Method for purifying fluid that includes trifluoroethylene, and method for producing trifluoroethylene
US-2016347693-A1 · Dec 1, 2016 · US
US11124469B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11124469-B2 |
| Application number | US-202016849059-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 15, 2020 |
| Priority date | May 16, 2011 |
| Publication date | Sep 21, 2021 |
| Grant date | Sep 21, 2021 |
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A hydrogenation process is disclosed. The process involves reacting a fluoroolefin with H2 in a reaction zone in the presence of a palladium catalyst to produce a hydrofluoroalkane product, wherein the palladium catalyst comprises palladium supported on a carrier wherein the palladium concentration is from about 0.001 wt % to about 0.2 wt % based on the total weight of the palladium and the carrier. Also disclosed is a palladium catalyst composition consisting essentially of palladium supported on α-Al2O3 wherein the palladium concentration is from about 0.001 wt % to about 0.2 wt % based on the total weight of the palladium and the α-Al2O3. Also disclosed is a hydrogenation process comprising (a) passing a mixture comprising fluoroolefin and H2 through a bed of palladium catalyst in a reaction zone wherein the palladium catalyst comprises palladium supported on a carrier; and (b) producing a hydrofluoroalkane product; characterized by: the palladium catalyst in the front of the bed having lower palladium concentration than the palladium catalyst in the back of the bed.
Opening claim text (preview).
What is claimed is: 1. A composition comprising at least one fluoroolefin having the formula C n H m F 2n-m , wherein n is an integer from 2 to 8 and m is an integer from 0 to 2n−1; at least one hydrofluoroalkane which is the hydrogenation product of said at least one fluoroolefin; a diluent other than the at least one hydrofluoroalkane, wherein the diluent is selected from the group consisting of methane, ethane, propane, CHF 3 , CH 2 F 2 , CHF 2 CF 3 , CHF 2 CHF 2 , CH 2 FCF 3 , CF 3 CF 3 , CF 3 CF 2 CF 3 , CF 3 CHFCH 2 F, CF 3 CH 2 CHF 2 , CF 3 CHFCH 3 , CF 3 CH 2 CH 2 F, CF 3 CHFCHF 2 , CF 3 CH 2 CF 3 , CF 3 CF 2 CH 2 F, CF 3 CH 2 CH 2 CF 3 , CF 3 CHFCHFC 2 F 5 , C 6 F 14 , and C 2 F 5 CHFCHFC 3 F 7 and selected to be different from the at least one hydrofluoroalkane; and a palladium catalyst comprising palladium supported on a carrier comprising α-Al 2 O 3 . 2. The composition of claim 1 wherein the palladium concentration is from about 0.001 wt % to about 0.2 wt % based on the total weight of the palladium and the carrier. 3. The composition of claim 1 wherein the palladium concentration is from about 0.001 wt % to about 0.1 wt % based on the total weight of the palladium and the carrier. 4. The composition of claim 1 wherein the palladium concentration of the palladium catalyst is from about 0.001 wt % to about 0.04 wt % based on the total weight of the palladium and the carrier. 5. The composition of claim 1 wherein the palladium concentration of the palladium catalyst is from about 0.015 wt % to about 0.025 wt % based on the total weight of the palladium and the carrier. 6. The composition of claim 1 wherein the fluoroolefin is selected from the group consisting of CF 3 CF═CF 2 (HFP), CF 3 CF═CHF (HFO-1225ye), CF 3 CH═CF 2 , CF 3 CF═CH 2 , CF 3 CH═CHF, CF 3 CF═CFCF 3 , CF 3 CH═CHCF 3 , CF 3 CH═CFCF 3 , CF 3 CF 2 CF═CF 3 , CF 3 CF 2 CH═CHCF 3 , (CF 3 ) 2 CFCF═CF 2 , CF 3 CF═CHC 2 F 5 , CF 3 CH═CFC 2 F 5 , C 4 F 9 CH═CH 2 , CF 3 CF 2 CF 2 CF 2 CF═CFCF 3 , CF 3 CF 2 CF 2 CF═CFCF 2 CF 3 , C 2 F 5 CH═CFCF 2 C 2 F 5 , C 2 F 5 CF═CHCF 2 C 2 F 5 , and mixtures thereof. 7. The composition of claim 1 wherein the molar ratio of the hydrofluoroalkane to fluoroolefin is from 10:1 to 1:1. 8. The composition of claim 7 wherein the molar ratio of the hydrofluoroalkane to fluoroolefin is from 5:1 to 1:1. 9. The composition of claim 1 wherein the fluoroolefin is CF 3 CF═CF 2 and the hydrofluoroalkane is CF 3 CHFCHF 2 or where the fluoroolefin is CF 3 CF═CHF and the hydrofluoroalkane is CF 3 CHFCH 2 F. 10. The composition of claim 1 wherein hydrogen is additionally present. 