Preparation of Aliphatic Anhydrides and Alkylidene Dicarboxylates From Divinyl Ethers and Carboxylic Acids

This invention relates to a process for preparing aliphatic anhydrides from divinyl ethers and carboxylic acid.

Divinyl ethers may be synthesized by the process disclosed by Gillis and Schimmel, J. Org. Chem., 25, 2187-90 (1960).

Anhydrides are usually made by displacing chloride from an acid chloride by a carboxylate ion or by heating an acid with an acidic dehydrating agent, such as phosphorus pentoxide or acetic anhydride. These reactions require either high temperatures or generate inorganic waste products.

The invention is a process for preparing aliphatic anhydrides comprising contacting a divinyl ether with a carboxylic acid in the presence of a catalytic amount of a strong acid. The invention is further a process for preparing alkylidene dicarboxylates, which are intermediates in the above preparation of aliphatic anhydrides.

The divinyl ethers used in this invention are represented by the formula ##STR1## wherein R' is separately in each occurrence a substituted or unsubstituted C.sub.1-10 aliphatic group or a hydrogen atom. Preferably, the starting divinyl ether is symmetrical. Most preferably, the starting ether is diisopropenyl ether, which is represented by the formula ##STR2##

In the invented process, these divinyl ethers are reacted with carboxylic acids. Preferably, the carboxylic acids are substituted and unsubstituted aliphatic carboxylic acids. More preferably, the carboxylic acid is 1 to 10 carbon alkenyl or alkyl carboxylic acids. Most preferably, the carboxylic acid is acetic acid, propionic acid or acrylic acid.

The reactants should be combined in about a 2 to 1 ratio of the carboxylic acid to the dialkenyl ether.

In this process carboxylic acid reacts with divinyl ether to form an intermediate which is an alkylidene dicarboxylate, formula II below, and a carbonyl compound, formula III below. This reaction can be represented by the following equation, A: ##STR3## wherein R' is separately in each occurrence a 1 to 10 carbon aliphatic group or a hydrogen atom; and R is a substituted or unsubstituted aliphatic group. More preferably, R is C.sub.1-10 alkenyl or C.sub.1-10 alkyl.

The alkylidene dicarboxylate (II) is a fairly stable compound which is an intermediate in the production of the anhydride. The compound decomposes with heating to the anhydride (I) and the carbonyl compound (III). This can be represented by the following equation, B: ##STR4##

R and R' are defined above. Where the most preferred divinyl ether, diisopropenyl ether is used, the reaction can be described by the following equations: ##STR5##

In this embodiment of the invention, the carbonyl compound (III) is acetone.

The reaction is catalyzed by a strong acid. Preferable strong acids are those with a pK.sub.a of less than 2.0. More preferably, the acids are oxalic acid and trifluoroacetic acid. The catalyst is preferably used in mole ratios of catalyst to divinyl ether of between about 0.5 to 1.0 and 0.001 to 1.0 and more preferably between about 0.1 to 1.0 and 0.01 to 1.0. Other strong acids which may be used include sulfuric acid, hydrochloric acid and nitric acid.

Where the carboxylic acid is a liquid, no solvent is necessary, although a solvent may be used. Suitable solvents include inert organic solvents, preferably chlorinated aliphatic compounds, most preferably those represented by the formula CCl.sub.X Y.sub.4-x, wherein x is an integer from 1 to 4 inclusive and Y is hydrogen or deuterium. To get the desired product of the anhydride, the most preferable solvents are those represented by the formula CCl.sub.3 Y. It has been discovered that the use of CDCl.sub.3 and CHCl.sub.3 as solvents speeds up the reaction and aids the decomposition of the alkylidene dicarboxylate to the anhydride.

Some alkylidene dicarboxylates are more stable than others, and elevated temperatures are required for some of the alkylidene dicarboxylates to decompose to give the anhydride product. Elevated temperatures mean herein above 60.degree. C., preferably between 120.degree. C. and 500.degree. C. Between 25.degree. C. and 60.degree. C., the alkylidene dicarboxylate is the predominant product of this reaction. Between 60.degree. C. and 120.degree. C. both the alkylidene dicarboxylate and the aliphatic anhydride are produced in substantial amounts.

