Process for making aromatic nitriles

Abstract: In a process for making an aromatic nitrile a benzotrichloride is reacted with an ammonium halide in the presence of an oxygen-donating initiator at a temperature of about 150 to about 250°C. An optional catalyst of a metal oxide or a metal salt can be used if desired.

Description: This invention relates to a method of making an aromatic nitriles from a benzotrihalide and an ammonium halide. Aromatic nitriles are important intermediates in the dye and pharmaceutical industries. At the present time, benzonitrile and chlorinated benzonitriles are made on an industrial scale by reacting benzotrichloride or a chlorinated benzotrichloride, respectively, with ammonia gas, ammonium hydroxide, or ammonium chloride in the presence of a catalyst such as ferric chloride, zinc chloride, copper chloride, or copper oxide. While these reactions produce the desired product, they also produce unwanted byproducts, such as tar residues, resulting in a significant amount of solid waste. Also, some of the reactions have been found to selectively form triazine in the presence of catalysts such as ferric chloride. EP0441004 discloses the preparation of aromatic nitriles by heating a mixture of an ammonium halide, a trichloromethyl aromatic starting material and a catalyst comprising a metal oxide or metal salt. Japanese Patent Application No. 06283006 discloses the preparation of 3,4-dichlorobenzonitrile from 3,4-dichlorobenzotrichloride, an ammonium halide, sulfolane, and a copper catalyst. According to this invention there is provided a method of making an aromatic nitrile having the general formula comprising (A) preparing a mixture which comprises (1) a benzotrihalide having the general formula where X is halogen, R is halogen or aliphatic from C 1 to C 8 or aromatic from C 6 to C 8 , and n is 0 to 5; (2) an ammonium halide in an amount within about 50 mole% of stoichiometric with said benzotrihalide; (3) 0.001 to 0.25 equivalents of an initiator comprising an acid halide, or an optionally substituted benzoic acid, benzamide, benzoic acid anhydride or benzoic acid chloride; and (B) heating said mixture at 150 to 250°C. In preferred embodiments of the invention n may be 0 to 4, or 0 to 3, or 0 to 2, or 0 to 1. In a preferred embodiment; (1) said benzotrihalide has the general formula; where n is 1 to 3; and (2) said ammonium halide is present in an amount within 20 mole% of stoichiometric with said benzotrihalide. Preferably X is chlorine or bromine.Preferably the method includes the additional last step of recovering said aromatic nitrile from said mixture by distillation.Conveniently, said benzotrihalide is benzotrichloride.Advantageously said ammonium halide is ammonium chloride.Preferably said ammonium halide is formed in situ by the addition of gaseous ammonia to said mixture.Advantageously said initiator is the acid, acid chloride, or amide that corresponds to said aromatic nitrile. In a preferred embodiment, (1) said benzotrihalide comprises chlorobenzotrichloride having the general formula; where n is 1 to 3; (2) said ammonium chloride is present in an amount between stoichiometric and up to 5 mole % in excess of stoichiometric with said chlorobenzotrichloride; (3) said initiator is present in an amount from 0.02 to 0.15 equivalents and is the acid, acid chloride, or amide that corresponds to said aromatic nitrile, which reacts with said chlorobenzotrichloride and said ammonium chloride to form said aromatic nitrile; and (B) heating said mixture at 180 to 230°C; and (C) recovering said aromatic nitrile from said mixture by distillation. Conveniently said benzotrihalide is orthochlorobenzotrichloride, or parachlorobenzotrichloride or 3,4-dichlorobenzotrichloride. The initiator may be incorporated in the mixture of benzotrihalide and ammonium chloride by admixing the initiator into the mixture. However, alternatively, said initiator is an acid chloride that is formed in situ by the reaction of water with said benzotrihalide. Optionally the mixture comprises up to 5 wt% of a metal oxide or metal salt catalyst. Conveniently the amount of said catalyst is 100 ppm to 1 wt%. Conveniently the metal of the catalyst is zinc or copper. Preferably said catalyst is zinc chloride or copper chloride. We have discovered that benzotrihalides (including substituted benzotrihalides) can be reacted with an ammonium halide to form benzonitriles by using an oxygen-donating initiator. In the reaction of this invention, a catalyst is not essential. Unlike prior processes for producing aromatic nitriles, the process of this invention does not produce significant amounts of solid waste and does not need a large excess of an ammonia source. The invention will now be described in detail by way of example. In the process of this invention, a benzotrihalide is reacted with an ammonium halide in