Claims
- 1. In the process of preparing bis-chloromethyl tetrachlorobenzene of the formula ##STR3## which comprises in a first stage contacting xylene with chlorine for formation of tetrachloroxylene, in the presence of FeCl.sub.3 or FeCl.sub.3.6H.sub.2 O as catalyst for the reaction, and in a second stage contacting the tetrachloroxylene with chlorine for formation of said tetrachlorobenzene in the presence of ultraviolet light or a compound which decomposes radially a radical catalyst for the second stage reaction, the improvement which comprises performing the second stage at a temperature of 60.degree.-85.degree. C. in the presence of the catalyst from the first stage and in the presence of hexamethylenetetramine for complexing with the catalyst, the weight ratio of hexamethylenetetramine to ferric chloride present in the second stage being from 0.1:1 to 2.5:1.
- 2. The process of claim 1, wherein an organic solvent is employed as the reaction medium.
- 3. Process of claim 2, wherein the organic solvent is carbon tetrachloride.
- 4. Process of claim 1, wherein the weight ratio of hexamethylenetetramine to ferric chloride present in the second stage is 1:1 to 2:1.
- 5. Process of claim 1, wherein the temperature for the first stage is -10.degree. to +40.degree. C.
- 6. Process of claim 1, wherein the xylene is overchlorinated and the chlorine content of the product of the second stage is 0.1 to 1.0 weight % higher than the theoretical chlorine content of said bis-chloromethyl tetrachlorobenzene.
- 7. Process of claim 1, wherein said tetrachlorobenzene is o-bis-chloromethyl tetrachlorobenzene and the xylene is o-xylene.
- 8. Process of claim 1, wherein said tetrachlorobenzene is m-bis-chloromethyl tetrachlorobenzene and the xylene is m-xylene.
- 9. Process of claim 1, wherein said tetrachlorobenzene is p-bis-chloromethyl tetrachlorobenzene and the xylene is p-xylene.
- 10. Process of claim 1, wherein the first and second stages are performed in a single reaction vessel.
- 11. Process of claim 1, wherein the bis-chloromethyl-tetrachlorobenzene is precipitated from the reaction medium and the precipitated product has a purity of 95-99%.
- 12. Process of claim 1, wherein the weight proportion of hexamethylenetetramine to the FeCl.sub.3 of the catalyst is 0.5:1 to 2.5:1.
- 13. Process of claim 1, wherein the amount of catalyst is 0.5 to 5% by weight with respect to the xylene.
Priority Claims (1)
Number |
Date |
Country |
Kind |
2556322 |
Dec 1975 |
DEX |
|
Parent Case Info
This is a continuation of application Ser. No. 003,553, filed Jan. 15, 1979, abandoned, which is a continuation of application Ser. No. 895,186, filed Apr. 10, 1978, abandoned, which is a continuation of application Ser. No. 748,266, filed Dec. 7, 1976, abandoned.
US Referenced Citations (2)
Continuations (3)
|
Number |
Date |
Country |
Parent |
3553 |
Jan 1979 |
|
Parent |
895186 |
Apr 1978 |
|
Parent |
748266 |
Dec 1976 |
|