CA1304749C - Process for the co-production of aromatic carboxylates and alkyl iodides - Google Patents
Process for the co-production of aromatic carboxylates and alkyl iodidesInfo
- Publication number
- CA1304749C CA1304749C CA000580594A CA580594A CA1304749C CA 1304749 C CA1304749 C CA 1304749C CA 000580594 A CA000580594 A CA 000580594A CA 580594 A CA580594 A CA 580594A CA 1304749 C CA1304749 C CA 1304749C
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- aromatic
- ether
- carbonylation
- iodides
- pressure
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Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/02—Esters of acyclic saturated monocarboxylic acids having the carboxyl group bound to an acyclic carbon atom or to hydrogen
- C07C69/04—Formic acid esters
- C07C69/06—Formic acid esters of monohydroxylic compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C19/00—Acyclic saturated compounds containing halogen atoms
- C07C19/07—Acyclic saturated compounds containing halogen atoms containing iodine
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/76—Esters of carboxylic acids having a carboxyl group bound to a carbon atom of a six-membered aromatic ring
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- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Abstract PROCESS FOR THE CO-PRODUCTION OF AROMATIC
CARBOXYLATES AND ALKYL IODIDES
Disclosed is a process for the co-production of aromatic carboxylic esters and alkyl iodides by the carbonylation of aromatic iodides in the presence of an ether and a nickel catalyst.
CARBOXYLATES AND ALKYL IODIDES
Disclosed is a process for the co-production of aromatic carboxylic esters and alkyl iodides by the carbonylation of aromatic iodides in the presence of an ether and a nickel catalyst.
Description
~ ~304749 PROCE~S FOR THE CO-PRODUCTION OF
AROMATIC CARBOXYLATE AND ALKYL IODIDES
This invention relates to a novel carbonylation process for the preparation of both aromatic carboxylic esters and an iodine containing compound from which the iodine values can be economically recovered. The carbonylation is conducted in the presence of an ether and a catalytic amount of nickel.
The carbonylation of aromatic halides in the presence of nickel to obtain aromatic carboxylic acids and esters is well known in the art. Nakayama and Mizoroki (Bull. Chem. Soc. Japan 42 (1969) 1124) disclose the carbonylation of aromatic halides in the presence of an alcohol and a potassium acetate to produce the corresponding carboxylic acid ester.
While it is known that aromatic iodides can be carbonylated, the use of these materials has been discouraged by the cost associated with the difficulty of recovering the iodine values. For example, the use of basic materials in the carbonylation of aromatic halides, such as potassium acetate by Nakayama and Mizoroki, results in the formation of halide salts from which the halide values can be reclaimed only through uneconomical procedures involving severe chemical treatments.
In U.S. Patent 2,565,462, Prichard and Tabet disclose the carbonylation of aromatic halides to aromatic carboxylic esters in the presence of alcohols, ethers, and phenols using nickel tetracarbonyl. However, only noncatalytic quantities of iron, nickel, and cobalt are used as promoters under reaction conditions of both temperature and 130~749 pressure that are much more severe than is shown by our invention.
When alcohols are employed in reactions under typical carbonylation reaction conditions for aryl S halides, water is a byproduct. ~ater can be formed in a number of different ways. For example, reaction of in situ generated hydrogen iodide with methanol results in the formation of methyl iodide and water. Alcohols can often dehydrate to their corresponding ether and water under typical carbonylation reaction conditions.
The presence of water in the reaction mixture often leads to the production of a mixture of both carboxylic acids and esters. The presence of acid groups can present a purification problem if pure ester is desired lS as a polymer precursor.
We have discovered a process which not only results in the carbonylation of aromatic iodides to aromatic carboxylic esters with low acid content in excellent yields and at excellent rates of conversion but also results in production of alkyl iodides from which the iodine values can be economically recovered.
In this invention, the carbonylation is conducted in the presence of an ether and a carboxylic amount of a nickle catalyst under aromatic carboxylic ester and alkyl iodide-forming conditions of temperature and pressure.
The advantage afforded by our invention over the prior art is two-fold. First, the iodine values in the alkyl iodide may be readily recovered by simply flashing the relatively volatile alkyl iodide from the mixture resulting from the carbonylation reaction.
