Process for the reduction of R
This disclosure relates to processes which involve: contacting a mixture comprising at least one fluoroolefin and at least one impurity with at least one zeolite to reduce the concentration of the at least one impurity in the mixture; and the at least one zeolite is selected from the group consisting of zeolites having pore opening of at least 4 Angstroms and no more than about 5 Angstroms, zeolites having pore opening of at least about 5 Angstroms and Sanderson electronegativity of no more than about 2.6, and mixtures thereof; provided that the at least one zeolite is not zeolite 4A. This disclosure also relates to processes for making at least one hydrotetrafluoropropene product selected from the group consisting of CF 3 CF═CH 2 , CF 3 CH═CHF, and mixtures thereof; and relates to processes for making at least one hydrochlorotrifluoropropene product selected from the group consisting of CF 3 CCl═CH 2 , CF 3 CH═CHCl, and mixtures thereof.
1. A composition comprising:
at least one zeolite selected from the group consisting of zeolite 5A, zeolite 13X, zeolite LSX, zeolite AW-300, zeolite AW-500, and mixtures thereof; and
at least one compound sorbed to the zeolite, wherein the at least one compound has the formula R f C≡CX, wherein R f is a straight-chain perfluorinated alkyl group, and X is selected from the group consisting of H, F, Cl, Br, and I.
2. The composition according to claim 1 , wherein R f is selected from the group consisting of —CF 3 , —CF 2 CF 3 , and —CF 2 CF 2 CF 3 .
3. The composition according to claim 1 , wherein X is selected from the group consisting of H, F, and Cl.
4. The composition according to claim 1 further comprising at least one fluoroolefin.
5. A process comprising:
subjecting a composition comprising at least one zeolite and at least one compound sorbed to the at least one zeolite to a condition to effect desorption and removal of the at least one compound from the at least one zeolite;
wherein the at least one zeolite is selected from the group consisting of zeolite 5A, zeolite 13X, zeolite LSX, zeolite AW-300, zeolite AW-500, and mixtures thereof; and
wherein the at least one compound has the formula R f C≡CX, wherein R f is a straight-chain perfluorinated alkyl group, and X is selected from the group consisting of H, F, Cl, Br, and I.
6. The process according to claim 5 , wherein the condition comprises heating the composition.
7. The process according to claim 6 further comprising applying a purge liquid to the composition.
8. The process according to claim 6 further comprising applying a purge gas to the composition.
9. The process according to claim 5 , wherein the condition comprises a pressure reduction.
10. The process according to claim 5 , wherein the subjecting regenerates the at least one zeolite.
11. The process according to claim 5 further comprising heating the at least one zeolite to a temperature of 550° C. to activate the at least one zeolite.
12. The process according to claim 5 , wherein R f is selected from the group consisting of —CF 3 , —CF 2 CF 3 , and —CF 2 CF 2 CF 3 .
13. The process according to claim 5 , wherein X is selected from the group consisting of H, F, and Cl.