Process for production of 2,3-dichlorobutadiene-1,3
View Patent ↗Purified chlorinated alkenes are produced by a process in which a mixture of i) a first chlorinated alkene that has at least one beta-chlorine substituent and no alpha-chlorine substituents and ii) a second chlorinated alkene that has at least one alpha-chlorine substituent is contacted with chlorine in an amount sufficient to further chlorinate the second chlorinated alkene, but which is insufficient to cause conversion of more than 20% of the first chlorinated alkene. The resultant reaction product may be easily enriched to provide a chlorinated alkene product wherein a) the weight percentage of chlorinated alkenes having at least one beta-chlorine substituent and no alpha-chlorine substituents, based on the total weight of the chlorinated alkenes present in the enriched chlorinated alkene product compared to b) the weight percentage of chlorinated alkenes having at least one beta-chlorine substituent and no alpha-chlorine substituents, based on the total weight of the chlorinated alkenes present in the mixture prior to chlorination is increased by at least 0.25 wt. %.
1. A process for production of a purified chlorinated olefin composition, the process comprising the steps of:
A. providing a first composition comprising a mixture of a) a chlorinated alkene having at least one beta-chlorine substituent and no alpha-chlorine substituents and b) a chlorinated alkene having at least one alpha-chlorine substitutent;
B. contacting said first composition with chlorine having a purity of at least 96% in an amount sufficient to further chlorinate said chlorinated alkene having at least one alpha-chlorine substituent but insufficient to cause conversion of more than 20% of said chlorinated alkene having at least one beta-chlorine substituent and no alpha-chlorine substituents to more highly chlorinated species, thereby producing a reaction product; and
C. isolating from said reaction product a second composition which is a chlorinated olefin composition wherein i) the weight percentage of chlorinated alkenes having at least one beta-chlorine substituent and no alpha-chlorine substitutents, based on the total weight of the chlorinated alkenes present in the second composition compared to ii) the weight percentage of chlorinated alkenes having at least one beta-chlorine substituent and no alpha-chlorine substituents, based on the total weight of the chlorinated alkenes present in the first composition is increased by at least 0.25 wt. %.
2. A process of claim 1 wherein the first composition comprises the product of a dehydrochlorination reaction.
3. A process of claim 1 wherein the chlorinated olefin composition that is isolated comprises a chlorinated alkene selected from the group consisting of 2-chlorobutadiene-1,3 and 2,3-dichlorobutadiene-1,3.
4. A process of claim 1 wherein the first composition comprises a chlorinated butene.
5. A process of claim 3 wherein the chlorinated alkene is 2-chlorobutadiene-1,3.
6. A process of claim 3 wherein the chlorinated alkene is 2,3-dichlorobutadiene-1,3.
7. A process of claim 1 wherein the first composition is contacted with chlorine in the presence of an ionic catalyst.
8. A process of claim 1 wherein the first composition is contacted with chlorine in a plug flow reactor.
9. A process of claim 1 wherein the first composition is contacted with chlorine in a batch reactor.
10. A process of claim 1 wherein the weight of chlorinated alkene having at least one beta-chlorine substituent and no alpha-chlorine substituents is increased by at least 0.5 wt. %.
11. A process of claim 1 wherein the weight of chlorinated alkene having at least one beta-chlorine substituent and no alpha-chlorine substituents is increased by at least 5 wt. %.