This can be accomplished either in the ~';
~30~749 carbonylation reactor or, more preferably, in a pressure reduction vessel to which the mixture resulting from the carbonyl~tion reaction is fed.
Second, the object in feeding organic ethers is to minimize the amount of water in the carbonylation reactor which will reduce the acid content of the ester product. The ratio of aromatic acids to esters produced in the present invention is dependent on the concentration of water present in the carbonylation reactor. The capability of producing aromatic carboxylic esters with low acid content is both novel and useful. The low acid content allows for simpler and less expensive production and purification schemes and eliminates the need for an e~terification step when esters are the desired product.
The aromatic iodides which msy be used in our process may be monoiodo or polyiodo e.g., di-, tri-and tetra-iodo aromatic compounds. The aromatic nucleus or moiety can contain from 6 to 18 carbon atoms, preferably 6 to 10 carbon atoms and may be carbocyclic aromatic such as benzene, biphenyl, terphenyl, naphthalene, anthracene, etc., or heterocyclic aromatic such as pyridine, thiophene, pyrrole, indole, etc. In addition to one or more iodine atoms, the aromatic moiety may be substituted by various substituents substantially inert under the conditions employed in our process. Examples of such substituents include alkyl of up to 12 carbon atoms such as methyl, ethyl, isobutyl, hexyl, 2-ethylhexyl, nonyl, decyl, dodecyl, etc.: cycloalkyl of 5 to 12 carbon atoms such as cyclopentyl, cyclohexyl, 4-butylcyclohexyl, etc.; halogen such as chloro and bromo; alkoxycarbonyl of from 2 to 8 carbon atoms such as methoxycarbonyl, ethoxycarbonyl, butoxycarbonyl, hexyloxycarbonyl, etc.; carboxyl;
cyano; alkenyl of 2 to 12 carbon atoms such as vinyl allyl, etc.; formyl; alkanoyl of 2 to 8 carbon atoms such as acetyl, propionyl, butyryl, hexanoyl, etc.;
alkanoylamido of 2 to 8 carbon atoms such as acetamido butylamido, etc.; aroylamino such as benzamido; and alkylsulfonamide such as methanesulfonamide hexanesulfonamide, etc.
Specific examples of the aromatic iodide reactants include iodobenzene, 1,3- and 1,4-diiodobenzene 1,3,5-triiodobenzene, 4-iodotoluene, 4-iodophenol, 4-iodoanisole, 4-iodoacetophenone, 4,4'-diiodobiphenyl, 4-chloroiodobenzene, 3-bromoiodobenzene and 2,6- and 2,7-diiodonaphthalene. Our process is particularly useful for the preparation of benzenedicarboxylic and naphthalenedicarboxylic esters with low acid content and thus the preferred reactants are diiodobenzenes, especially 1,3- and 1,4-diiodobenzenel and diiodonaphthalenes, especially 2,6- and 2,7-diiodonaphthalene.
The aromatic iodide reactants are known compounds and/or can be prepared according to published procedures. For example, T. Hudlicky et.al. The Chemistry of Halides. Pseudohalides and Azides, Supplement D, Part 2, 1142-1158, discloses a number of such processes. Another process described in J. Chem.
Soc. 150 (1952) comprises treating an aromatic compound, such as benzene, ~ith iodine in the presence of silver sulfate dissolved in concentrated sulfuric acid.
The ether used in the process of this invention, which is preferably dimethyl ether, results in the formation of methyl carboxylate esters, which may be used in transesterification reactions, and produces ~`~J
~304749 methyl iodide which is the most volatile of the alkyl iodides. However, other ethers containing up to 12 carbon atoms, preferably up to 4 carbon atoms, may be employed if desired. Examples of other suitable ethers include diethyl ether, dipropyl ether, dibutyl ether, dipentyl ether, dihexyl ether, diheptyl ethert dioctyl ether, didecyl ether, dibenzyl ether, dioxane, anisole, or mixed dialkyl ethers. Mixture of these ethers may also be employed. For each mole equivalent of aromatic ester produced, one mole of ether is required.
The process provided by our invention can also be carried out in the presence of an organic co-solvent such as aliphatic, alicyclic and aromatic hydrocarbons, and halogenated hydrocarbons. Examples of such solvents include benzene, toluene, the xylenes, hexane, heptane, chlorobenzene, ethylene dichloride, methychloroform, naphthalene, etc.