the presence of an oxygen-donating initiator. The benzotrihalide starting material has the general formula where X is Cl or Br, R is halogen, aliphatic from C 1 to C 8 , or aromatic from C 6 to C 8 , and n is 0 to 5. The X group is preferably chlorine because benzotrichlorides are less expensive than other benzotrihalides. Alternatively the X group may be bromine. The R group is preferably halogen, such as chlorine, or alkyl from C 1 to C 5 as those benzotrihalides are more readily available, and n is preferably 1 to 3 as those benzotrihalides are more important commercially at the present time. (It should be noted that the general formula is intended to cover only compounds that can be made, as some of the multiply substituted benzotrihalides cannot be made at this time.) Examples of compounds within the general formula include benzotrichloride (BTC), o-chlorobenzotrichloride (OCBTC), p-chlorobenzotrichloride (PCBTC), m-chlorobenzotrichloride, 2,4-dichlorobenzotrichloride (2,4-DCBTC), 3,4-dichlorobenzotrichloride (3,4-DCBTC), 3,5-dichlorobenzotrichloride, benzotribromide, o-chlorobenzotribromide, m-trifluorotrichloroxylene, and m-hexachloroxylene. The preferred compounds are BTC, OCBTC, PCBTC, and 3,4-DCBTC, because those compounds make commercially important nitriles. The benzotrihalide is reacted with an ammonium halide, which can be ammonium chloride, ammonium bromide, or ammonium fluoride. Ammonium chloride and ammonium bromide are preferred and ammonium chloride is particularly preferred as it is inexpensive. The ammonium halide can be formed in situ by the reaction of gaseous ammonia with the hydrogen halide byproduct of the reaction. The amount of ammonium halide can be within 50 mole% of stoichiometric with the amount of benzotrihalide as the reaction proceeds well in that range; it is preferably within 20 mole% of stoichiometric and is most preferably stoichiometric or up to 5 mole% in excess of stoichiometric. The reaction must be performed in the presence of an initiator, which is in the form of an oxygen donating initiator, as it will not proceed at a significant rate in the absence of an initiator. The preferred initiator is an acid halide or a compound that can react with benzotrihalide or a substituted benzotrihalide to form the corresponding acid halide. Examples of preferred initiators include benzoic acid, benzamide, benzoic acid anhydride, and benzoyl chloride. The initiator can be admixed into the mixture of benzotrihalide and ammonium halide before the mixture is heated (as will be described below). Thus the initiator may be mixed with either the benzotrihalide before it is mixed with the ammonium halide, or with the ammonium halide before it is mixed with the benzotrihalide; or the initiator may be added to the mixture of the benzotrihalide and the ammonium halide, or the benzotrihalide, the ammonium halide and the initiator may be admixed simultaneously. Alternatively, the initiator can be formed in situ in the mixture of the benzotrihalide and the ammonium halide by adding, to the mixture, a compound, such as water, ammonium hydroxide, or magnesium oxide, that will react with the benzotrihalide to form an acid chloride. The preferred initiators (or compounds that form initiators in situ) react with the ammonium halide to form the desired nitrile product, thereby increasing product yield and avoiding the production of a mixture of nitriles. If the initiator is an acid, acid chloride, or amide it preferably corresponds to the product nitrile so that it will be converted into the desired product. For example, if the desired product is o-chlorobenzonitrile (OCBN), the preferred initiators are water, o-chlorobenzoic acid (OCBA), o-chlorobenzoyl chloride (OCBOC), or o-chlorobenamide (OCBAM) because those initiators will react with OCBTC and the ammonium halide to form OCBN. The amount of initiator is critical to the success of the reaction. If too much initiator is present, the reaction rate is faster but a significant amount of the corresponding acid and amide will be formed as well as the desired nitrile. If too little initiator is present, the reaction may take so long as to be impractical. We have found that the amount of initiator available to the reaction must be between 0.001 and 0.25 equivalents in order to avoid the ill effects of too little or too much initiator. For best results, the amount initiator should be between 0.02 and 0.15 equivalents. Since some initiators (or compounds that form initiators), such as water, may evaporate if the reaction is not performed under pressure, the amount of initiator should be calculated as the amount that is available to the reactants and not the amount that is placed in the reaction mixture or formed in situ in the reaction mixture. Preferably, no catalyst is used in the process of this invention because we have found that a catalyst