1,1,1,2,3,3,3-heptafluoropropane

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

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

Procedure: According to another embodiment of the present invention, a 34 cubic centimeter Inconel™ reactor tube is equipped with a ceramic fiber heater. The reactor is purged with nitrogen between 150° C. and 200° C. The reactor is connected to tubing providing chlorine and the hydrofluorocarbon heptafluoropropane (HFC-227). The flow of the chlorine and HFC-227 is controlled with gas flowmeters. Table 3 below indicates the suggested reaction parameters as well as the expected results. Fluoromonomer precursor chloroheptafluoropropane (CFC-217) exiting the reactor is first passed through a 10% (wt./wt.) KOH solution and then dried over CaSO4, before being captured for subsequent gas chromatography analysis. the suggested reaction parameters as well as the expected results dried over CaSO4

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

Procedure: A 34 cubic centimeter Inconel™ reactor tube, equipped with a ceramic fiber heater, was packed with Takeda™ brand activated carbon. The activated carbon and reactor were purged with nitrogen between 150° C. and 200° C. The reactor was connected to tubing providing chlorine and the hydrofluorocarbon heptafluoropropane (HFC-227, containing 839 ppm 227ca and the remainder HFC-227ea). The flow of the chlorine and HFC-227 were controlled with gas flowmeters. Tables 1 and 2 below indicate the reaction parameters as well as the results. Fluoromonomer precursor chloroheptafluoropropane (CFC-217) exiting the reactor was first passed through a 10% (wt./wt.) KOH solution and then dried over CaSO4 before being captured for subsequent gas chromatography analysis. the reaction parameters as well as the results dried over CaSO4

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

Procedure: A 34 cubic centimeter Inconel™ reactor tube, equipped with a ceramic fiber heater, was packed with Takeda™ brand activated carbon. The activated carbon and reactor were purged with nitrogen between 150° C. and 200° C. The reactor was connected to tubing providing chlorine and the hydrofluorocarbon heptafluoropropane (HFC-227, containing 839 ppm 227ca and the remainder HFC-227ea). The flow of the chlorine and HFC-227 were controlled with gas flowmeters. Tables 1 and 2 below indicate the reaction parameters as well as the results. Fluoromonomer precursor chloroheptafluoropropane (CFC-217) exiting the reactor was first passed through a 10% (wt./wt.) KOH solution and then dried over CaSO4 before being captured for subsequent gas chromatography analysis. the reaction parameters as well as the results dried over CaSO4

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

Procedure: 2-Chloroheptafluoropropane (1.38 g/hr) and hydrogen (22 cc/min) were fed into the 1/4" Inconel® nickel alloy reactor filled with Inconel® nickel alloy chips (10 g). Operation at 500° C. and 250 psig for 33.3 hours gave an average of 91.3% conversion with 99.4% selectivity to CF3CHFCF3.

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

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

Procedure: 2-Chloroheptafluoropropane (1.38 g/hr) and hydrogen (22 cc/min) were fed into the 1/4" Inconel® nickel alloy reactor filled with Inconel® nickel alloy chips (10 g). Operation at 500° C. and 250 psig for 33.3 hours gave an average of 91.3% conversion with 99.4% selectivity to CF3CHFCF3.

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

Procedure: 2-Chloroheptafluoropropane (1.38 g/hr) and hydrogen (22 cc/min) were fed into the 1/4" Inconel® nickel alloy reactor filled with Inconel® nickel alloy chips (10 g). Operation at 500° C. and 250 psig for 33.3 hours gave an average of 91.3% conversion with 99.4% selectivity to CF3CHFCF3.

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

Procedure: A vapor plug flow reactor ½″ diameter×3′ long Monel® pipe is fed with 1 g/min of the hexafluoro-2-propanol and 150 cc/min of elemental fluorine at ambient conditions to produce 1,1,1,2,3,3,3 heptafluoropropane in greater than 90% yield.

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

Procedure: reacting 1,1,1,3,3,3-hexafluoropropane with an effective amount of elemental fluorine in an inert gas, in a mole ratio of 1,1,1,3,3,3-hexafluoropropane to elemental fluorine of from about 1:1 to about 50:1, at a temperature of from about 0° to about 200° C. and for a reaction time of from about 0.1 seconds to about 72 hours, to produce a 1,1,1,2,3,3,3-heptafluoropropane product comprising 1,1,1,2,3,3,3-heptafluoropropane, unreacted starting materials and byproducts;

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

Procedure: reacting 1,1,1,3,3,3-hexafluoropropane with an effective amount of elemental fluorine in an inert gas, in a mole ratio of 1,1,1,3,3,3-hexafluoropropane to elemental fluorine from about 1:2 to about 100:1, at a temperature of from about -20° to about 400° C. and for a reaction time of from about 0.1 seconds to about 72 hours, to produce a 1,1,1,2,3,3,3-heptafluoropropane product comprising 1,1,1,2,3,3,3-heptafluoropropane, unreacted starting materials and byproducts; and

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

Procedure: 2-Chloroheptafluoropropane (1.38 g/hr) and hydrogen (22 cc/min) were fed into the 1/4" Inconel® nickel alloy reactor filled with Inconel® nickel alloy chips (10 g). Operation at 500° C. and 250 psig for 33.3 hours gave an average of 91.3% conversion with 99.4% selectivity to CF3CHFCF3.