High-purity 1-fluorobutane and plasma etching method
US-2016372335-A1 · Dec 22, 2016 · US
US9321708B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9321708-B2 |
| Application number | US-201314375193-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 24, 2013 |
| Priority date | Feb 2, 2012 |
| Publication date | Apr 26, 2016 |
| Grant date | Apr 26, 2016 |
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Provided is a purification method for efficiently reducing an undesirable organic compound or compound in (E)-1-chloro-3,3,3-trifluoropropene and thereby obtaining (E)-1-chloro-3,3,3-trifluoropropene with high purity. The purification method of OF-1233E according to the present invention is characterized by bringing a composition containing OF-1233E and at least one organic compound selected from the group consisting of HCFC-142 isomers, HCFC-244fa, HFC-245fa, OF-1234E, OF-1234Z and OF-1233Z into contact with a solid adsorbent.
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The invention claimed is: 1. A method for purifying (E)-1-chloro-3,3,3-trifluoropropene (OF-1233E), comprising bringing a composition containing OF-1233E and 1,1,1,3,3-pentafluoropropane (HCFC-245fa) into contact with a solid adsorbent, wherein the solid adsorbent is a zeolite X; and wherein the weight ratio of the composition to the solid adsorbent is in a range of 5 to 50. 2. The method according to claim 1 , wherein the zeolite X is at least one of a Na-exchanged zeolite X and a Ca-exchanged zeolite X. 3. The method according to claim 1 , wherein the weight ratio of the composition to the solid adsorbent is in the range of 8 to 40. 4. The method according to claim 2 , wherein the weight ratio of the composition to the solid adsorbent is in the range of 8 to 40. 5. A method for purifying OF-1233E, comprising bringing a composition containing OF-1233E, HFC-245fa, and at least one organic compound selected from the group consisting of compounds of the formula C 2 H 3 ClF 2 (HCFC-142 isomers), 1-chloro-1,3,3,3-tetrafluoropropane (HCFC-244fa), (E)-1,3,3,3-tetrafluoropropene (OF-1234E), (Z)-1,3,3,3-tetrafluoropropene (OF-1234Z), and (Z)-1-chloro-3,3,3-trifluoropropene (OF-1233Z) into contact with a solid adsorbent, wherein the solid adsorbent is a zeolite X; and wherein the weight ratio of the composition to the solid adsorbent is in a range of 5 to 50. 6. The method according to claim 5 , wherein the zeolite X is at least one of a Na-exchanged zeolite X and a Ca-exchanged zeolite X. 7. The method according to claim 5 , wherein the weight ratio of the composition to the solid adsorbent is in the range of 8 to 40. 8. The method according to claim 6 , wherein the weight ratio of the composition to the solid adsorbent is in the range of 8 to 40. 9. A solid-liquid heterogeneous mixture for use in the method according to claim 1 , comprising: a composition containing OF-1233E and; and a solid adsorbent, wherein the solid adsorbent is a zeolite X; and wherein the weight ratio of the composition to the solid adsorbent is in a range of 5 to 50. 10. The solid-liquid heterogeneous mixture according to claim 9 , wherein the zeolite X is at least one of a Na-exchanged zeolite X and a Ca-exchanged zeolite X. 11. The solid-liquid heterogeneous mixture according to claim 9 , wherein the weight ratio of the composition to the solid adsorbent is in the range of 8 to 40. 12. The solid-liquid heterogeneous mixture according to claim 10 , wherein the weight ratio of the composition to the solid adsorbent is in the range of 8 to 40. 13. The solid-liquid heterogeneous mixture for use in the method according to claim 5 , comprising: a composition containing OF-1233E, HFC-245fa, and at least one organic compound selected from the group consisting of HCFC-142 isomers, HCFC-244fa, OF-1234E, OF-1234Z, and OF-1233Z; and a solid adsorbent, wherein the solid adsorbent is a zeolite X; and wherein the weight ratio of the composition to the solid adsorbent is in a range of 5 to 50. 14. The solid-liquid heterogeneous mixture according to claim 13 , wherein the zeolite X is at least one of a Na-exchanged zeolite X and a Ca-exchanged zeolite X. 15. The solid-liquid heterogeneous mixture according to claim 13 , wherein the weight ratio of the composition to the solid adsorbent is in the range of 8 to 40. 16. The solid-liquid heterogeneous mixture according to claim 14 , wherein the weight ratio of the composition to the solid adsorbent is in the range of 8 to 40.
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