Process for producing a cyclic acetal in a heterogeneous reaction system
View Patent ↗A process for producing a cyclic acetal is disclosed. According to the process, a formaldehyde source is combined with an aprotic compound and contacted with a heterogeneous catalyst which causes the formaldehyde source to convert into a cyclic acetal such as trioxane. The catalyst, for instance, may comprise a solid catalyst such as an ion exchange resin. In one embodiment, the process is used for converting anhydrous formaldehyde gas to trioxane. The anhydrous formaldehyde gas may be produced form an aqueous formaldehyde solution by an extractive distillation.
1. A process for producing a cyclic acetal comprising:
contacting a formaldehyde source with a liquid medium comprising a liquid aprotic compound in the presence of a heterogeneous catalyst, the heterogeneous catalyst comprising a solid catalyst, the aprotic compound having a boiling point of 140° C. or higher, determined at 1 bar; and
at least partially converting the formaldehyde source into a cyclic acetal.
2. A process as defined in claim 1 , wherein the heterogeneous catalyst comprises an add ion-exchange material.
3. A process as defined in claim 1 , wherein the heterogeneous catalyst comprises a Lewis add or a Broensted add fixed on a solid support.
4. A process as defined in claim 3 , wherein the solid support is an inorganic material.
5. A process as defined in claim 3 , wherein the solid support is an organic material comprising a polymer.
6. A process as defined in claim 1 , wherein the formaldehyde source comprises gaseous formaldehyde.
7. A process as defined in claim 1 , wherein the formaldehyde source comprises a paraformaldehyde, polyoxymethylene homo- or compolymer, an aqueous formaldehyde solution, or mixtures thereof.
8. A process as defined in claim 1 , wherein the formaldehyde source comprises a mixture of formaldehyde with trioxane.
9. A process as defined in claim 1 , where in the heterogeneous catalyst comprises a Lewis add or Broensted add dissolved in an organic molten salt immobilized on a solid support.
10. A process as defined in claim 1 , wherein the formaldehyde source is converted into the cyclic acetal at a temperature of from about 80° C. to about 120° C., and at a pressure from about 0.15 bar to about 5 bar.
11. A process for producing a cyclic acetal comprising:
contacting a formaldehyde source with a liquid medium comprising a liquid aprotic compound in the presence of a heterogeneous catalyst, the heterogeneous catalyst comprising a solid catalyst; and
at least partially converting the formaldehyde source into a cyclic acetal,
wherein the heterogeneous catalyst is contained in a fixed bed and wherein the formaldehyde source and liquid medium flow through the fixed bed at a superficial liquid velocity of from about 5 m/hr to about 200 m/hr.
12. A process as defined in claim 11 , wherein the formaldehyde source is converted into a cyclic acetal in a reactor that has an inlet into which the formaldehyde source and liquid medium is fed, and wherein the reactor has a liquid-gas mass ratio at the reactor inlet of from about 2 kg/kg to about 30 kg/kg.
13. A process as defined in claim 1 , wherein the formaldehyde source is converted into the cyclic acetal in an agitated tank reactor, the heterogeneous catalyst being suspended within the tank reactor.
14. A process according to claim 1 , wherein the aprotic compound is a polar aprotic compound.
15. A process according to claim 11 , wherein the aprotic compound has a boiling point of 140° C. or higher, determined at 1 bar.
16. A process according to claim 1 wherein the aprotic compound has a relative static permittivity of more than 15, determined at 25° C.
17. A process according to claim 1 wherein higher than 50%, of the formaldehyde source is converted into one or more cyclic acetals during the reaction.
18. A process according to claim 1 wherein the aprotic compound comprises a sulfur-containing organic compound.
19. A process according to claim 1 wherein the aprotic compound is represented by formula (I):
wherein
n is an integer ranging from 1 to 6, and
wherein the ring carbon atoms may optionally be substituted by one or more substituents, preferably selected from C 1 -C 8 -alkyl which may be branched or unbranched.
20. A process according to claim 1 wherein the aprotic compound is sulfolane.
21. A process according to claim 1 wherein the aprotic compound is represented by formula (II):
wherein R 1 and R 2 are independently selected from C 1 -C 8 -alkyl which may be branched or unbranched.
22. A process according to claim 1 wherein the aprotic compound is represented by formula (III):
wherein
n is an integer ranging from 1 to 6, and
wherein the ring carbon atoms may optionally be substituted by one or more substituents, selected from C 1 -C 8 -alkyl which may be branched or unbranched; or
the aprotic compound is represented by formula (IV):
wherein R 3 and R 4 are independently selected from C 1 -C 8 -alkyl which may be branched or unbranched.
23. A process according to claim 1 , further comprising the step of separating the cyclic acetal from the liquid medium by distillation.
24. A process according to claim 1 , further comprising the step of manufacturing polyoxymethylene from the cyclic acetal.