Catalysts and methods for alcohol dehydration
US-2015375214-A1 · Dec 31, 2015 · US
US9452958B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9452958-B2 |
| Application number | US-201314358101-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 24, 2013 |
| Priority date | Jan 25, 2012 |
| Publication date | Sep 27, 2016 |
| Grant date | Sep 27, 2016 |
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This invention provides a process for producing a fluoroolefin comprising reacting, in a vapor phase, a fluorinating agent and a chlorine-containing alkene or a chlorine-containing alkane in the presence of at least one catalyst selected from the group consisting of chromium oxide containing a Group 5 element and fluorinated chromium oxide containing a Group 5 element. According to the process of the present invention, the target fluoroolefin can be obtained with high starting material conversion and good selectivity.
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The invention claimed is: 1. A process for producing a fluoroolefin of the following formula (6): CF 3 (CF 2 ) n CA=CHB, wherein one of A and B is F and the other is H, n is an integer of 0 to 2, with the proviso that n is 0 when a chlorine-containing alkene of the formula (5) is used as a starting material, the method comprising reacting, in a vapor phase, a fluorinating agent and at least one chlorine-containing compound in the presence of at least one catalyst selected from the group consisting of chromium oxide containing a Group 5B element and fluorinated chromium oxide containing a Group 5B element, wherein the at least one chlorine-containing compound is selected from the group consisting of a chlorine-containing alkane of the following formula (1): CX 3 (CX 2 ) n CClYCH 2 Z, wherein X is independently F or Cl, Y is H or F, when Y is H, Z is Cl or F, and when Y is F, Z is H, and n is an integer of 0 to 2; a chlorine-containing alkane of the following formula (2): CX 3 (CX 2 ) n CH 2 CHX 2 , wherein X is independently F or Cl, and at least one X is Cl, and n is an integer of 0 to 2; a chlorine-containing alkene of the following formula (3): CX 3 (CX 2 ) n CCl═CH 2 , wherein X is independently F or Cl, and n is an integer of 0 to 2; a chlorine-containing alkene of the following formula (4): CX 3 (CX 2 ) n CH═CHX, wherein X is independently F or Cl, and at least one X is Cl, and n is an integer of 0 to 2; and the chlorine-containing alkene of the following formula (5): CH 2 XCCl═CX 2 , wherein X is independently F or Cl, and wherein the Group 5B element is in a quadrivalent or pentavalent state. 2. The process for producing a fluoroolefin according to claim 1 , wherein the Group 5B element contained in the catalyst is at least one element selected from the group consisting of V and Nb. 3. The process for producing a fluoroolefin according to claim 1 , wherein the Group 5B element contained in the catalyst is two or more elements selected from the group consisting of V, Nb, and Ta. 4. The process for producing a fluoroolefin according to claim 1 , wherein the Group 5B element in the catalyst is contained in an amount of 0.1 to 30 atom % based on the total amount of Cr and the Group 5B element in the catalyst. 5. The process for producing a fluoroolefin according to claim 1 , wherein the catalyst contains vanadium in an amount of 0.1 to 6 atom % based on the total amount of Cr and the Group 5B element in the catalyst. 6. The process for producing a fluoroolefin according to claim 1 , wherein the fluorinating agent is anhydrous hydrogen fluoride. 7. The process for producing a fluoroolefin according to claim 1 , wherein the chlorine-containing compound used as a starting material is at least one member selected from the group consisting of the chlorine-containing alkane of the following formula (1): CX 3 (CX 2 ) n CClYCH 2 Z, the chlorine-containing alkene of the following formula (3): CX 3 (CX 2 ) n CCl═CH 2 , and the chlorine-containing alkene of the following formula (5): CH 2 XCCl═CX 2 , and the fluoroolefin obtained is a compound of the following formula (6-1): CF 3 (CF 2 ) n CF═CH 2 , or a mixture of the compound of the formula (6-1) and a compound of the following formula (6 2): CF 3 (CF 2 ) n CH═CHF, wherein n in each of formula (6-1) and formula (6-2) is an integer of 0 to 2, with the proviso that n is 0 when the chlorine-containing alkene of the formula (5) is used as a starting material. 8. The process for producing a fluoroolefin according to claim 7 , wherein the chlorine-containing compound used as a starting material is at least one member selected from the group consisting of CF 3 CHClCH 2 Cl (HCFC-243db), CF 3 CFClCH 3 (HCFC-244bb), CCl 3 CCl═CH 2 (HCO-1230xf), CF 3 CCl═CH 2 (HCFO-1233xf), and CH 2 ClCCl═CCl 2 (HCO-1230xa), and the fluoroolefin obtained is CF 3 CF═CH 2 (HFO-1234yf) or a mixture of CF 3 CF═CH 2 (HFO-1234yf) and CF 3 CH═CHF (HFO-1234ze). 9. The process for producing a fluoroolefin according to claim 1 , wherein the chlorine-containing compound used as a starting material is at least one member selected from the group consisting of the chlorine-containing alkane of the following formula (2): CX 3 (CX 2 ) n CH 2 CHX 2 and the chlorine-containing alkene of the following formula (4): CX 3 (CX 2 ) n CH═CHX, and the fluoroolefin obtained is a fluoroolefin of the following formula (6-2): CF 3 (CF 2 ) n CH═CHF, wherein n is an integer of 0 to 2. 10. The process for producing a fluoroolefin according to claim 9 , wherein the chlorine-containing compound used as a starting material is at least one member selected from the group consisting of CCl 3 CH═CHCl (HCO-1230zd) and CF 3 CH═CHCl (HCFO-1233zd), and the fluoroolefin obtained is CF 3 CH═CHF (HFO-1234ze). 11. The process for producing a fluoroolefin according to claim 10 , wherein the chlorine-containing compound used as a starting material is CF 3 CH═CHCl (HCFO-1233zd) and the fluoroolefin obtained is CF 3 CH═CHF (HFO-1234ze). 12. The process for producing a fluoroolefin according to claim 1 , wherein reaction is performed in the presence of oxygen, chlorine, or both oxygen and chlorine. 13. The process for producing a fluoroolefin according to claim 12 , wherein the reaction is performed in the presence of oxygen in an amount of 0.001 to 0.2 mol per mol of the chlorine-containing compound used as a starting material.
X-ray diffraction · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
Compounds characterised by their crystallite size · CPC title
characterised by their amorphous structures · CPC title
Precipitation · CPC title
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