulphonic acid, 2,6-difluorobenzenesulphonic acid, 2,4,6-trichlorobenzene­ sulphonic acid, 2,6-dichlorophenol, 2,6-difluorophenol, 2,4,6-tri­ bromophenol, 2,4,6-trifluorophenol, 2,4,6-trichlorobenzoic acid, 2,4,6-tribromobenzoic acid and 2,4,6-trifluorobenzoic acid. The acid of the general formula II may be an ion exchange resin con­ taining sulphonic acid groups, such as, for example, Amberlite 252H ("Amberlite" is a trade name), the group R being a polymeric hydrocarbon group, for example a polystyrene group substituted with sulphonic acid groups. Use may be made of two or more different protonic acids of the general formula II, for example of an acid of formula II in which Q represents an SO₃H group and one in which Q represents an OH group or a C(O)OH group, or of an acid of formula II in which Q represents an OH group and one in which Q represents a C(O)OH group. Other examples of protonic acids that may be used in the process according to the present invention are those that can be formed, possibly in situ, by interaction of a Lewis acid, such as, for example, BF₃, AsF₅, SbF₅, PF₅, TaF₅ or NbF₅ with a Broensted acid such as, for example, a hydrohalogenic acid, in particular HF, fluorosulphonic acid, phoshoric acid or sulphuric acid. Specific examples of the last-named type of acids are H₂SiF₆, HBF₄, HPF₆ and HSbF₆. Examples of sulphonic acids that can be used are fluor­ osulphonic acid, trifluoromethylsulphonic acid, and chlorosulphonic acid. HClO₄ is another example of an acid that may be used. Further examples of protonic acids are alkanoic acids, particularly those having not more than 12 carbon atoms per molecule, for example acetic acid, propionic acid, butyric acid, isobutyric acid, valeric acid, isovaleric acid, pivalic acid, heptanoic acid and lauric acid. If use is made of n protonic acids, n being an integer, for example 2, not more than n-1 protonic acids may be present in the form of salts thereof with a transition metal, for example with copper, iron, cobalt, nickel, manganese, chromium, vanadium or titanium. For example, use may be made of a salt of a transition metal, particularly copper, of an acid of formula II in which R represents an optionally substituted phenyl group and Q an SO₃H group, in combination with an acid of formula II in which R also represents an optionally substituted phenyl group and Q a C(O)OH group. The process according to the present invention is carried out in the presence of palladium and or a palladium compound. Palladium can be used as such, deposited on an inert carrier such as carbon or alumina, or in the form of palladium compounds, especially palladium salts. Good results can also be obtained when a palladium compound is used which is substantially soluble in the prevailing reaction mixture. Examples of convenient palladium salts include palladium chloride, palladium bromide, palladium iodide, sodium tetrachloro­ palladate, potassium tetrachloropalladate, potassium tetra-iodo­ palladate, palladium acetate, palladium propionate, palladium isobutyrate, palladium acetylacetonate and similar palladium compounds. Preference is given to the use of palladium salts of organic acids, in particular of an alkanoic acid having not more than 12 carbon atoms per molecule. Very good results have been obtained with palladium acetate. As stated hereinbefore, the isocyanates are prepared from aromatic nitro compounds, i.e. compounds containing at least one aromatic group in which an NO₂ group is directly attached to a carbon atom forming part of an aromatic nucleus. Examples of aromatic nitro compounds include nitrobenzene, alkyl- and alkoxy-­ nitrobenzenes, aryl- and aryloxy-nitrobenzenes, dinitrobenzenes, alkyl- and alkoxy-, aryl- and aryloxy-dinitrobenzenes, such as 2,4-dinitrotoluene, 2,6-dinitrotoluene and 4,4′-dinitrodiphenyl­ methane, and polynitrobenzenes. Preferred aromatic nitro compounds are nitrobenzene, m-dinitrobenzene, 2-, 3- and 4-nitrotoluene, 2,4-dinitrotoluene, 2,6-dinitrotoluene and 4,4′-dinitrodiphenyl­ methane. Mixtures of two or more aromatic nitro compounds can be applied, e.g. a mixture of two dinitrotoluenes. The amount of palladium or palladium compound to be used in the process according to the present invention is conveniently