Refrigerant compositions and use thereof in systems using flooded evaporators

1 . A method for retrofitting an existing heat transfer system selected from refrigerant systems, air conditioning systems and chiller systems, said method comprising:

(a) providing an existing vapor compression system comprising:

(i) a refrigerant in the existing vapor compression system, said refrigerant being selected from the group consisting of R-22, R404A, and R507A;

(ii) a compressor having a compressor inlet receiving refrigerant vapor at a first pressure and a compressor outlet discharging refrigerant vapor at second pressure higher than said first pressure;

(iii) a condenser which receives said refrigerant vapor discharged from said compressor and which transfers heat out of said refrigerant vapor to produce liquid refrigerant;

(iv) a pressure reducing device which receives liquid refrigerant from said condenser and produces a mixture of liquid refrigerant and refrigerant vapor at a pressure below said second pressure; and

(v) a flooded evaporator receiving: (1) said mixture of liquid refrigerant and refrigerant vapor from said an expansion device, wherein said flooded evaporator produces refrigerant vapor feeding said compressor inlet;

(b) removing at least a substantial portion of the existing refrigerant from the existing vapor compression system; and

(c) after said removing step, adding to said existing vapor compression system a new refrigerant consisting essentially of:

(i) from about 25% to about 45% by weight of 1,1,1,2-tetrafluoroethane (HFC-134a);

(ii) from 25% to about 35% by weight of trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E)) and/or 2,3,3,3-tetrafluoropropene (HFO-1234yf); and

(iii) from about 37% to about 46% by weight of a combination of difluoromethane (HFC-32) and pentafluoroethane (HFC-125), provided that the weight ratio of HFO-32:HFC-125 is from about 1.21:1 to about 0.8:1,

and further provided that said refrigerant is a non-flammable refrigerant and that said refrigerant has a GWP of 1350 or less;

(d) after said adding step, evaporating at least a portion of said new refrigerant from the liquid phase to the vapor phase in said flooded evaporator; and

(e) operating said existing vapor compression system with said new refrigerant at a capacity of at least about 90% relative to R-22 in said vapor compression system and wherein said compressor has a power consumption that is less than about 120% of the power consumption of R-22 in said existing vapor compression system.

2 . The method of claim 1 wherein said new refrigerant consists essentially of

(i) from about 30% to about 45% by weight of 1,1,1,2-tetrafluoroethane (HFC-134a);

(ii) from 25% to about 35% by weight of a combination of trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E)) and 2,3,3,3-tetrafluoropropene (HFO-1234yf), provided that the weight ratio of HFO-1234yf:HFO-1234ze(E) is from about 5:1 to about 2:1; and

(iii) from about 40% to about 46% by weight of a combination of difluoromethane (HFC-32) and pentafluoroethane (HFC-125), provided that the weight ratio of HFO-32:HFC-125 is from about 1.21:1 to about 0.8:1.

3 . The method of claim 1 , wherein said new refrigerant consists essentially of:

(i) about 31% by weight of 1,1,1,2-tetrafluoroethane (HFC-134a);

(ii) about 27% by weight of a combination of trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E)) and 2,3,3,3-tetrafluoropropene (HFO-1234yf), provided that the weight ratio of HFO-1234yf:HFO-1234ze(E) is from about 5:1 to about 2:1; and

(iii) about 42% by weight of a combination of difluoromethane (HFC-32) and pentafluoroethane (HFC-125), provided that the weight ratio of HFO-32:HFC-125 is from about 1.21:1 to about 0.8:1.

4 . The method of claim 1 , wherein said new refrigerant consists essentially of:

(i) about 25% to about 31% by weight of 1,1,1,2-tetrafluoroethane (HFC-134a);

(ii) from 27% to about 32% by weight of a combination of trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E)) and optionally 2,3,3,3-tetrafluoropropene (HFO-1234yf), provided that the refrigerant comprises at least 6.5% by weight of 1234ze(E);

(iii) about 22% by weight of difluoromethane (HFC-32); and

(iv) about 22% by weight of pentafluoroethane (HFC-125), provided that said refrigerant is a non-flammable refrigerant.