increases the amount of tar produced and can change the selectivity so that in some cases more triazine is made. However, if desired, an optional catalyst can be used to increase the reaction rate. Catalysts that can be used in the reaction of this invention are metal salts (e.g., halides) and metal oxides of Groups IB, IIB, IIIA, IIA, and VIII of the Periodic Table. The preferred catalysts are metal oxides or metal salts where the metal is copper or zinc. Zinc chloride and copper chloride are the most preferred catalysts because they work well at ppm levels. When making p-chlorobenzonitrile (PCBN) and 3,4-dichlorobenzonitrile (3,4-DCBN) ferric chloride is not preferred because it increases the formation of triazine. Up to about 5 wt% catalyst can be used, based on the weight of the benzotrihalide, and the preferred amount of catalyst is about 100 ppm to about 1 wt% as less has little effect and more may cause the reaction to be too fast to control. The reaction is performed by simply mixing together the benzotrihalide or substituted benzotrihalide, the ammonium halide, the initiator, and the catalyst if one is used. The reactants are heated to a temperature of 150 to 250°C as at lower temperatures the reaction rate is too slow and at higher temperatures byproducts and tar may form; the preferred temperature range is 180 to 230°C. The desired nitrile product has the general formula: The nitrile product can be recovered from the reaction mixture by distillation. The following examples further illustrates this invention. EXAMPLE 1 OCBTC (230 g, 1.0 mol), ammonium chloride (59 g, 1.10 eq), and OCBA (15.7 g) were added to a 500 mL reactor equipped with thermocouple, overhead stirrer, and reflux condenser. The reaction mixture was stirred, heated up to 225°C, and maintained at that temperature while the reaction was periodically followed by gas chromatography (GC). After a reaction time of about 8 h, OCBN (121.5 g, 88.4%) was obtained by distillation (melting point: 45-46°C). EXAMPLE 2 The reaction was carried out as described in Example 1. PCBTC (230 g, 1.0 mol), ammonium chloride (56.2 g, 1.05 eq), and p-chlorobenzoic acid (11.5 g) were charged to the reactor. The mixture was heated at 215°C for 9 h. Distillation of the reaction mixture gave PCBN (122.4g, 89%, melting point: 92-93°C). EXAMPLE 3 The reaction was performed as in Example 1. The following reactants were charged to the reactor: 2,4-DCBTC (132.8 g, 0.5 mol), ammonium chloride (28.1 g, 1.05 eq), and 2,4-dichlorobenzoyl chloride (13.3 g). The mixture was heated at 230°C for 14 h. Distillation of the reaction mixture gave pure 2,4-dichlorobenzonitrile (2,4-DCBN) (76.4 g, 89% yield, melting point: 59-60°C). EXAMPLE 4 The reaction was carried out as described in Example 1. BTC (195.5 g, 1.0 mol), ammonium chloride (56.1 g, 1.05 eq), and benzoyl chloride (20 g) were charged to the reactor. The mixture was heated at 190°C for 15 h. The GC yield of BN was 92.3%. EXAMPLE 5 Example 1 was repeated using OCBTC (230 g, 1.0 mol), ammonium chloride (59 g, 1.10 eq), and water (4.6 g, 2%). The mixture was heated up to 215°C. Most of water was distilled off from the reactor. The reaction mixture was then maintained at 215°C for 22 h. Distillation of the reaction mixture gave pure OCBN (125.2 g, 91%). EXAMPLE 6 The reaction was performed as in Example 1 except that the following reactants were charged to the reactor: OCBTC (230 g, 1.0 mol), ammonium chloride (59 g, 1.10 eq), and o-chlorobenzoyl chloride (35 g). The mixture was heated at 225°C for 10 h. The GC yield of OCBN was 89.6%. EXAMPLE 7 The reaction was carried out as in Example 1. The following reactants were charged to the reactor: OCBTC (90 g, 0.39 mol), ammonium chloride (23 g, 1.10 eq), and o-chlorobenzamide (9 g). The mixture was heated at 225°C for 11 h. The GC yield of OCBN was 92.4%. EXAMPLE 8 The reaction was performed as in Example 1. OCBTC (230 g, 1.0 mol), ammonium chloride (59 g, 1.10 eq), OCBA (15.6 g), and zinc acetate (460 mg, 0.2%) were charged to the reactor. The mixture was heated at 225°C for 5 h. The GC yield of OCBN was 90.5%. EXAMPLE 9 The reaction was carried out as in Example 1. The following reactants were charged to the reactor: OCBTC (233.5 g, 1.02 mol), ammonium chloride (54.8 g, 1.0 eq), OCBA (13.87 g), and anhydrous ferric chloride (70.9 mg, 300 ppm). The mixture was heated at 215°C for 5 h. The GC yield of OCBN was 85.1%. EXAMPLE 10 OCBTC (406 G, 1.76 mol) and OCBA (32.75 g, 0.21 mol) were added to a 500 mL flask equipped with a thermocouple, overhead stirrer, reflux condenser, and NH 3 blow tube. The reaction mixture was heated to 225°C and the flow of NH 3 (70-100 mUmin) was started through the blow tube, forming NH 4 Cl in situ. After 8 hours, GC indicated that all the OCBTC had reacted. The reaction mixture was distilled, obtaining 224 g of OCBN (95% by GC, mp 45°C).

