1,1,1,2,2-pentachloropropane

Conditions: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

Procedure: The overhead stream comprising 1,2,3-trichloropropane, TCPE, tetrachloropropanes, 1,1,2,2,3-pentachloropropane, 1,1,1,2,3-pentachloropropane, and 1,1,1,2,2-pentachloropropane is then provided to a reactor where it is dehydrochlorinated to provide dichloropropenes, trichloropropenes, 2,3,3,3-tetrachloropropene, and 1,1,2,3-tetrachloropropene. More specifically, dehydrochlorination reactor may typically be a batch or a continuous stirred tank reactor. The mixing can be done, e.g., by mechanical or jet mixing of feed streams. Those of ordinary skill in the art are readily able to determine the appropriate conditions at which to run a dehydrochlorination reactor in order to conduct the aforementioned dehydrochlorination. is then provided to a reactor where it

Conditions: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

Procedure: In operation of process 310, 1,1-dichloropropene is fed to chlorination reactor 302 and chlorinated in the presence of a catalytic amount of aluminum chloride to produce 1,1,1,2,2-pentachloropropane, 1,1,1,2-tetrachloropropane intermediate, and anhydrous HCl as a byproduct. The HCl and excess chlorine is fed to HCl purification unit 304 where anhydrous HCl is purified and taken as the overhead stream. The bottom stream comprising Cl2 is then recycled back to reactor 302. The bottom product stream of chlorination reactor 302, comprising 1,1,1,2,2-pentachloropropane, 1,1,1,2-tetrachloropropane, and heavies is quenched to remove aluminum chloride in the aqueous phase. The organic product is dried in drying unit 306 and the dried stream provided to separation unit 318.

Conditions: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

Procedure: The overhead stream comprising 1,2,3-trichloropropane, TCPE, tetrachloropropanes, 1,1,2,2,3-pentachloropropane, 1,1,1,2,3-pentachloropropane, and 1,1,1,2,2-pentachloropropane is then provided to a reactor where it is dehydrochlorinated to provide dichloropropenes, trichloropropenes, 2,3,3,3-tetrachloropropene, and 1,1,2,3-tetrachloropropene. More specifically, dehydrochlorination reactor may typically be a batch or a continuous stirred tank reactor. The mixing can be done, e.g., by mechanical or jet mixing of feed streams. Those of ordinary skill in the art are readily able to determine the appropriate conditions at which to run a dehydrochlorination reactor in order to conduct the aforementioned dehydrochlorination. is then provided to a reactor where it