PROCESS FOR PREPARING (HYDROCARBYLTHIO) AMINES AND THE USE OF SUCH AMINES

Abstract: (Hydrocarbylthio)aromatic polyamines are prepared by reacting an aromatic polyamine, such as a diamino­ benzene, with a hydrocarbyl disulfide, such as an alkyl disulfide, in the presence of an iodide or bromide of a metal other than an alkali metal as a catalyst.

Description: This invention relates to (hydrocarbylthio)aromatic polyamines and more particularly to a process for prepar­ ing them. As disclosed in U. S. Patent 4,594,453 (Ranken et al.), it is known that various (hydrocarbylthio)aromatic amines are useful as intermediates in the preparation of polyurethanes, and they can be prepared by reacting an aromatic amine with a hydrocarbyl disulfide in the presence of a catalytic amount of a Lewis acid. The preferred catalysts of Ranken et al. are metal halides, such as aluminum chloride, boron trifluoride, boron trichloride, ferric chloride, and zinc chloride. In the case of the diamines, it has been found that the preferred catalysts identified by Ranken et al. have the disadvantages of effecting the desired hydrocarbyl­ thiations at too slow a rate to be completely satisfactory and of sometimes providing too low a yield of product. An object of this invention is to provide a novel process for preparing (hydrocarbylthio)aromatic diamines. Another object is to provide such a process wherein the products are prepared by the hydrocarbylthiation of aromatic polyamines in the presence of metal halide catalysts. A further object is to provide such a process wherein the reaction rates and/or product yields are improved. These and other objects are attained by reacting an aromatic polyamine with a hydrocarbyl disulfide in the presence of a catalytic amount of an iodide or bromide of a metal other than an alkali metal. Aromatic polyamines utilizable in the practice of the invention are compounds having at least two amino groups attached to a carbocyclic or heterocyclic ring of an aromatic compound containing one or more simple and/or fused rings, such as benzene, naphthalene, anthracene, pyrrole, pyridine and indole. The compounds may bear no substituents other than the required amino groups, or they may bear substituents inert to the reaction conditions, such as chloro, fluoro, alkyl, alkoxy, alkylthio, aryl, aryloxy, arylthio, alkaryl, or aralkyl groups on any positions other than those to be substituted by hydro­ carbylthio groups. In the case of coupled aromatic rings, the rings may be directly attached to one another or may be coupled through a bridge such as an oxygen, sulfur, sulfoxide, sulfone, alkyl, or other hydrocarbon link. Useful aromatic polyamines include, for example, 1,5-diaminonaphthalene, 2,6-diaminopyridine, 1,2-diamino­ benzene, 1,3-diaminobenzene, 1,4-diaminobenzene, 2,4-diaminotoluene, 2,6-diaminotoluene and 2,6-diamino-1-­ ethylbenzene. Hydrocarbyl disulfides which may be reacted with the aromatic polyamines include saturated and unsaturated aliphatic, cycloaliphatic, and aromatic disulfides in which the hydrocarbyl groups optionally bear inert, such as chloro, substituents. Exemplary of such compounds are methyl, ethyl, propyl, n-butyl, sec-butyl, t-butyl, 2-chloropentyl, cyclopentyl, cyclohexyl, phenyl, benzyl, p-tolyl, and p-chlorophenyl disulfides. This component of the reaction mixture is generally employed in at least the stoichiometric amount required to yield the desired (hydrocarbylthio)aromatic amine; that is, at least an equimolar amount being used when a mono(hydrocarbylthio)­ aromatic amine is desired, and at least two molar equivalents being utilized when a di(hydrocarbylthio)­ aromatic amine is desired. The reaction of the aromatic polyamine with the hydrocarbyl disulfide is generally conducted at a tempera­ ture in the range of 20-300°C., preferably 100-200°C., and at a pressure of atmospheric up to 1000 psi; and, as men­ tioned above, it is conducted in the presence of a cata­ lytic amount of a non-alkali metal iodide or bromide. Metal iodides and bromides that can be used in the practice of the invention can be any of the known Lewis acid catalysts which are iodides or bromides of metals other than alkali metals, such as the ferrous, ferric, cuprous, cupric, zinc, cadmium, lead, cobaltous, mercu­ rous, and mercuric iodides and bromides. The preferred catalysts, however, are the iodides, especially cuprous, ferrous, cobaltous, cadmium, and zinc iodides. The catalyst is employed in catalytic amounts, generally in a catalyst/aromatic amine mol ratio of 0.01-0.5/1, preferably 0.01-0.2/1. In conducting the process of the invention, it is frequently preferred to (1) heat a mixture of the catalyst and aromatic polyamine at a suitable temperature, usually a temperature higher than the boiling point of the disul­ fide to be added, usually 100-150°C., until all of the catalyst has reacted and then (2) maintain the reaction mixture at reflux temperature after the disulfide has been added to effect a hydrocarbylthiation process while removing evolved hydrocarbyl thiol by-product from the reaction vessel. It is also satisfactory to conduct the process by simply mixing the catalyst and reactants together and heating them to the reflux temperature. An inert solvent may be employed if desired. The metal iodide or bromide may be used in conjunction with another catalyst or a promoter, such as boron trifluoride etherate. The process of the invention, like the process of Ranken et al., results in the formation of (hydrocarbyl­ thio)aromatic amines which are useful as intermediates in the preparation of polyurethanes. It is particularly advantageous in that it is characterized by higher reac­ tion rates and/or higher yields than are obtained when the metal chlorides of Ranken et al. are used. The following examples are given to illustrate the invention and are not intended as a limitation thereof. COMPARATIVE EXAMPLE A One molar proportion of commercial toluenediamine (c-TDA) -- a material containing 80% 2,4-diaminotoluene and 20% 2,6-diaminotoluene -- was heated with 0.065 molar proportion of aluminum chloride at 150°C. for one hour. Methyl disulfide was then added in sufficient excess to maintain the reaction temperature at 135°C., and the reaction was conducted for 39 hours to achieve 100% con­ version of the c-TDA. Analysis of the product showed it to contain 16 mol% mono(methylthio) derivatives of c-TDA (MMTDA), 78 mol% di(methylthio) derivatives of c-TDA (DMTDA), and 6 mol% by-products. EXAMPLE I Each of seventeen reactions was conducted essen­ tially as described in Comparative Example A except for substituting 0.05 molar proportion of another catalyst for the 0.065 molar proportion of aluminum chloride. The catalysts employed, the reaction times required, the conversions obtained, and the percentages of MMTDA and DMTDA in the final product are shown below. EXAMPLE II Comparative Example A was essentially repeated except that 0.045 molar proportion of zinc bromide was substituted for the aluminum chloride and the reaction time was only 21 hours. The reaction resulted in 95% conversion, and analysis showed the product to contain 46 mol% MMTDA and 54 mol% DMTDA. EXAMPLE III Comparative Example A was essentially repeated except that 0.044 molar proportion of zinc iodide was sub­ stituted for the aluminum chloride and the reaction time was only 19 hours. The reaction resulted in 98% conver­ sion, and analysis showed the product to contain 30 mol% MMTDA and 68 mol% DMTDA. EXAMPLE IV Comparative Example A was essentially repeated except that 0.02 molar proportion of zinc iodide and 0.033 molar proportion of boron trifluoride etherate were sub­ stituted for the aluminum chloride and the reaction time was only 20.5 hours. The reaction resulted in 100% con­ version, and analysis showed the product to contain 12 mol% MMTDA and 86 mol% DMTDA. COMPARATIVE EXAMPLE B Comparative Example A was essentially repeated except that 0.05 molar proportion of boron trifluoride etherate was substituted for the aluminum chloride and the reaction was continued for only 7.5 hours, at which time it was terminated because of the substantial absence of any reaction. It is obvious that many variations may be made in the products and processes set forth above without departing from the spirit and scope of this invention.