However, the use of a co-solvent is not critical to the practice of this invention. Water or potential esterifying agents such as alcohols and their carboxylate esters may also be present in the reaction mixture depending upon the desired ester to acid ratio.
The nickel catalyst can be provided to the reaction medium as either nickel metal or as a number of nickel salts or complexes. Illustrative sources of nickel are nickel acetate, nickel chloride, nickel bromide, nickel iodide, nickel carbonate, nickel hydroxide, nickel oxide, nickel acetylacetonate, nickel tetracarbonyl and its phosphine and halogen substituted analogs. The amount of nickel is not significant as long as enough is present to catalyze the reaction. Preferably, the catalyst is present in a concentration of 10 to 0.001 mole percent, preferably 2.5 to 0.1 mole percent based on the moles ~3~4749 of aromatic iodide reactant. Therefore, the total reaction medium has a catalyst concentration of 10,000 ppm to l ppm with preferred catalyst concentrations o~ 2,500 to 100 ppm.
The carbonylation reaction i5 conducted in the presence of carbon monoxide, which is employed in amounts such that the total reaction pressure is suitable ~or the formation of both the aromatic carboxylic ester and the alkyl iodide. The carbon monoxide employed may be essentially pure or it may contain other gases such as carbon dioxide, hydrogen, methane and other compounds produced by synthesis gas plants. Normally, the carbon monoxide will be at least 90, preferably at least 95, percent pure.
The process of the present invention can be conducted at temperatures and pressures suitable for formation of both the aromatic carboxylic ester and alkyl iodide. The temperatures and pressures are interdependent and can vary considerably. Normally, the pressure will be at least 7 kg/cm2. While the process can be carried out at pressures as high as 700 kg/cm2, the cost of utilities and equipment required for such high pressure operation may not be commercially ~ustified. Thus, the pressure normally w~ll be in the range of 9 to 280 kg/cm , preferably 21 to 105 kg/cm . A particularly preferred pressure is 52 to 105 kg/cm . A pressure of 84 kg/cm is often most desirable. While temperature as low as 125C and higher than 225C may be used, our process normally is carried out between 150 and 275C. The preferred temperature range is 180 to 250C. A particularly preferred temperature is 220C.
The relative amounts of cArbon monoxide, ether and aromatic iodide and in our process can be varied substantially and are, in general, not critical.
~304749 However, it is preferable to have at least stoichiometric amounts present relative to the aromatic iodide if complete conversion is desired.
When a polyiodo aromatic compound is used as the reactant in our carbonylation process, the products obtained include both aromatic polycarboxylic esters and partially carbonylated products such as iodoaromatic carboxylic esters. The latter compounds are useful as intermediates in the preparation of derivatives of aromatic carboxylic esters, for example, by displacement reactions whereby the iodo substituent is replaced with other radicals. The difunctional esters, such as dimethyl 2,6-naphthalenedicarboxylate, can be reacted with diols to produce high molecular weight polyesters suitable for molding plastics. Useful articles can be molded from these plastics, such as by in~ection molding. The relative amounts of partially or totally carbonylated products is highly dependent on the period of time that the reactant resides under carbonylation conditions.
The alkyl iodides prepared according to the process of our invention may be uQed in other chemical processes such 8S in the preparation of carboxylic acids and carboxylic anhydrides according to known carbonylation procedures. Alternatively, the alkyl iodide can be oxidatively decomposed at elevated temperature to produce a gaseous mixture of iodine, carbon dioxide, and water from which the iodine can be recovered. Alternatively, the alkyl iodides may be thermally decomposed to iodine and an alkane, or hydrogenated to hydrogen iodide and methane.
Our process is carried out at a pKa of less than 5. Therefore, there are no significant amounts of basic materials which preferentially combine with hydroqen iodide and interface with the formation of an alkyl iodide. Examples of such bases which are not present in significant amounts in our process include amines, particularly tertiary amines, and hydroxides, alkoxides and weak acid salts, e.g., carboxylates of the alkali and alkaline earth metals.
Our invention is further illustrated by the following examples. In the procedures utilized in the examples the materials employed are loaded into a 330 mL autoclave constructed of Hastelloy B2 (trademark) alloy which is designed to operate in a rocking mode.
