Process for the production of chlorinated propenes

Patent metadata

Field	Value
Publication number	US-9382176-B2
Application number	US-201414770860-A
Country	US
Kind code	B2
Filing date	Feb 27, 2014
Priority date	Feb 27, 2013
Publication date	Jul 5, 2016
Grant date	Jul 5, 2016

Abstract

Processes for the production of chlorinated propenes are provided. The processes proceed through the production of cyclic intermediate that is thereafter readily converted to a desired chloropropane, e.g., via selective pyrolysis. The process may be conducted using starting materials that are readily commercially available and/or that may be reacted safely in standard laboratory equipment so that capital cost savings may be seen. The process does not require the use of catalysts and yet, process conditions less extreme than many conventional processes for the production of chlorinated propenes are suitable, so that raw material and utility cost savings are also possible.

First claim

The invention claimed is:

1. A process for the production of chlorinated propenes, comprising reacting vinylidene chloride with sodium trichloroacetate and/or chloroform, or, reacting perchloroethylene with diazomethane to provide 1,1,2,2,-tetrachlorocyclopropane and converting the 1,1,2,2,-tetrachlorocyclopropane to the desired chlorinated propene.

2. The process of claim 1 , wherein the sodium trichloroacetate, chloroform or diazomethane generate a carbene in situ.

3. The process of claim 2 , wherein the carbene comprises methylene, dichlorocarbene, or a combination of these.

4. The process of claim 1 , comprising reacting chloroform and vinylidene chloride.

5. The process of claim 1 , wherein the chloroform is preheated to a temperature of from 250° C. to 400° C.

6. The process of claim 4 wherein the chloroform and vinylidene chloride are passed through a hot tube reactor.

7. The process of claim 6 , wherein the chloroform and vinylidene chloride are mixed prior to being heated above 400° C.

8. The process of claim 6 , wherein the hot tube reactor is operated at temperatures of from 400° C. to 600° C.

9. The process of claim 6 , wherein the hot tube reactor is operated at pressures of from 0-10 psig.

10. The process of claim 6 , further comprising passing a carrier gas through the hot tube reactor.

11. The process of claim 2 , wherein the 1,1,2,2,-tetrachlorocyclopropane is prepared in the liquid phase from sodium trichloroacetate and vinylidene chloride.

12. The process of claim 1 , wherein the chlorinated propene comprises 1,1,2,3-tetrachloropropene.

13. A continuous process for the production of chlorinated propenes, comprising passing vinylidene chloride and chloroform through a hot tube reactor to provide 1,1,2,2,-tetrachlorocyclopropane and converting the 1,1,2,2,-tetrachlorocyclopropane to the desired chlorinated propene, wherein the cyclopropane is prepared from reactants comprising chloroform and vinylidene chloride which are passed through a hot tube reactor.

Assignees

• Blue Cube Ip Llc

Inventors

• Grandbois Matthew L
• Murdoch Brian
• Meyer Matthew M

Classifications

• C07C17/358

  by isomerisation · CPC title

• C07C17/278

  of only halogenated hydrocarbons · CPC title

• C07C23/04

  with a three-membered ring · CPC title

• C07C2101/02

  Chemistry & Metallurgy · mapped topic

• C07C17/269 Primary

  of only halogenated hydrocarbons · CPC title