5 . The method of claim 1 , wherein said new refrigerant consists essentially of:

(i) about 29% by weight of 1,1,1,2-tetrafluoroethane (HFC-134a);

(ii) about 31% by weight of 2,3,3,3-tetrafluoropropene (HFO-1234yf),

(iii) about 20% by weight of difluoromethane (HFC-32); and

(iv) about 20% by weight of pentafluoroethane (HFC-125).

6 . The method of claim 1 , wherein said new refrigerant consists essentially of:

(i) about 31% by weight of 1,1,1,2-tetrafluoroethane (HFC-134a);

(ii) about 20% by wight of 2,3,3,3-tetrafluoropropene (HFO-1234yf);

(iii) about 7% by weight of trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E));

(iv) about 21% by weight of difluoromethane (HFC-32); and

(v) about 21% by weight of pentafluoroethane (HFC-125).

7 . The method of claim 1 , wherein said new refrigerant consists essentially of:

(i) about 26% by weight of 1,1,1,2-tetrafluoroethane (HFC-134a);

(ii) about 18% by wight of 2,3,3,3-tetrafluoropropene (HFO-1234yf);

(iii) about 14% by weight of trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E));

(iv) about 21% by weight of difluoromethane (HFC-32); and

(v) about 21% by weight of pentafluoroethane (HFC-125).

8 . The method of claim 1 , wherein said new refrigerant consists essentially of:

(i) about 25% by weight of 1,1,1,2-tetrafluoroethane (HFC-134a);

(ii) about 11% by weight of 2,3,3,3-tetrafluoropropene (HFO-1234yf);

(iii) about 20% by weight of trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E));

(iv) about 22% by weight of difluoromethane (HFC-32); and

(v) about 22% by weight of pentafluoroethane (HFC-125).

9 . The method of claim 1 , wherein said new refrigerant consists essentially of:

(i) about 25% by weight of 1,1,1,2-tetrafluoroethane (HFC-134a);

(ii) about 29% by weight of trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E));

(iii) about 23% by weight of difluoromethane (HFC-32); and

(v) about 23% by weight of pentafluoroethane (HFC-125).

10 . The method of claim 1 wherein said existing vapor compression system comprises: (1) an accumulator which receives said mixture f liquid refrigerant and said refrigerant vapor from said pressure reducing device, separates said refrigerant vapor from said liquid refrigerant, and produces a liquid refrigerant stream and a refrigerant vapor stream, wherein said refrigerant vapor from said accumulator feeds said compressor inlet, and (2) a liquid pomp which receives said liquid refrigerant from said accumulator and directs said liquid refrigerant to said flooded evaporator.

11 . A refrigerant composition consisting essentially of: (a) from about 25% to about 31% by weight of 1,1,1,2-tetrafluoroethane (HFC-134a); (b) from about 27% to about 32% by weight of trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E)) and/or 2,3,3,3-tetrafluoropropene (HFO-1234yf), provided that the composition comprises no more than about 22 wt % of HFO-1234yf; and (c) from 41.5% to about 46% by weight of a combination of difluoromethane (HFC-32) and pentafluoroethane (HFC-125), provided that the weight ratio of HFO-32:HFC-125 is from about 1.21:1 to about 0.8:1.

12 . The refrigerant of claim 11 , further provided that the composition comprises at least about 6.5% by weight of HFO-1234ze(E).

13 . A method for cooling comprising:

(a) providing a compression refrigeration system comprising: (i) a liquid refrigerant and gaseous a refrigerant; (ii) a compressor receiving said gaseous refrigerant at a first pressure and producing gaseous refrigerant at second pressure above said first pressure; (ii) a condenser which receives gaseous refrigerant exiting said compressor and which rejects heat from said gaseous refrigerant to produce said liquid refrigerant; (iii) a pressure reducer receiving said liquid refrigerant from said condenser and producing a mixture of said liquid and said gaseous refrigerant at a pressure below said second pressure; (iv) optionally an accumulator which receives said mixture from said pressure reducer and separates said gaseous refrigerant from said liquid refrigerant and produces a liquid refrigerant stream and a gaseous refrigerant stream which flows to the low pressure side of said compressor; and (v) a flooded evaporator receiving said liquid refrigerant from said pressure reducer and/or said accumulator when present and producing said gaseous refrigerant which flows to the low pressure side of said compressor and/or to the accumulator when present;

