Method for removing unsaturated halogenated impurities from 2,3,3,3-tetrafluoropropene (HFO-1234yf)
A method for removing unsaturated halogen impurities from 2,3,3,3-tetrafluoropropene (HFO-1234yf) of the type that may otherwise be difficult to separate from HFO-1234yf due to the impurities having boiling points which are close to that of HFO-1234yf and/or the potential of one or more of the impurities to form azeotropic mixtures with HFO-1234yf. A HFO-1234yf stream including unsaturated halogenated impurities is first passed through a caustic scrubber and is then passed through an acid scrubber. In the caustic scrubber and acidic scrubber, undesirable impurities are removed, in particular, 3,3,3-trifluoropropene (1243zf), 1-chloro-1-fluoroethylene (1131a), vinyl chloride (1140), and/or 1-chloro-2-fluoroethylene (1131).
1. A method for removing unsaturated halogenated impurities from 2,3,3,3-tetrafluoropropene (HFO-1234yf), comprising the steps of:
providing a stream of 1234yf containing at least one impurity selected from the group consisting of 3,3,3-trifluoropropene (1243zf), 1-chloro-1-fluoroethylene (1131a), vinyl chloride (1140), 1-chloro-2-fluoroethylene (1131), and combinations thereof; and
contacting the stream with an acidic scrubbing fluid in an acid scrubber.
2. The method of claim 1 , wherein the at least one impurity includes 1-chloro-1-fluoroethylene (1131a) and, after said contacting step, an amount of 1131a in the stream is reduced by at least 5 wt. % relative to an amount of 1131a originally present in the stream.
3. The method of claim 1 , wherein the at least one impurity includes vinyl chloride (1140) and, after said contacting step, an amount of 1140 in the stream is reduced by at least 5 wt. % relative to an amount of 1140 originally present in the stream.
4. The method of claim 1 , wherein the at least one impurity includes 1-chloro-2-fluoroethylene (1131) and, after said contacting step, an amount of 1131 in the stream is reduced by at least 5 wt. % relative to an amount of 1131 originally present in the stream.
5. The method of claim 1 , wherein the acidic scrubbing fluid is sulfuric acid having a concentration between 88 wt. % and 99 wt. %.
6. The method of claim 1 , wherein at least one of the following conditions are present within the acid scrubber:
a temperature between 0° C. and 70° C.; and
a contact time between the vapor stream and acidic scrubbing fluid of between 0.1 second and 200 seconds.
7. The method of claim 1 , further comprising the additional step, prior to said contacting step, of contacting the stream with a basic scrubbing fluid in a caustic scrubber.
8. The method of claim 7 , wherein the at least one impurity includes 3,3,3-trifluoropropene (1243zf) and, after said contacting step, an amount of 1243zf in the stream is reduced by at least 5 wt. % relative to an amount of 1243zf originally present in the stream.
9. A method for removing unsaturated halogenated impurities from 2,3,3,3-tetrafluoropropene (HFO-1234yf), comprising the steps of:
providing a stream of 1234yf containing at least one impurity selected from the group consisting of 3,3,3-trifluoropropene (1243zf), 1-chloro-1-fluoroethylene (1131a), vinyl chloride (1140), 1-chloro-2-fluoroethylene (1131), and combinations thereof;
contacting the stream with a basic scrubbing fluid in a caustic scrubber; and
thereafter, contacting the stream with an acidic scrubbing fluid in an acid scrubber.
10. The method of claim 9 , wherein the at least one impurity includes 3,3,3-trifluoropropene (1243zf) and, after said contacting step, an amount of 1243zf in the stream is reduced by at least 5 wt. % relative to an amount of 1243zf originally present in the stream.
11. The method of claim 9 , wherein the at least one impurity includes 1-chloro-1-fluoroethylene (1131a) and, after said contacting step, an amount of 1131a in the stream is reduced by at least 5 wt. % relative to an amount of 1131a originally present in the stream.
12. The method of claim 9 , wherein the at least one impurity includes vinyl chloride (1140) and, after said contacting step, an amount of 1140 in the stream is reduced by at least 5 wt. % relative to an amount of 1140 originally present in the stream.
13. The method of claim 9 , wherein the at least one impurity includes 1-chloro-2-fluoroethylene (1131) and, after said contacting step, an amount of 1131 in the stream is reduced by at least 5 wt. % relative to an amount of 1131 originally present in the stream.
14. The method of claim 9 , wherein the acidic scrubbing fluid is sulfuric acid having a concentration between 88 wt. % and 99 wt. %.
15. The method of claim 9 , wherein at least one of the following conditions are present within the acid scrubber:
a temperature between 0° C. and 70° C.; and
a contact time between the vapor stream and acidic scrubbing fluid of between 0.1 second and 200 seconds.
16. The method of claim 1 , wherein the following conditions are present within the acid scrubber:
a temperature between 20° C. and 30° C.; and
a contact time between the vapor stream and acidic scrubbing fluid of between 5 seconds and 50 seconds.
17. The method of claim 9 , wherein the following conditions are present within the acid scrubber:
a temperature between 20° C. and 30° C.; and
a contact time between the vapor stream and acidic scrubbing fluid of between 5 seconds and 50 seconds.