IP Library Granted Patent US 8,722,946
Granted Patent B2
US 8,722,946 · App. 13/481,111 · Granted May 13, 2014

Method for avoiding the generation of by-products during the production of haloalkane compounds

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Quick Facts
Patent No.
US 8,722,946
App. No.
13/481,111
Granted
May 13, 2014
Kind
B2
Abstract

Disclosed is a process for the manufacture of haloalkane compounds, and more particularly, to an improved process for the manufacture of the compound 1,1,1,3,3-pentachloropropane (HCC-240fa), which mitigates the formation of by-products. The present invention is also useful in the manufacture of other haloalkane compounds such as HCC-250 and HCC-360. One embodiment of the process comprises a method and system for avoiding the formation of polyvinyl chloride during the production of HCC-240fa from CCl 4 , in which vinyl chloride (VCM) is fed into a reactor as a vapor instead of as a liquid, using a diffusing device to further increase the contact surface between VCM vapor and CCl 4 .

Claims (24)

1. A process for the manufacture of haloalkane compounds comprising reacting carbon tetrachloride and an alkene wherein poly(alkene) by-products are minimized during the reaction by the use of a diffusing device with an iron catalyst and one or more organo-phosphate compounds as a co-catalyst;

wherein the alkene is selected from the group consisting of vinyl chloride, ethylene and 2-chloropropene; and

wherein the haloalkane compounds are selected from the group consisting of HCC-240fa, HCC-250 and HCC-360; and wherein the diffusing device increases the contact surface between the reactants.

2. The process of claim 1 , wherein the iron catalyst has a form selected from the group consisting of iron powder, iron balls, iron wire, iron shavings, and mixtures thereof.

3. The process of claim 2 , wherein the iron powder comprises a fine powder of pure metallic iron.

4. The process of claim 3 , wherein the iron powder has a particle size smaller than 325 mesh.

5. The process of claim 3 , wherein the iron powder is added to the reactor by powder slurry in carbon tetrachloride.

6. The process of claim 3 , wherein the iron powder is added to the reactor by powder slurry in the organophosphate.

7. The process of claim 3 , wherein the iron powder is added to the reactor by powder slurry in a mixture of CCl 4 and the organophosphate.

8. The process of claim 1 , wherein the organophosphate co-catalyst is selected from the group consisting of triphenylphosphate, tributylphosphate, trimethyl-phosphate, triethylphosphate, tripropylphosphate, and mixtures of two or more of these.

9. The process of claim 1 , which is conducted as a continuous operation.

10. The process of claim 1 , which is conducted as a batch operation.

11. The process of claim 1 , wherein the diffusing device comprises a dip tube.

12. The process of claim 1 , wherein the diffusing device comprises a sponge type gas diffuser.

13. An improved process for manufacturing HCC-240fa, which comprises:

(a) providing a continuous CCl 4 liquid stream and a continuous VCM vapor stream;

(b) producing a product stream in a reactor by reacting carbon tetrachloride and vinyl chloride in the presence of a catalyst mixture consisting of iron metal and tributylphosphate under conditions sufficient to produce HCC-240fa and not produce significant amounts of PVC by the use of a diffusing device, wherein the diffusing device increases the contact surface between the reactants; and

(c) recovering HCC-240fa from said product stream of step (b).

14. The process of claim 13 , wherein the VCM vapor is fed into a reactor precharged with CCl 4 , tributylphosphate and iron powder through a dip tube.

15. The process of claim 13 , wherein the VCM vapor is fed into a reactor precharged with CCl 4 , tributylphosphate and iron powder through a sponge type gas diffuser.

16. The process of claim 13 , wherein the iron powder has a particle size smaller than 325 mesh.

17. The process of claim 13 , wherein the iron powder is added to the reactor by powder slurry in carbon tetrachloride.

18. The process of claim 13 , wherein the iron powder is added to the reactor by powder slurry in the tributylphosphate.

19. The process of claim 13 , wherein the iron powder is added to the reactor by powder slurry in a mixture of CCl 4 and the tributylphosphate.

Assignments (2)
SECURITY INTEREST Recorded Jan 12, 2026
From: SOLSTICE ADVANCED MATERIALS US, INC.
To: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 074569/0260 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 25, 2012
From: CLOSE, JOSHUA; WANG, HAIYOU; TUNG, HSUEH SUNG
To: HONEYWELL INTERNATIONAL INC.
Reel/Frame 028272/0539 →