The autoclave is pressurized with 14 kg~cm2 carbon monoxide gas pressure at room temperature and then the gas is vented and the autoclave is sealed. In Examples 1-8, the autoclave is pressurized to 14 kg~c* with carbon monoxide gas at ambient temperature and heated and rocked until reaction temperature was reached, at which time additional carbon monoxide qas is added to increase the autoclave internal pressure to the predetermined value. Reactor pressure is maintained by adding carbon monoxide at the same rate at which it is consumed by the reactants. The carbon monoxide used is essentially pure. When the predetermined reaction time is completed, the autoclave is cooled by a stream of cold air to approximately 25C. After the gas is vented from the autoclave the crude product is isolated by filtration and analyzed by gas chromatographic methods. The % conversion is the mole percent of iodo-group converted to carboxylic acid or ester. The results are shown below.
~ .
~ i.
ExamPle No. 1 2 Iodoaromatic 2,6-diiodonaph-2,6-diiodonaph-Wt (g~ thalene thslene 30.0 30.0 5Catalyst NiI2-6H20 NiI2-6H20 Wt (g) 0.38 0.38 Ether Dimethyl EtherDimethyl Ether Vol (mL) 40.0 40.0 Co-Solvent Naphthalenel-Methylnaph-10Wt (g) 100.0 thalene 99.8 Time 2 (hour) Pressure 105 105 (kg/cm2) Temp. (C) 220 190 % Conversion 100 47.4 ExamPle No. 3 4 20Iodoaromatic 2,6-diiodonaph-2,6-diiodonaph-Wt (g) thalene thalene 30.0 30.0 Catalyst NiI2-6H20 NiI2-6H20 Wt (g) 0.38 0.38 Ether Dimethyl EtherDimethyl Ether 25Vol (mL) 40.0 40.0 Co-Solvent 1-Methylnaph-1-Methylnaph-Wt (g) thalene thalene 100.2 99.9 Time 30(hour) Pressure 105 105 ( kg/cm2 ) Temp. (C~ 205 245 % Conversion 85.3 96.1 ~304749 Example No. 5 6 Iodoaromatic 2,6-diiodonaph-2,6-diiodonaph-Wt (g) thalene thalene 30.0 30.0 5Catalyst NiI2-6H2O NiI2-6H20 Wt ~g) 0.38 0.38 Ether Dimethyl EtherDimethyl Ether Vol (mL) 40.0 40.0 Co-Solvent 1-Methylnaph-1-Methylnaph-10Wt (g) thalene thalene lOO.Q 100.2 Time (hour) Pressure 70 52.5 15(kg/cm2) Temp. (C) 220 220 % Conversion 83.6 67.4 ExamPle No. 7 8 Iodoaromatic 2,6-diiodonaph-2,6-di1odonaph-20Wt (g) thalene thalene 30.0 30.0 Catalyst NiI2-6H20 NiI2-6H20 Wt (g) 0.38 0.38 Ether Diethyl EtherAnisole 25Vol (mL~ 40.0 40.0 Co-Solvent l-Methylnaph-l-Methylnaph-W~ (g) thalene thalene 100.2 99.7 Time 30(hour) Pressure 105 105 ~kglcm2) Temp. (C) 220 220 % Conversion 96.2 33.4 ~304749 While the invention has been described in detail with particular reference to preferred embodiments thereof, 1t will be understood that variations and modifications can be effected within the spirit and scope of the invention.
AROMATIC CARBOXYLATE AND ALKYL IODIDES
This invention relates to a novel carbonylation process for the preparation of both aromatic carboxylic esters and an iodine containing compound from which the iodine values can be economically recovered. The carbonylation is conducted in the presence of an ether and a catalytic amount of nickel.
The carbonylation of aromatic halides in the presence of nickel to obtain aromatic carboxylic acids and esters is well known in the art. Nakayama and Mizoroki (Bull. Chem. Soc. Japan 42 (1969) 1124) disclose the carbonylation of aromatic halides in the presence of an alcohol and a potassium acetate to produce the corresponding carboxylic acid ester.
While it is known that aromatic iodides can be carbonylated, the use of these materials has been discouraged by the cost associated with the difficulty of recovering the iodine values. For example, the use of basic materials in the carbonylation of aromatic halides, such as potassium acetate by Nakayama and Mizoroki, results in the formation of halide salts from which the halide values can be reclaimed only through uneconomical procedures involving severe chemical treatments.