between 0.001 %w and 10 %w, in particular between 0.005 %w and 3 %w, calculated on the amount of nitro compound present in the reaction mixture. The use of rather small amounts of palladium compounds, e.g. less than 0.5 %w, calculated on nitro compound present in the reaction mixture, is preferred. The ligands according to the general formula I may be used in such an amount that the ratio (palladium or palladium compound): ligand according to the general formula I is conveniently between 0.05 and 50, preferably between 0.1 and 20. The amount of protonic acid present in the reaction mixture preferably lies between 0.01 and 150, more preferably between 0.1 and 100, and most preferably between 1 and 50 equivalents per gram atom of palladium. A molar ratio ligand of formula I to protonic acid in the range of from 0.2 to 5 is suitably used. The process according to the present invention can be carried out conveniently at temperatures up to 300 °C. Preference is given to the use of temperatures in the range between 75 °C and 200 °C, in particular between 85 °C and 175 °C. The reaction is normally carried out at superatmospheric pressure; pressures of up to 500 bar can be applied. Preferably, the process is operated at a pressure in the range of from 10 to 150 bar. Good results can already be obtained using initial pressures between 30 and 80 bar. The process according to the present invention is suitably carried out in the presence of an aprotic solvent. Examples of suitable solvents are hydrocarbons such as hexane, cyclohexane, octane, benzene, toluene, the threee xylenes, ethylbenzene and cumene; halogenated hydrocarbons such as chloroform, 1,2-dichloro­ ethane, perfluoroalkanes, chlorobenzene and the three dichloro­ benzenes; ethers such as tetrahydrofuran, diethyl ether, 3,6-dioxa­ octane, methyl tert.-butyl ether, dioxane, anisole, 2,5,8-triox­ anonane (also referred to as "diglyme") diphenyl ether and diisopropyl ether; N,N-dialkyl-substituted amides, such as N,N-dimethylformamide and N-methylpyrrolidone; sulphones such as diisopropyl sulphone and tetrahydrothiophene 1,1-dioxide (also referred to as "sulpholane"); esters such as methyl benzoate and ethyl acetate. The process according to the present invention can be carried out batchwise, semi-continuously or continuously. The reaction time is, of course, related to the temperature and pressure adopted. In general, reaction times between 1 and 20 hours appear to be adequate. The following examples further illustrate the invention. The experiments were carried out in a 300 ml magnetically stirred Hastelloy C autoclave ("Hastelloy" is a trade mark). The selectivi­ ty to a certain compound, expressed in a percentage, is defined herein as 100 × a/b, in which "a" is the amount of starting compound that has been converted into that certain compound and "b" is the total amount of starting compound that has been converted. Examples 1-7 Example 1 was carried out as follows. The autoclave was charged with nitrobenzene (7.5 ml), toluene (50 ml), palladium(II) acetate (0.8 mmol), 2,2′-bipyridyl (10 mmol), p-toluenesulphonic acid (1 mmol) and pentachlorophenol (5 mmol). Then, consecutively, the autoclave was pressurized with carbon monoxide until an initial pressure of 70 bar was reached, the temperature was raised to 150 °C, the reaction mixture was kept at this temperature for 5h, the reaction mixture was allowed to cool to ambient temperature and was analysed using gas-liquid chromatography. The conversion of nitrobenzene was 90% with a selectivity to phenyl isocyanate of 80%. Table 1 hereinafter shows the relevant data of this example; p-toluenesulphonic acid is abbreviated to "pTsA" in this table. Examples 2-7 were carried out in the same manner as Example 1, but with the differences as stated in Table 1; the results of Examples 4-7 were measured after 3 h. This table also presents the results. Example 8 The autoclave was charged with nitrobenzene (7.5 ml), diglyme (50 ml), palladium (II) acetate (0.8 mmol), 2,2′-bipyridyl (20 mmol), p-toluenesulphonic acid (1 mmol) and acetic acid (20 mmol). Then, consecutively, the autoclave was pressurized with carbon monoxide (initial pressure 60 bar), the temperature was raised to 150 °C, the reaction