(b) evaporating said liquid refrigerant in said flooded evaporator to produce vaporous refrigerant, wherein: (1) said liquid refrigerant in said flooded evaporator consists essentially of, on a weight basis with a tolerance of +/−0.5%: (i) from 22.8% to 41.5% of HFC-134a; (ii) from 20.7% to 23% of HFO-1234yf; (iii) from 7.7% to 10.9% of HFO-1234ze(E); (iv) from 11.6% to 23.6% of HFC-32; and (iv) 15.1% to 25.0% of HFC-125; and (2) said vaporous refrigerant in said flooded evaporator consists essentially of, on a weight basis with a tolerance of +/−0.5%: (i) from 11.5% to 27.1% of HFC-134a; (ii) from 15.7% to 19.3% of HFO-1234yf; (iii) from 3.4% to 5.7% of HFO-1234ze(E); (iv) from 24.8% to 23.6% of HFC-32; and (iv) 23.3% to 31.1% of HFC-125; and

(c) operating said system at a capacity of at least about 90% relative to R-22 in said system and wherein said compressor has a power consumption that is less than about 115% of the power consumption of R-22 in said system.

14 . The method of claim 13 wherein: (1) said liquid refrigerant in said flooded evaporator consists essentially of, on a weight basis with a tolerance of +/−0.5%: (i) from 33.3% to 41.5% of HFC-134a; (ii) from 20.7% to 21.8% of HFO-1234yf; (iii) from 7.7% to 10.4% of HFO-1234ze(E); (iv) from 11.6% to 18.5% of HFC-32; and (v) 15.1% to 19.8% of HFC-125; and (2) said vaporous refrigerant in said flooded evaporator consists essentially of, on a weight basis with a tolerance of +/−0.5%: (i) from 18.6% to 27.1% of HFC-134a; (ii) from 16.9% to 19.3% of HFO-1234yf; (iii) from 3.7% to 5.7% of HFO-1234ze(E); (iv) from 24.8% to 33.6% of HFC-32; and (v) 23.3% to 27.2% of HFC-125.

15 . The method of claim 13 wherein: (1) said liquid refrigerant in said flooded evaporator consists essentially of, on a weight basis with a tolerance of +/−0.5%: (i) from 31.2% to 39.2% of HFC-134a; (ii) from 32.3% to 35.0% of HFO-1234yf; (iii) from 11.1% to 17.6% of HFC-32; and (iv) 14.8% to 18.9% of HFC-125; and (2) said vaporous refrigerant in said flooded evaporator consists essentially of, on a weight basis with a tolerance of +/−0.5%: (i) from 11.5% to 17.7% of HFC-134a; (ii) from 15.7% to 18.6% of HFO-1234yf; (iii) from 3.4% to 5.5% of HFO-1234ze(E); (iv) from 30.1% to 38.3% of HFC-32; and (iv) 28.2% to 31.1% of HFC-125.

16 . The method of claim 13 wherein said liquid refrigerant evaporates in said flooded evaporator at a temperature of from about −65° C. up to and including about 0° C.

17 . The method of claim 13 wherein said liquid refrigerant evaporates in said flooded evaporator at a temperature of from about −20° C. up to and including about 20° C.

18 . The method of claim 13 wherein said liquid refrigerant evaporates in said flooded evaporator at an average temperature of from about −40° C. to less than about −12° C.

19 . The method of claim 13 wherein said liquid refrigerant evaporates in said flooded evaporator at an average temperature of from about −35° C. to about −25° C.

20 . The method of claim 13 wherein said system operates with a capacity in said system that is at least 95% of the capacity of R-22 in said system.

21 . The method of claim 20 wherein said system operates with a power consumption that is 110% or less than the power consumption of R-22 in said system.

22 . The method of claim 13 wherein said existing vapor compression system further comprises an accumulator, wherein said accumulator: (1) receives said mixture of liquid refrigerant and said gaseous refrigerant from said pressure reducer, separates said gaseous refrigerant from said liquid refrigerant, and produces a liquid refrigerant stream and a gaseous refrigerant stream, wherein said refrigerant vapor from said accumulator feeds said compressor inlet; and (2) a liquid pump which receives said liquid refrigerant from said accumulator and directs said liquid refrigerant to said flooded evaporator.