In U.S. Patent 2,565,462, Prichard and Tabet disclose the carbonylation of aromatic halides to aromatic carboxylic esters in the presence of alcohols, ethers, and phenols using nickel tetracarbonyl. However, only noncatalytic quantities of iron, nickel, and cobalt are used as promoters under reaction conditions of both temperature and 130~749 pressure that are much more severe than is shown by our invention.
When alcohols are employed in reactions under typical carbonylation reaction conditions for aryl S halides, water is a byproduct. ~ater can be formed in a number of different ways. For example, reaction of in situ generated hydrogen iodide with methanol results in the formation of methyl iodide and water. Alcohols can often dehydrate to their corresponding ether and water under typical carbonylation reaction conditions.
The presence of water in the reaction mixture often leads to the production of a mixture of both carboxylic acids and esters. The presence of acid groups can present a purification problem if pure ester is desired lS as a polymer precursor.
We have discovered a process which not only results in the carbonylation of aromatic iodides to aromatic carboxylic esters with low acid content in excellent yields and at excellent rates of conversion but also results in production of alkyl iodides from which the iodine values can be economically recovered.
In this invention, the carbonylation is conducted in the presence of an ether and a carboxylic amount of a nickle catalyst under aromatic carboxylic ester and alkyl iodide-forming conditions of temperature and pressure.
The advantage afforded by our invention over the prior art is two-fold. First, the iodine values in the alkyl iodide may be readily recovered by simply flashing the relatively volatile alkyl iodide from the mixture resulting from the carbonylation reaction.
This can be accomplished either in the ~';
~30~749 carbonylation reactor or, more preferably, in a pressure reduction vessel to which the mixture resulting from the carbonyl~tion reaction is fed.
Second, the object in feeding organic ethers is to minimize the amount of water in the carbonylation reactor which will reduce the acid content of the ester product. The ratio of aromatic acids to esters produced in the present invention is dependent on the concentration of water present in the carbonylation reactor. The capability of producing aromatic carboxylic esters with low acid content is both novel and useful. The low acid content allows for simpler and less expensive production and purification schemes and eliminates the need for an e~terification step when esters are the desired product.
The aromatic iodides which msy be used in our process may be monoiodo or polyiodo e.g., di-, tri-and tetra-iodo aromatic compounds. The aromatic nucleus or moiety can contain from 6 to 18 carbon atoms, preferably 6 to 10 carbon atoms and may be carbocyclic aromatic such as benzene, biphenyl, terphenyl, naphthalene, anthracene, etc., or heterocyclic aromatic such as pyridine, thiophene, pyrrole, indole, etc. In addition to one or more iodine atoms, the aromatic moiety may be substituted by various substituents substantially inert under the conditions employed in our process. Examples of such substituents include alkyl of up to 12 carbon atoms such as methyl, ethyl, isobutyl, hexyl, 2-ethylhexyl, nonyl, decyl, dodecyl, etc.: cycloalkyl of 5 to 12 carbon atoms such as cyclopentyl, cyclohexyl, 4-butylcyclohexyl, etc.; halogen such as chloro and bromo; alkoxycarbonyl of from 2 to 8 carbon atoms such as methoxycarbonyl, ethoxycarbonyl, butoxycarbonyl, hexyloxycarbonyl, etc.; carboxyl;
cyano; alkenyl of 2 to 12 carbon atoms such as vinyl allyl, etc.; formyl; alkanoyl of 2 to 8 carbon atoms such as acetyl, propionyl, butyryl, hexanoyl, etc.;
alkanoylamido of 2 to 8 carbon atoms such as acetamido butylamido, etc.; aroylamino such as benzamido; and alkylsulfonamide such as methanesulfonamide hexanesulfonamide, etc.
Specific examples of the aromatic iodide reactants include iodobenzene, 1,3- and 1,4-diiodobenzene 1,3,5-triiodobenzene, 4-iodotoluene, 4-iodophenol, 4-iodoanisole, 4-iodoacetophenone, 4,4'-diiodobiphenyl, 4-chloroiodobenzene, 3-bromoiodobenzene and 2,6- and 2,7-diiodonaphthalene. Our process is particularly useful for the preparation of benzenedicarboxylic and naphthalenedicarboxylic esters with low acid content and thus the preferred reactants are diiodobenzenes, especially 1,3- and 1,4-diiodobenzenel and diiodonaphthalenes, especially 2,6- and 2,7-diiodonaphthalene.
