Process for the catalytic decarboxylative cross-ketonization of aryl and aliphatic carboxylic acid
The present invention pertains to a process for the cross-ketonization (Piria reaction) between an aryl carboxylic acid and an aliphatic carboxylic acid using a metal-based compound and a slight or a moderate excess of aryl carboxylic acid. A good selectivity, up to 99 mol %, can be achieved. The aryl aliphatic ketone can be used for the preparation of surfactants and other downstream products.
1. A process for the catalytic decarboxylative cross-ketonisation of aryl- and aliphatic carboxylic acids comprising the steps of:
a) providing a mixture containing:
i) an aryl carboxylic acid;
ii) an aliphatic carboxylic acid;
iii) a metal-containing compound;
in which the number of moles of the metal in the mixture is at least equal to 90% of the sum of the number of moles of aryl carboxylic acid and the number of moles of aliphatic carboxylic acid divided by the valency of the metal
said mixture being substantially free of any added solvent;
b) heating the mixture at a temperature sufficient to form metal carboxylates;
c) further heating the mixture at a temperature sufficient to form a dialiphatic ketone and an aryl aliphatic ketone K;
d) adding to the reaction mixture of step c):
i) aryl carboxylic acid in an amount which corresponds substantially to the amount of aryl carboxylic acid consumed during the formation of the aryl aliphatic ketone K in step c);
ii) aliphatic carboxylic acid in an amount which corresponds substantially to the amount of aliphatic carboxylic acid consumed during the formation of the aryl aliphatic ketone K and the dialiphatic ketone in step c);
maintaining the mixture at a temperature sufficient to continue forming the dialiphatic ketone and the aryl aliphatic ketone K;
e) optionally repeating step d).
2. The process of claim 1 , wherein:
x is the number of moles of aryl carboxylic acid
y is the number of moles of aliphatic carboxylic acid, and
the number of moles of a metal of valence z in the mixture of step a) is within the range of from 0.9[(x+y)/z] to 1.1[(x+y)/z].
3. The process according to claim 1 , wherein the metal is iron-containing compound.
4. The process of claim 3 , wherein the iron-containing compound is selected from the group consisting of iron metal, bivalent Fe (II) compounds, trivalent Fe (III) compounds, and compounds in which iron is present in both bivalent Fe (II) and bivalent Fe (III) oxidation states.
5. The process of claim 1 , wherein step b) is carried out at a temperature T 1 from 225° C. to 290° C., and steps c) and step d) are carried out at a temperature T 2 from 300° C. to 400° C.
6. The process of claim 1 , wherein the molar ratio of the total amount of aryl carboxylic acid and the aliphatic carboxylic acid ranges from 0.3 to 1.8.
7. The process of claim 1 , wherein the aryl carboxylic acid is selected from the group consisting of benzoic acid, furoic acid, o-toluic acid, m-toluic acid and p-toluic acid.
8. The process of claim 1 , wherein the aliphatic carboxylic acid is a fatty acid.
9. The process according to claim 8 , wherein the fatty acid contains from 8 to 18 carbon atoms.
10. A process for the preparation of at least one end compound from at least one aryl aliphatic ketone K, said process comprising:
synthesizing the aryl aliphatic ketone K through the process of claim 1 ,
causing the aryl aliphatic ketone K to react in accordance with a single or multiple chemical reaction scheme involving at least one reagent other than the aryl aliphatic ketone K, wherein at least one product of the chemical reaction scheme is the end compound product that is not further caused to be chemically converted into another compound.