Where propionic anhydride is the desired product, the reaction temperature should be between about 30.degree. C. and 200.degree. C. It is preferable to run the reaction between about 80.degree. C. and 180.degree. C., and most preferable to run it at a temperature between about 120.degree. C. and 150.degree. C. In the most preferred range, almost all of the alkylidene dicarboxylate decomposes.

When acrylic acid is the starting carboxylic acid, the alkylidene dicarboxylate formed is very stable. In order for the alkylidene dicarboxylate of acrylic acid to decompose to the anhydride, the alkylidene dicarboxylate of acrylic acid is preferably exposed to temperatures, up to about 400.degree. C.

When the alkylidene dicarboxylate is subjected to gas pyrolysis, it decomposes to the anhydride and the carbonyl compound. The pyrolysis step can be run between about 250.degree. C. and 400.degree. C. Thus, the process for preparing the anhydride disclosed herein can additionally include a gas pyrolysis step wherein a particularly stable alkylidene dicarboxylate is decomposed to give the anhydride. Where acrylic acid is the starting carboxylic acid, the alkylidene dicarboxylate produced decomposes to acrylic anhydride and the carbonyl compound when subjected to gas pyrolysis.

When acrylic anhydride is the desired product, CDCl.sub.3 or CHCl.sub.3 are the preferred solvents as acrylic anhydride is a significant portion of the product when those solvents are used.

This process can be run at autogeneous pressure. The process may be run in an inert gas atmosphere, such as N.sub.2.

Specific Embodiments

The practice of the instant invention is further illustrated by the following examples. These embodiments and examples are not intended to limit the scope of the instantly claimed invention.

Diisopropenyl ether (4.9 g, 0.05 mole, 97 percent pure) and acetic acid (6.0 g, 0.10 mole) were combined in a round-bottom flask outfitted with a condenser, thermometer and N.sub.2 blanket, and refluxed (60.degree. C.) for 2 hours. Gas chromatographic analysis showed the reaction had not gone to completion based on acetic acid remaining. Two drops of trifluoroacetic acid were added and the reaction went to completion with the formation of two major products, acetic anhydride and 2,2,-propane diacetate (alkylidene dicarboxylate). The volatiles were removed on a rotary evaporator and the two major products constituted 95 percent of the gas chromatograph area in a ratio of 1:1.4, acetic anhydride to 2,2,-propane diacetate.

This example demonstrates the catalytic effect of the strong acid and the products which result from the reaction.

Propionic acid (3.9 ml, 0.052 mole) was added dropwise to stirring diisopropenyl ether (2.55 g, 0.026 mole) in a 25-ml, 3-neck round-bottom flask equipped with condenser, dropping funnel, thermometer and N.sub.2 blanket. Oxalic acid (50 mg) was added causing an immediate rise in temperature from 25.degree. C. to 38.degree. C. The reactants were allowed to react at 25.degree. C. for 68 hours. Thereafter, the temperature of the reaction mixture was raised to 60.degree. C. and kept there for 72 hours. This reaction was followed by gas chromatography as samples of the mixture were taken periodically.

The reaction did not reach completion after 72 hours at 60.degree. C. Heating at 60.degree. C. enhanced formation of both the propionic anhydride and the 2,2-propane dipropionate (the alkylidene dicarboxylate). Table I shows the gas chromatographic data relative to the amounts of alkylidene dicarboxylate and aliphatic anhydride produced.

Diisopropenyl ether (7.42 g, 0.076 mole) and oxalic acid (0.056 g, 0.06 mmole) were combined in a reaction vessel like that used in Example 2. Propionic acid (11.2 ml, 0.15 mole) was added dropwise with stirring and the reaction mixture was held at 35.degree. C. with an ice bath. Upon completion of the addition, the reaction mixture was heated to 60.degree. C. for 23 hours. Thereafter the temperature was raised to 100.degree. C. for 23 hours and then 140.degree. C. for 5 hours, after which gas chromatography and nuclear magnetic resonance indicated the reaction was complete.

The reaction was followed by gas chromatography and the data relative to the amounts of alkylidene dicarboxylate and aliphatic anhydride produced are compiled in Table II.

These data show that the 2,2-propane dipropionate and propionic anhydride concentrations increase at 60.degree. C. with the former forming more rapidly and reaching its maximum concentration after 28 hours. At 100.degree. C. the 2,2,-propane dipropionate reaches its maximum concentration after about 1 hour, thereafter it starts to decompose to propionic anhydride.

