Chlorinolysis process for producing carbon tetrachloride

1. A chlorinolysis process for producing carbon tetrachloride comprising providing a chlorination zone at an operating temperature of from 400 to 600° C. with i) chlorine, ii) a C 1 chlorinated compound comprising 1 to 3 chlorine atoms, and iii) a carbon/second chlorine source to produce a reaction mixture, and, after a residence time, extracting a product mixture from the chlorination zone, the product mixture comprising carbon tetrachloride and optionally perchloroethylene, wherein the product mixture comprises a higher molar content of carbon tetrachloride than perchloroethylene, if present.

2. The process of claim 1 , wherein the C 1 chlorinated compound comprising 1 to 3 chlorine atoms comprises chloroform, methylene chloride, methyl chloride, or mixtures thereof.

3. The process of claim 1 , wherein the carbon/second chlorine source comprises purified optionally chlorinated alkane alkene materials having a purity level of at least about 60% by weight.

4. The process of claim 3 , wherein the carbon/second chlorine source is selected from the group consisting of methane, ethane, ethene, propane, propene, dichloroethane, dichloropropane, and any combination thereof.

5. The process of claim 1 , wherein the carbon/second chlorine source comprises unpurified materials.

6. The process of claim 1 , wherein the carbon/second chlorine source comprises: a. phosphorous containing compounds in an amount of 5000 ppm (0.5%) or less; b. oxygen containing compounds in an amount of 5000 ppm (0.5%) or less; c. iron in an amount of 5000 ppm (0.5%) or less and/or, d. water in an amount of 1000 ppm (0.1%) or less.

7. The process of claim 1 , wherein the carbon/second chlorine source comprises byproduct material from processes for preparing chlorinated alkanes, chlorinated alkenes, or both.

8. The process of claim 7 , wherein the chlorinated alkanes, chlorinated alkenes, or both are selected from the group consisting of carbon tetrachloride, 1,1,1,2,3-pentachloropropane, 1,1,1,3,3-pentachloropropane, 1,1,2,2,3-pentachloropropane, 1,1,2,3-tetrachloropropene, 1,1,3-trichloropropene, 1,1,1,3-tetrachloropropane, 1,1,1,3-tetrachloropropene, 1,1,3,3-tetrachloropropene, 2,3,3,3-tetrachloropropene, and 1,3,3,3-tetrachloropropene.

9. The process of claim 7 , wherein the byproduct material comprises heavy ends material, light ends material, or both.

10. The process of claim 1 , wherein the carbon/second chlorine source comprises one, two, three, four, five or more optionally chlorinated alkane or chlorinated alkene compounds.

11. The process of claim 1 , wherein the carbon/second chlorine source comprises carbon tetrachloride and one or more alkanes and/or alkenes and/or chlorinated alkanes and/or chlorinated alkenes having a boiling point differing from the boiling point of carbon tetrachloride by about 10° C. or less.

12. The process of claim 1 , wherein the carbon/second chlorine source comprises methane, ethane, or both.

13. The process of claim 1 , wherein the carbon/second chlorine source comprises chlorinated C 1-6 compounds obtained from the chlorination of C 1-6 non-chlorinated saturated and unsaturated hydrocarbons having a content of C 1 compounds greater than 75% mol. or 75% vol.

14. The process of claim 1 , where the molar ratio of carbon tetrachloride:perchloroethylene produced in the chlorination zone is 20:1, 10:1 or 5:1 to 3:1, 2:1 or 1:1.

15. The process of claim 1 , wherein the operating temperature of the chlorination zone is 400° C. to 550° C.

16. The process of claim 1 , wherein the mean residence time of the reaction mixture in the chlorination zone is at least 5 seconds.

17. The process of claim 1 , wherein a content of hexa-chlorinated organic compounds in the product mixture is 2% or less by weight of the net carbon tetrachloride and perchloroethylene produced in the chlorination zone.

18. The process of claim 1 , further comprising quenching the product mixture extracted from the chlorination zone.

19. The process of claim 1 , further comprising subjecting the product mixture extracted from the chlorination zone to one or more distillation steps.

20. The process of claim 19 , wherein a stream rich in carbon tetrachloride is obtained from the one or more distillation steps.

21. The process of claim 20 , wherein the stream rich in carbon tetrachloride has a purity level of 99.9% or higher.

22. The process of claim 1 , wherein a number of carbon atoms in the carbon tetrachloride and perchloroethylene produced in the chlorination zone is more than 95% of the number of atoms in the ii) C 1 chlorinated compound comprising 1 to 3 chlorine atoms and iii) the carbon/second chlorine source.

23. The process of claim 1 , wherein the molar ratio of HCl produced in the chlorination zone:carbon tetrachloride plus perchloroethylene produced in the chlorination zone is lower than 2.5:1, lower than 2:1, lower than 1.5:1, or lower than 1.1:1.

24. The process of claim 1 , wherein the ratio by mass of carbon tetrachloride:perchloroethylene produced in the chlorination zone ranges from 1:100 to 100:0.1, or from 1:10 to 100:1, or from 1:5 to 5:1, or from 1:2 to 2:1.

25. The process of claim 1 , wherein the chlorination zone is exposed to UV/visible light.

26. The process of claim 1 , further comprising adding the carbon tetrachloride produced in the chlorination zone as a feedstock in a downstream process, wherein the downstream process produces a stream comprising optionally chlorinated organic compounds, and said stream is recycled hack to the chlorination zone for use as the carbon/second chlorine source.

27. The process of claim 1 , wherein a crude carbon tetrachloride composition is obtained, and at least a portion of said composition is recycled hack to the chlorination zone.

28. The process of claim 1 , wherein a crude carbon tetrachloride composition is produced and the produced composition is added as a feedstock in a downstream process for the production of chlorinated organic compounds, fluorinated organic compounds, or both.