The aromatic iodide reactants are known compounds and/or can be prepared according to published procedures. For example, T. Hudlicky et.al. The Chemistry of Halides. Pseudohalides and Azides, Supplement D, Part 2, 1142-1158, discloses a number of such processes. Another process described in J. Chem.
Soc. 150 (1952) comprises treating an aromatic compound, such as benzene, ~ith iodine in the presence of silver sulfate dissolved in concentrated sulfuric acid.
The ether used in the process of this invention, which is preferably dimethyl ether, results in the formation of methyl carboxylate esters, which may be used in transesterification reactions, and produces ~`~J
~304749 methyl iodide which is the most volatile of the alkyl iodides. However, other ethers containing up to 12 carbon atoms, preferably up to 4 carbon atoms, may be employed if desired. Examples of other suitable ethers include diethyl ether, dipropyl ether, dibutyl ether, dipentyl ether, dihexyl ether, diheptyl ethert dioctyl ether, didecyl ether, dibenzyl ether, dioxane, anisole, or mixed dialkyl ethers. Mixture of these ethers may also be employed. For each mole equivalent of aromatic ester produced, one mole of ether is required.
The process provided by our invention can also be carried out in the presence of an organic co-solvent such as aliphatic, alicyclic and aromatic hydrocarbons, and halogenated hydrocarbons. Examples of such solvents include benzene, toluene, the xylenes, hexane, heptane, chlorobenzene, ethylene dichloride, methychloroform, naphthalene, etc.
However, the use of a co-solvent is not critical to the practice of this invention. Water or potential esterifying agents such as alcohols and their carboxylate esters may also be present in the reaction mixture depending upon the desired ester to acid ratio.
The nickel catalyst can be provided to the reaction medium as either nickel metal or as a number of nickel salts or complexes. Illustrative sources of nickel are nickel acetate, nickel chloride, nickel bromide, nickel iodide, nickel carbonate, nickel hydroxide, nickel oxide, nickel acetylacetonate, nickel tetracarbonyl and its phosphine and halogen substituted analogs. The amount of nickel is not significant as long as enough is present to catalyze the reaction. Preferably, the catalyst is present in a concentration of 10 to 0.001 mole percent, preferably 2.5 to 0.1 mole percent based on the moles ~3~4749 of aromatic iodide reactant. Therefore, the total reaction medium has a catalyst concentration of 10,000 ppm to l ppm with preferred catalyst concentrations o~ 2,500 to 100 ppm.
The carbonylation reaction i5 conducted in the presence of carbon monoxide, which is employed in amounts such that the total reaction pressure is suitable ~or the formation of both the aromatic carboxylic ester and the alkyl iodide. The carbon monoxide employed may be essentially pure or it may contain other gases such as carbon dioxide, hydrogen, methane and other compounds produced by synthesis gas plants. Normally, the carbon monoxide will be at least 90, preferably at least 95, percent pure.
The process of the present invention can be conducted at temperatures and pressures suitable for formation of both the aromatic carboxylic ester and alkyl iodide. The temperatures and pressures are interdependent and can vary considerably. Normally, the pressure will be at least 7 kg/cm2. While the process can be carried out at pressures as high as 700 kg/cm2, the cost of utilities and equipment required for such high pressure operation may not be commercially ~ustified. Thus, the pressure normally w~ll be in the range of 9 to 280 kg/cm , preferably 21 to 105 kg/cm . A particularly preferred pressure is 52 to 105 kg/cm . A pressure of 84 kg/cm is often most desirable. While temperature as low as 125C and higher than 225C may be used, our process normally is carried out between 150 and 275C. The preferred temperature range is 180 to 250C. A particularly preferred temperature is 220C.
The relative amounts of cArbon monoxide, ether and aromatic iodide and in our process can be varied substantially and are, in general, not critical.
~304749 However, it is preferable to have at least stoichiometric amounts present relative to the aromatic iodide if complete conversion is desired.
