1,1,1-trifluoroethane

Conditions: temp:0.00; pressure:0.00; stir:

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

Procedure: From the above results, it is believed that the reaction of HCFC-133a into HFC-134a occurs predominantly and HFC-143a and HFC-125 are produced from a side reaction in the first reactor, whereas the reaction of TCE into HCFC-133a is predominant but production of HFC-134a from HFC-134a is little in the second reactor.

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

Procedure: From the above results, it is believed that the reaction of HCFC-133a into HFC-134a occurs predominantly and HFC-143a and HFC-125 are produced from a side reaction in the first reactor, whereas the reaction of TCE into HCFC-133a is predominant but production of HFC-134a from HFC-134a is little in the second reactor.

Conditions: temp:0.00; pressure:0.00; stir:

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

Procedure: An alternative approach to HCFC's is the chlorination of fluorocarbons such as CH3CF3 (HFC-143a). For example, McBee (Industrial and Engineering Chemistry, Vol. 39, pp. 409-412 (1947)) reported that vapor phase chlorination of HFC-143a afforded a mixture of HCFC-133a, HCFC-132b, CHCl2CF3 (HCFC-123), and the fully chlorinated CF3CCl3 (CFC-113a). McBee also reported the chlorination of CH3CClF2 (HCFC-142b) to give HCFC-132b, HCFC-122, and the fully chlorinated CClF2CCl3 (CFC-112a). Again, using this technique --CH2Cl and --CHCl2 groups dominate the attainable substitution pattern. afforded

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

Procedure: From the above results, it is believed that the reaction of HCFC-133a into HFC-134a occurs predominantly and HFC-143a and HFC-125 are produced from a side reaction in the first reactor, whereas the reaction of TCE into HCFC-133a is predominant but production of HFC-134a from HFC-134a is little in the second reactor.