A solution of oxalic acid (0.23 g, 0.003 mole) in propionic acid (29.0 ml, 0.39 mole) was added dropwise with stirring to diisopropenyl ether (18.38 g, 0.188 mole) at 0.degree. C. to 10.degree. C. in a 100-ml reaction flask equipped as described in the above examples. The flask was placed in a preheated (65.degree. C.) oil bath to begin the reaction. The temperature was gradually increased to 120.degree. C. and the reaction was followed by gas chromatography. Upon completion of the reaction, the anhydride concentration, as measured by gas chromatography, was 97 percent and no 2,2-propane dipropionate was present in the product. The data relative to the amounts of alkylidene dicarboxylate and aliphatic anhydride generated by this test are compiled in Table III.

Diisopropenyl ether (105.9 g, 1.03 moles, 95.5 percent pure) was placed in a 500-ml, 3-neck flask fitted with a magnetic stirrer, thermometer, condenser and dropping funnel with a pressure equalizing side-arm. p-Methoxyphenol (0.025 g, 0.002 mole) was added as an inhibitor and oxalic acid (0.96 g, 0.01 mole) was added as a catalyst. Acrylic acid (165.7 g, 2.3 moles) containing 200 ppm p-methoxyphenol was added slowly to the reaction vessel by the dropping funnel. An ice bath was used to keep the reaction mixture temperature between 22.degree. C. and 25.degree. C. during the addition. The reaction was followed by periodically removing samples and analyzing them by gas chromatography. After 2 days, the reaction mixture had a constant composition. After distillation, 101.0 g of 95 percent by gas-liquid chromatography area of 2,2-propane diacrylate (a 51 percent isolated yield) were recovered. Only traces of acrylic anhydride were observed throughout the reaction. The p-methoxyphenol was added to inhibit polymerization. Later testing determined its use was unnecessary.

Microliter quantities of 2,2-propane diacrylate were pyrolyzed in the injection block of a Hewlett-Packard 5712A gas chromatograph at temperatures ranging from 250.degree. C. to 400.degree. C. Gas chromatographic analysis of the pyrolysates showed that the concentration of the acrylic anhydride in the reaction mixture had increased significantly.

Acrylic acid (1.47 g, 0.02 mole), diisopropenyl ether (0.99 g, 0.01 mole) and oxalic acid (0.008 g, 8.9.times.10.sup.-5 moles) were mixed in a nitrogen-filled 10-ml volumetric flask. A 30-.mu.l aliquot of this mixture was transferred to a nuclear magnetic resonance tube, mixed with CDCl.sub.3 (0.5 ml), methylene chloride (10 .mu.) and tetramethylsilane. After 24.5 hours, the sample in the nuclear magnetic resonance tube showed that the reaction was almost complete as the acid was nearly consumed. The amount of acrylic anhydride produced was 1.5:1 to that of the 2,2-propane diacrylate. Conversely the mixture in the original volumetric flask had a much lower conversion of reactants to products and almost no anhydride. After 14 days, the amount of acrylic anhydride in the nuclear magnetic resonance tube increased while that in the volumetric flask did not. The ratio of acrylic anhydride to 2,2-propane diacrylate was 3.3:1.

The CDCl.sub.3 has some solvent effect on the formation of an anhydride over the alkylidene dicarboxylate. The product mix is also affected by the length of time of the reaction in that yield of anhydride increases with time.

As a point of comparison for following the formation of propionic anhydride distillative isolation, nuclear magnetic resonance and gas chromatographic analysis were performed on the initial reaction mixture of Example 4. The nuclear magnetic resonance spectrum in CDCl.sub.3 showed an absence of diisopropenyl ether, low levels of the 2,2-propane dipropionate and high levels of propionic anhydride and acetone. During the nuclear magnetic resonance analysis, the sample had undergone a color change from colorless to dark yellow. Gas chromatographic analysis on the initial reaction mixture and on the sample used for nuclear magnetic resonance gave the following reactant/product distribution:

There is a solvent effect with CDCl.sub.3 which causes decomposition of the alkylidene dicarboxylate to the anhydride and acetone.