When a polyiodo aromatic compound is used as the reactant in our carbonylation process, the products obtained include both aromatic polycarboxylic esters and partially carbonylated products such as iodoaromatic carboxylic esters. The latter compounds are useful as intermediates in the preparation of derivatives of aromatic carboxylic esters, for example, by displacement reactions whereby the iodo substituent is replaced with other radicals. The difunctional esters, such as dimethyl 2,6-naphthalenedicarboxylate, can be reacted with diols to produce high molecular weight polyesters suitable for molding plastics. Useful articles can be molded from these plastics, such as by in~ection molding. The relative amounts of partially or totally carbonylated products is highly dependent on the period of time that the reactant resides under carbonylation conditions.
The alkyl iodides prepared according to the process of our invention may be uQed in other chemical processes such 8S in the preparation of carboxylic acids and carboxylic anhydrides according to known carbonylation procedures. Alternatively, the alkyl iodide can be oxidatively decomposed at elevated temperature to produce a gaseous mixture of iodine, carbon dioxide, and water from which the iodine can be recovered. Alternatively, the alkyl iodides may be thermally decomposed to iodine and an alkane, or hydrogenated to hydrogen iodide and methane.
Our process is carried out at a pKa of less than 5. Therefore, there are no significant amounts of basic materials which preferentially combine with hydroqen iodide and interface with the formation of an alkyl iodide. Examples of such bases which are not present in significant amounts in our process include amines, particularly tertiary amines, and hydroxides, alkoxides and weak acid salts, e.g., carboxylates of the alkali and alkaline earth metals.
Our invention is further illustrated by the following examples. In the procedures utilized in the examples the materials employed are loaded into a 330 mL autoclave constructed of Hastelloy B2 (trademark) alloy which is designed to operate in a rocking mode.
The autoclave is pressurized with 14 kg~cm2 carbon monoxide gas pressure at room temperature and then the gas is vented and the autoclave is sealed. In Examples 1-8, the autoclave is pressurized to 14 kg~c* with carbon monoxide gas at ambient temperature and heated and rocked until reaction temperature was reached, at which time additional carbon monoxide qas is added to increase the autoclave internal pressure to the predetermined value. Reactor pressure is maintained by adding carbon monoxide at the same rate at which it is consumed by the reactants. The carbon monoxide used is essentially pure. When the predetermined reaction time is completed, the autoclave is cooled by a stream of cold air to approximately 25C. After the gas is vented from the autoclave the crude product is isolated by filtration and analyzed by gas chromatographic methods. The % conversion is the mole percent of iodo-group converted to carboxylic acid or ester. The results are shown below.
~ .
~ i.
ExamPle No. 1 2 Iodoaromatic 2,6-diiodonaph-2,6-diiodonaph-Wt (g~ thalene thslene 30.0 30.0 5Catalyst NiI2-6H20 NiI2-6H20 Wt (g) 0.38 0.38 Ether Dimethyl EtherDimethyl Ether Vol (mL) 40.0 40.0 Co-Solvent Naphthalenel-Methylnaph-10Wt (g) 100.0 thalene 99.8 Time 2 (hour) Pressure 105 105 (kg/cm2) Temp. (C) 220 190 % Conversion 100 47.4 ExamPle No. 3 4 20Iodoaromatic 2,6-diiodonaph-2,6-diiodonaph-Wt (g) thalene thalene 30.0 30.0 Catalyst NiI2-6H20 NiI2-6H20 Wt (g) 0.38 0.38 Ether Dimethyl EtherDimethyl Ether 25Vol (mL) 40.0 40.0 Co-Solvent 1-Methylnaph-1-Methylnaph-Wt (g) thalene thalene 100.2 99.9 Time 30(hour) Pressure 105 105 ( kg/cm2 ) Temp. (C~ 205 245 % Conversion 85.3 96.1 ~304749 Example No. 5 6 Iodoaromatic 2,6-diiodonaph-2,6-diiodonaph-Wt (g) thalene thalene 30.0 30.0 5Catalyst NiI2-6H2O NiI2-6H20 Wt ~g) 0.38 0.38 Ether Dimethyl EtherDimethyl Ether Vol (mL) 40.0 40.0 Co-Solvent 1-Methylnaph-1-Methylnaph-10Wt (g) thalene thalene lOO.Q 100.2 Time (hour) Pressure 70 52.5 15(kg/cm2) Temp. (C) 220 220 % Conversion 83.6 67.4 ExamPle No. 7 8 Iodoaromatic 2,6-diiodonaph-2,6-di1odonaph-20Wt (g) thalene thalene 30.0 30.0 Catalyst NiI2-6H20 NiI2-6H20 Wt (g) 0.38 0.38 Ether Diethyl EtherAnisole 25Vol (mL~ 40.0 40.0 Co-Solvent l-Methylnaph-l-Methylnaph-W~ (g) thalene thalene 100.2 99.7 Time 30(hour) Pressure 105 105 ~kglcm2) Temp. (C) 220 220 % Conversion 96.2 33.4 ~304749 While the invention has been described in detail with particular reference to preferred embodiments thereof, 1t will be understood that variations and modifications can be effected within the spirit and scope of the invention.