Claims: 1. A process comprising reacting an aromatic polyamine with a hydrocarbyl disulfide in the presence of a catalytic amount of an iodide or bromide of a metal other than an alkali metal to form a (hydrocarbylthio)aromatic amine. 2. A process as claimed in claim 1 in which the aromatic polyamine is a diaminobenzene or a diaminotoluene. 3. A process as claimed in claim 2 in which the aromatic polyamine is a mixture containing 2,4-diaminotoluene and 2,6-diaminotoluene. 4. A process as claimed in any one of claims 1 to 3 in which the hydrocarbyl disulfide is methyl disulfide. 5. A process as claimed in any one of claims 1 to 4 in which the metal iodide or bromide is zinc iodide, cuprous iodide, ferrous iodide, cadmium iodide, or cobaltous iodide. 6. The use of an iodide or bromide of a metal other than an alkali metal as a catalyst in effecting hydrocarbylthiation of an aromatic diamine. 7. The preparation of a polyurethane employing a (hydrocarbylthio)aromatic amine formed by a process as claimed in any one of claims 1 to 5 or in the use claimed in claim 6.

Inventors: DAVIS, ROBERT LYNN
Applicants: ETHYL CORPORATION
Application year: 1987
Main classification: C07C319
IPC codes: C07C321, C07C319