Process for heterogeneously catalyzed preparation of carboxylic acid derivatives
View Patent ↗Process for heterogeneously catalyzed preparation of carboxylic acid derivatives using a reactor system comprising at least one reservoir vessel V, feed lines, at least one pump and a reaction vessel R, characterized in that a permanent gas flow through the reaction vessel R is applied through a gas feed line, and in which a reaction chamber in which the heterogeneous catalyst is not introduced in tightly packed form is delimited by at least two filters such that both the mass flow and the gas flow are passed through the reaction chamber.
1. A process for heterogeneously catalysed preparation of a carboxylic acid derivative, selected from the group consisting of esters, thioesters, and amides, by reacting a carboxylic acid with a corresponding reactant sufficient to form the carboxylic acid derivative therewith, the process comprising:
(a) utilizing a reactor system comprising:
at least one reservoir vessel (V);
a reaction vessel (R) comprising a reaction chamber;
reaction medium feed lines which connect the reservoir vessel (V) to the reaction vessel (R); and
at least one pump operably connected to at least one of the reaction medium feed lines;
(b) providing a heterogeneous catalyst in the reaction chamber, the heterogeneous catalyst comprising at least one enzyme or comprising microorganisms comprising at least one enzyme;
(c) applying, through a gas feed line, a permanent gas flow through the reaction vessel (R);
(d) applying a reaction medium to the reaction chamber, the reaction medium comprising the carboxylic acid and the corresponding reactant sufficient to form the carboxylic acid derivative; and
(e) reacting the reaction medium in the presence of the heterogeneous catalyst and the gas flow, so as to prepare the carboxylic acid derivative;
wherein the heterogeneous catalyst, which is not introduced in tightly packed form, is delimited in the reaction chamber between at least two filters, such that both the mass flow of the reaction medium and the gas flow are passed through the reaction chamber.
2. The process according to claim 1 ;
wherein the enzyme or microbial catalyst is supported on a solid.
3. The process according to claim 2 ;
wherein the enzymatic or microbial catalyst is fixed covalently or noncovalently in particulate form on the solid.
4. The process according to claim 3 ;
wherein the solid comprises at least one substance selected from the group consisting of:
polymers selected from the group consisting of polyacrylate, polymethacrylate, polyvinylstyrene, styrene-divinylbenzene copolymers, polypropylene, polyethylene, polyethylene terephthalate, polytetrafluoroethylene, and copolymers of these compounds; and
oxidic and ceramic supports.
5. The process according to claim 4 ;
wherein the solid comprises an acidic or basic ion exchange resin.
6. The process according to claim 4 ;
wherein the solid comprises a polymethacrylate polymer.
7. The process according to claim 6 ;
wherein the solid is in the form of support material having a mean particle size of greater than 0.5 μm.
8. The process according to claim 7 ;
wherein the heterogeneous catalyst is reused.
9. The process according to claim 8 , further comprising:
applying a vacuum pressure at the reservoir vessel (V).
10. The process according to claim 9 ;
wherein the gas comprises at least one component selected from the group consisting of air, lean air, oxygen, nitrogen, noble gases, and carbon dioxide.
11. The process according to claim 10 ;
wherein the reaction is performed at a temperature of 20° C. to 100° C.
12. The process according to claim 2 ;
wherein the solid comprises at least one substance selected from the group consisting of;
polymers selected form the group consisting of polyacrylate, polymethacrylate, polyvinylstyrene, styrene-divinylbenzene copolymers, polypropylene, polyethylene, polyethylene terephthalate, polytetrafluoroethylene, and copolymers of these compounds; and
oxidic and ceramic supports.
13. The process according to claim 2 ;
wherein the solid consists of an acidic or basic ion exchange resin.
14. The process according to claim 2 ; wherein the oxidic and/or ceramic support consists of diatomite, zeolites, silica or controlled-pore glass.
15. The process according to claim 2 ;
wherein the solid is in the form of support material with a mean particle size of greater than 0.5 μm.
16. The process according to claim 1 ;
wherein the heterogeneous catalyst is reused.
17. The process according to claim 1 , further comprising:
applying a vacuum pressure at the reservoir vessel (V).
18. The process according to claim 1 ;
wherein the gas comprises at least one component selected from the group consisting of air, lean air, oxygen, nitrogen, noble gases, and carbon dioxide.
19. The process according to claim 1 ;
wherein the reaction is performed at a temperature of 20° C. to 100° C.