Claims (8)
1. A process for the co-production of aromatic carboxylic esters and alkyl iodides which comprises carboxylating aromatic iodides using carbon monoxide in the presence of an ether containing up to 12 carbon atoms and a catalytic amount of a nickel catalyst wherein the temperature is in the range of 150° to 275°C and the pressure is in the range of 9 to 280 kg/cm2.
2. The process of Claim 1 wherein the aromatic iodides are selected from diiodonaphthalene and diiodobenzenes.
3. The process of Claim 2 wherein the diiodonaphthalene is 2,6-diiodonaphthalene and the diiodobenzene is 1,4-diiodobenzene.
4. The process of Claim 1 wherein the ether contains from 1 to 4 carbon atoms.
5. The process of Claim 4 wherein the ether is dimethyl ether.
6. The process of Claim 6 wherein the temperature is in the range of 180° to 250°C.
7. The process of Claim 1 wherein the pressure is in the range of 21 to 105 kg/cm2.
8. The process of Claim 1 wherein the process is carried out in the presence of an organic co-solvent.
d53560/amdtca2/mlt
d53560/amdtca2/mlt
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US11529587A | 1987-11-02 | 1987-11-02 | |
| US115,295 | 1987-11-02 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1304749C true CA1304749C (en) | 1992-07-07 |
Family
ID=22360441
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000580594A Expired - Fee Related CA1304749C (en) | 1987-11-02 | 1988-10-19 | Process for the co-production of aromatic carboxylates and alkyl iodides |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP0409834A1 (en) |
| JP (1) | JPH03500779A (en) |
| KR (1) | KR890701535A (en) |
| CA (1) | CA1304749C (en) |
| WO (1) | WO1989004296A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9938217B2 (en) | 2016-07-01 | 2018-04-10 | Res Usa, Llc | Fluidized bed membrane reactor |
| US9981896B2 (en) | 2016-07-01 | 2018-05-29 | Res Usa, Llc | Conversion of methane to dimethyl ether |
| US10189763B2 (en) | 2016-07-01 | 2019-01-29 | Res Usa, Llc | Reduction of greenhouse gas emission |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4806676A (en) * | 1988-06-20 | 1989-02-21 | Eastman Kodak Company | Carbonylation process for preparation of aromatic carboxylic esters and an alkyl iodide |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA1280437C (en) * | 1985-11-26 | 1991-02-19 | Thomas Hassell Larkins Jr. | Process for the co-production of aromatic carboxylates and alkyl iodides |
-
1988
- 1988-10-19 CA CA000580594A patent/CA1304749C/en not_active Expired - Fee Related
- 1988-10-24 KR KR1019890701227A patent/KR890701535A/en not_active Application Discontinuation
- 1988-10-24 JP JP63509158A patent/JPH03500779A/en active Pending
- 1988-10-24 EP EP88909857A patent/EP0409834A1/en not_active Withdrawn
- 1988-10-24 WO PCT/US1988/003704 patent/WO1989004296A1/en not_active Application Discontinuation
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9938217B2 (en) | 2016-07-01 | 2018-04-10 | Res Usa, Llc | Fluidized bed membrane reactor |
| US9981896B2 (en) | 2016-07-01 | 2018-05-29 | Res Usa, Llc | Conversion of methane to dimethyl ether |
| US10189763B2 (en) | 2016-07-01 | 2019-01-29 | Res Usa, Llc | Reduction of greenhouse gas emission |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03500779A (en) | 1991-02-21 |
| KR890701535A (en) | 1989-12-20 |
| EP0409834A1 (en) | 1991-01-30 |
| WO1989004296A1 (en) | 1989-05-18 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MKLA | Lapsed |