Process for the separation of 2-chloro-1,1-difluoroethane and trans-dichloroethylene

US10227277B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10227277-B2
Application numberUS-201615551789-A
CountryUS
Kind codeB2
Filing dateFeb 15, 2016
Priority dateFeb 17, 2015
Publication dateMar 12, 2019
Grant dateMar 12, 2019

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Abstract

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The invention relates to the separation of a mixture comprising 2-chloro-1,1-difluoroethane (R142) and trans-dichloroethylene (TDCE) by extractive distillation and more particularly to a separation process wherein the TDCE is removed selectively by extractive distillation, thus leading to purified 2-chloro-1,1-difluoroethane.

First claim

Opening claim text (preview).

The invention claimed is: 1. A process for the separation of a mixture comprising 2-chloro-1,1-difluoroethane and trans-dichloroethylene by extractive distillation. 2. The separation process according to claim 1 , wherein the 2-chloro-1,1-difluoroethane/trans-dichloroethylene molar ratio before extractive distillation ranges from 2 to 100. 3. The separation process according to claim 1 , wherein the 2-chloro-1,1-difluoroethane/trans-dichloroethylene molar ratio after extractive distillation ranges from 9 to 99.999. 4. The separation process according to claim 1 , wherein the extractive distillation is carried out under a pressure ranging from 0.05 bar to 10 bar. 5. The separation process according to claim 1 , wherein the extractive distillation is carried out at a temperature ranging from −50° C. to 250° C. 6. The separation process according to claim 1 , wherein the extractive distillation is carried out using an extracting agent/product to be removed molar ratio ranging from 0.01 to 20. 7. The separation process according to claim 1 , wherein the mixture comprising 2-chloro-1,1-difluoroethane and trans-dichloroethylene originates from a fluorination reaction of 1,1,2-trichloroethane. 8. The separation process according to claim 1 , wherein an extraction agent is utilized, consisting of compounds having a boiling point greater than 35° C. 9. The separation process according to claim 1 , wherein an extraction agent is utilized, having a dipole moment less than or equal to 5 Debye. 10. The separation process according to claim 8 , wherein the separation factor of the 2-chloro-1,1-difluoroethane and trans-dichloroethylene in the extraction agent is greater than 1.1. 11. The separation process according to claim 8 , wherein the separation factor of the 2-chloro-1,1-difluoroethane and trans-dichloroethylene in the extraction agent is less than 1. 12. The separation process according to claim 8 , wherein the extraction agent is a hydrocarbon selected from the linear, branched or non-branched, cyclic or aromatic, saturated or unsaturated hydrocarbons, optionally substituted. 13. The separation process according to claim 12 , wherein the optionally substituted hydrocarbons have from 1 to 12 carbon atoms. 14. The separation process according to claim 12 , wherein the hydrocarbons are substituted with at least one substituent chosen from an oxygen atom, a nitrogen atom, a halogen atom, an alcohol group, an amine group. 15. The separation process according to claim 8 , wherein the extraction agent is chosen from the linear, branched, cyclic or aromatic hydrocarbons comprising from 6 to 8 carbon atoms. 16. The separation process according to claim 15 , wherein the extraction agent is chosen from hexane, cyclohexane, methylcyclohexane, n-heptane, octane, 2-methylpentane or toluene. 17. The separation process according to claim 8 , wherein the extraction agent is chosen from the halogenated hydrocarbons comprising from 2 to 4 halogen atoms. 18. The separation process according to claim 17 , wherein the halogenated hydrocarbons are chosen from tetrachloromethane, 1,1,2-trichloroethane, 1,1,1-trichloroethane, tetrachloroethene, 1,1,2,2-tetrachloroethane, 1,1,1,2-tetrachloroethane, trichloroethene, tribromomethane or triiodomethane, preferably 1,1,2-trichloroethane and tetrachloroethene. 19. The separation process according to claim 7 , wherein the extraction agent is 1,1,2-trichloroethane originating from said fluorination reaction.

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What does patent US10227277B2 cover?
The invention relates to the separation of a mixture comprising 2-chloro-1,1-difluoroethane (R142) and trans-dichloroethylene (TDCE) by extractive distillation and more particularly to a separation process wherein the TDCE is removed selectively by extractive distillation, thus leading to purified 2-chloro-1,1-difluoroethane.
Who is the assignee on this patent?
Arkema France
What technology area does this patent fall under?
Primary CPC classification C07C17/383. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Mar 12 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).