Claims: A method of making an aromatic nitrile having the general formula comprising (A) preparing a mixture which comprises (1) a benzotrihalide having the general formula where X is halogen, R is halogen or aliphatic from C 1 to C 8 or aromatic from C 6 to C 8 , and n is 0 to 5; (2) an ammonium halide in an amount within 50 mole% of stoichiometric with said benzotrihalide; (3) 0.001 to 0.25 equivalents of an initiator comprising an acid halide, or an optionally substituted benzoic acid, benzamide, benzoic acid anhydride or benzoic acid chloride; and (B) heating said mixture at 150 to 250°C. A method according to Claim 1 wherein n is 0 to 4. A method according to Claim 2 wherein n is 0 to 3. A method according to Claim 3 wherein n is 0 to 2. A method according to Claim 4 wherein n is 0 to 1. A method according to Claim 1 wherein (1) said benzotrihalide has the general formula; where n is 1 to 3; and (2) said ammonium halide is present in an amount within 20% of stoichiometric with said benzotrihalide A method according to any one of the preceding Claims where X is chlorine or bromine. A method according to any one of the preceding Claims including the additional last step of recovering said aromatic nitrile from said mixture by distillation. A method according to any one of the preceding Claims wherein said benzotrihalide is benzotrichloride. A method according to any one of the preceding Claims wherein said ammonium halide is ammonium chloride. A method according to any one of the preceding Claims wherein said ammonium halide is formed in situ by the addition of gaseous ammonia to said mixture. A method according to any one of the preceding Claims wherein said initiator is the acid, acid chloride, or amide that corresponds to said aromatic nitrile. A method according to Claim 1 wherein (1) said benzotrihalide comprises chlorobenzotrichloride having the general formula; where n is 1 to 3; (2) said ammonium chloride is present in an amount between stoichiometric and up to 5 mole % in excess of stoichiometric with said chlorobenzotrichloride; (3) said initiator is present in an amount from 0.02 to 0.15 equivalents and is the acid, acid chloride or amide that corresponds to said aromatic nitrile, which reacts with said chlorobenzotrichloride and said ammonium chloride to form said aromatic nitrile; and; (B) the mixture is heated at 180 to 230°C, and (C) said aromatic nitrile is recovered from said mixture by distillation A method according to any one of the preceding Claims wherein said benzotrihalide is orthochlorobenzotrichloride. A method according to any one of Claims 1 to 13 wherein said benzotrihalide is parachlorobenzotrichloride. A method according to any one of Claims 1 to 13 wherein said benzotrihalide is 3,4-dichlorobenzotrichloride. A method according to any one of the preceding Claims wherein the initiator is incorporated in the mixture of benzotrihalide and ammonium halide, or ammonium chloride by admixing the initiator into the mixture. A method according to any one of Claims 1 to 16 wherein said initiator is an acid chloride that is formed in situ by the reaction of water with said benzotrihalide. A method according to any one of the preceding Claims wherein the mixture comprises up to 5 wt% of a metal oxide or metal salt catalyst. A method according to Claim 19 wherein the amount of said catalyst is 100 ppm to 1 wt%, A method according to Claim 19 or 20 wherein the metal of said catalyst is zinc or copper. A method according to Claim 20 wherein the catalyst is zinc chloride or copper chloride.

Inventors: HAUSLADEN MICHAEL C, HUANG BAO-GUO, TANG DAVID Y, HAUSLADEN, MICHAEL C., HUANG, BAO-GUO, TANG, DAVID Y.
Applicants: AMERICAN WRECKING CORP OF NEW, SECO AMERICAN CORP, AMERICAN WRECKING CORPORATION OF NEW JERSEY, SECO AMERICAN CORPORATION
Application year: 1998
Main classification: C07C253
IPC codes: C07C255, C07C253