11. The composition of claim 10 wherein the molar ratio of hydrogen to fluoroolefin is from 0.5:1 to 5:1. 12. The composition of claim 1 wherein the diluent is selected from the group consisting of CHF 3 , CH 2 F 2 , CHF 2 CF 3 , CHF 2 CHF 2 , CH 2 FCF 3 , CF 3 CF 3 , CF 3 CF 2 CF 3 , CF 3 CHFCH 2 F, CF 3 CH 2 CHF 2 , CF 3 CHFCH 3 , CF 3 CH 2 CH 2 F, CF 3 CHFCHFC 2 F 5 , C 6 F 14 , C 2 F 5 CHFCHFC 3 F 7 , and combinations thereof and selected to be different from the at least one hydrofluoroalkane. 13. The composition of claim 1 , wherein the fluoroolefin is CF 3 CF═CH 2 or CF 3 CH═CHF. 14. The composition of claim 1 , wherein the at least one fluoroolefin is a terminal fluoroolefin having 3 to 7 carbons. 15. A composition comprising a fluoroolefin having the formula C n H m F 2n-m wherein n is an integer from 2 to 8 and m is an integer from 0 to 2n−1; a hydrofluoroalkane which is the hydrogenation product of said fluoroolefin, said hydrofluoroalkane having the formula C n H m+2 F 2n-m ; a diluent other than the at least one hydrofluoroalkane, wherein the diluent is selected from the group consisting of CHF 3 , CH 2 F 2 , CHF 2 CF 3 , CHF 2 CHF 2 , CH 2 FCF 3 , CF 3 CF 3 , CF 3 CF 2 CF 3 , CF 3 CHFCH 2 F, CF 3 CH 2 CHF 2 , CF 3 CHFCH 3 , CF 3 CH 2 CH 2 F, CF 3 CHFCHFC 2 F 5 , C 6 F 14 , C 2 F 5 CHFCHFC 3 F 7 , and combinations thereof and selected to be different from the at least one hydrofluoroalkane; and a bed of palladium catalyst supported on a carrier comprising α-Al 2 O 3 , the bed of palladium catalyst having a front and a back, wherein the palladium catalyst in the front of the bed has a lower palladium concentration than the palladium catalyst in the back of the bed. 16. The composition according to claim 15 wherein the palladium concentration of the catalyst in the front of the bed is from about 0.001 wt % to about 0.2 wt % based on the total weight of the palladium and the carrier, and the palladium concentration of the catalyst in the back of the bed is from about 0.1 wt % to about 1 wt % based on the total weight of the palladium and the carrier. 17. The composition according to claim 15 wherein the palladium concentration of the catalyst in the front of the bed is from about 0.001 wt % to about 0.08 wt % based on the total weight of the palladium and the carrier, and the palladium concentration of the catalyst in the back of the bed is from about 0.2 wt % to about 0.8 wt % based on the total weight of the palladium and the carrier. 18. The composition according to claim 15 wherein the palladium concentration of the catalyst in the front of the bed is from about 0.015 wt % to about 0.025 wt % based on the total weight of the palladium and the carrier, and the palladium concentration of the catalyst in the back of the bed is from about 0.3 wt % to about 0.6 wt % based on the total weight of the palladium and the carrier. 19. The composition of claim 15 wherein the fluoroolefin is selected from the group consisting of CF 3 CF═CF 2 (HFP), CF 3 CF═CHF (HFO-1225ye), CF 3 CH═CF 2 , CF 3 CF═CH 2 , CF 3 CH═CHF, CF 3 CF═CFCF 3 , CF 3 CH═CHCF 3 , CF 3 CH═CFCF 3 , CF 3 CF 2 CF═CFCF 3 , CF 3 CF 2 CH═CHCF 3 , (CF 3 ) 2 CFCF═CF 2 , CF 3 CF═CHC 2 F 5 , CF 3 CH═CFC 2 F 5 , C 4 F 9 CH═CH 2 , CF 3 CF 2 CF 2 CF 2 CF═CFCF 3 , CF 3 CF 2 CF 2 CF═CFCF 2 CF 3 , C 2 F 5 CH═CFCF 2 C 2 F 5 , C 2 F 5 CF═CHCF 2 C 2 F 5 , and mixtures thereof. 20. The composition of claim 15 wherein the molar ratio of the hydrofluoroalkane to fluoroolefin is from 5:1 to 1:1 at the back of the bed. 21. The composition of claim 15 wherein the fluoroolefin is CF 3 CF═CF 2 and the hydrofluoroalkane is CF 3 CHFCHF 2 or where the fluoroolefin is CF 3 CF═CHF and the hydrofluoroalkane is CF 3 CHFCH 2 F. 22. The composition of claim 15 where H 2 is additionally present and the molar ratio of H 2 to fluoroolefin ranges from about 0.5:1 to about 5:1. 23. The composition of claim 15 , wherein the fluoroolefin is CF 3 CF═CH 2 or CF 3 CH═CHF.
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