mixture was kept at this temperature for 1.5 h and the reaction mixture was allowed to cool to ambient temperature. The conversion of nitrobenzene was 80%, with a selectivity to phenyl isocyanate of 61%. Example 9 The autoclave was charged with nitrobenzene (15 ml), diglyme (42.5 ml), palladium (II) acetate (0.8 mmol), 2,2′-bipyridyl (20 mmol), cupric tosylate (1 mmol) and 2,6-dichlorobenzoic acid (10 mmol). Then, consecutively, the autoclave was pressurized with carbon monoxide (inital pressure 70 bar), the temperature was raised to 150 °C, the reaction mixture was kept at this temperature for 5 h and the reaction mixture was allowed to cool to ambient temperature. The conversion of nitrobenzene was 40%, with a selectivity to phenyl isocyanate of 85%. Example 10 The autoclave was charged with nitrobenzene (15 ml), p-xylene (50 ml), palladium(II) acetate (0.8 mmol), 1,10-phenanthroline (10 mmol), 2,4,5-trichlorosulphonic acid (1 mmol) and 2,6-dichloro­ benzoic acid (10 mmol). Then, consecutively, the autoclave was pressurized with carbon monoxide (initial pressure 70 bar), the temperature was raised to 150 °C, the reaction mixture was kept at this temperature for 3 h and the reaction mixture was allowed to cool to ambient temperature. The conversion of nitrobenzene was 46%, with a selectivity to phenyl isocyanate of 60%. Comparative Experiment The autoclave was charged with nitrobenzene (7.5 ml), diglyme (50 ml), palladium(II) acetate (0.2 mmol), pyridine (20 mmol), p-toluenesulphonic acid (1 mmol) and acetic acid (20 mmol). Then, consecutively, the autoclave was pressurized with carbon monoxide (initial pressure 60 bar), the temperature was raised to 150 °C, the reaction mixture was kept at this temperature for 5 h and the reaction mixture was allowed to cool to ambient temperature. Phenyl isocyanate could not be detected in the reaction mixture.

Claims: 1. Process for the preparation of organic isocyanates by reacting an aromatic nitro compound with carbon monoxide, which process is carried out in the presence of a catalytic system prepared by combining:- a) palladium and/or a palladium compound, b) a ligand having the general formula I in which X and Y are the same or different bridging groups each of which has 3 or 4 atoms in the bridge, of which atoms at least two are carbon atoms and which groups X and Y may be bound to each other, and c) one or more protonic acids, except hydrohalogenic acids. 2. Process as claimed in claim 1, in which X and Y are also bound to each other by means of a connection other than that formed by the carbon atoms shown in formula I. 3. Process as claimed in claim 2, in which the ligand is 1,10-phenanthroline or a derivative thereof. 4. Process as claimed in claim 2, in which the ligand is 2,2′-bipyridyl or a derivative thereof. 5. Process as claimed in any one of the preceding claims, in which use is made of one or more protonic acids having the general formula II RQ (II) in which R represents an optionally substituted aromatic group and Q represents an SO₃H, OH or C(O)OH group. 6. Process as claimed in claim 5, in which R represents an optionally substituted phenyl group. 7. Process as claimed in claim 5 or 6, in which the aromatic group is halogenated. 8. Process as claimed in claim 7, in which the aromatic group is chlorinated. 9. Process as claimed in claim 8, in which use is made of 2,4,5-trichlorobenzenesulphonic acid. 10. Process as claimed in claim 8, in which use is made of penta­ chlorophenol. 11. Process as claimed in claim 8, in which use is made of 2,6-di­ chlorobenzoic acid. 12. Process as claimed in claim 6, in which use is made of p-toluenesulphonic acid. 13. Process as claimed in any one of the preceding claims, in which the palladium compound is a palladium salt of an organic acid. 14. Process as claimed in any one of the preceding claims, which is carried out at a temperature in the range of from 75 °C to 200 °C. 15. Process as claimed in any one of the preceding claims, which is carried out at a pressure in the range of from 10 to 150 bar.

Inventors: DRENT, EIT
Applicants: SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1986
Main classification: C07C265
IPC codes: C07C265, B01J31, C07C67, C07D213, C07C263, C07C241, C07B61