Method for heating and/or air-conditioning in a vehicle
A method for heating and/or air-conditioning in a motor vehicle interior by means of a reversible refrigeration loop in which a refrigerant fluid circulates, said fluid including: between 4 and 6 wt. % of difluoromethane (HFC-32); between 2.5 and 3.5 wt. % of pentafluoroethane (HFC-125); and between 91 and 93.5 wt. % of tetrafluoropropene, preferably 2,3,3,3-tetrafluoropropene.
1. A process for heating and/or air conditioning a motor vehicle passenger compartment using a reversible refrigerating loop, in which a refrigerant circulates, comprising a first heat exchanger, an expansion valve, a second heat exchanger, a compressor and means for inversion of the operation of the reversible refrigerating loop, wherein the refrigerant comprises:
from 4% to 6% by weight of difluoromethane;
from 2.5% to 3.5% by weight of pentafluoroethane; and
from 91% to 93.5% by weight of tetrafluoropropene.
2. The process as claimed in claim 1 , in which the refrigerant comprises:
from 4.5% to 5.5% by weight of difluoromethane;
from 2.5% to 3.5% by weight of pentafluoroethane; and
from 91% to 93% by weight of tetrafluoropropene.
3. The process as claimed in claim 1 , in which the refrigerant comprises:
from 4.5% to 5.5% by weight of difluoromethane;
from 2.5% to 3.5% by weight of pentafluoroethane; and
from 91.5% to 93% by weight of tetrafluoropropene.
4. The process as claimed in claim 1 , in which the refrigerant comprises:
from 4.5% to 5.5% by weight of difluoromethane;
from 3% to 3.5% by weight of pentafluoroethane; and
from 91% to 92% by weight of tetrafluoropropene.
5. The process as claimed in claim 4 , in which the tetrafluoropropene is 2,3,3,3-tetrafluoropropene.
6. The process as claimed in claim 1 , in which the refrigerant is chosen from the group consisting of:
5% by weight of difluoromethane, 3.3% by weight of pentafluoroethane and 91.7% by weight of tetrafluoropropene;
5% by weight of difluoromethane, 3% by weight of pentafluoroethane and 92% by weight of tetrafluoropropene;
5% by weight of difluoromethane, 3.1% by weight of pentafluoroethane and 91.9% by weight of tetrafluoropropene;
5% by weight of difluoromethane, 3.2% by weight of pentafluoroethane and 91.8% by weight of tetrafluoropropene;
6% by weight of difluoromethane, 3% by weight of pentafluoroethane and 91% by weight of tetrafluoropropene; and
6% by weight of difluoromethane, 2.5% by weight of pentafluoroethane and 91.5% by weight of tetrafluoropropene.
7. The process as claimed in claim 1 , in which the refrigerant has a GWP of less than 1500.
8. The process as claimed in claim 1 , in which the refrigerant has a lower flammability limit of greater than 285 g/m 3 .
9. The process as claimed in claim 1 , in which the refrigerant has a flame propagation rate of less than 2 cm/s.
10. The process as claimed in claim 1 , wherein the first and second exchangers are of the air/refrigerant type.
11. The process as claimed in claim 1 , wherein the refrigerating loop is thermally coupled with a cooling circuit of an engine and/or of an electronic circuit.
12. The process as claimed in claim 1 , wherein the first heat exchanger is traversed both by the refrigerant and by exhaust gases resulting from a heat engine of the motor vehicle or by heat resulting from a battery or from an electronic circuit of the motor vehicle.
13. The process as claimed in claim 1 , wherein the loop can comprise, as a bypass, at least one heat exchanger in thermal communication with a stream of air, intended to be admitted inside a heat engine of the motor vehicle, or with exhaust gases resulting from the motor vehicle heat engine, and/or with heat resulting from an electric motor and/or from an electronic circuit and from a battery of an electric motor vehicle.
14. The process as claimed in claim 1 , wherein the refrigerating loop is installed in the motor vehicle for the recovery of energy from a heat engine and/or from an electric battery.
15. A device comprising the reversible refrigerating loop as claimed in claim 1 .
16. The process as claimed in claim 1 , in which the tetrafluoropropene is 2,3,3,3-tetrafluoropropene.
17. The process as claimed in claim 1 , in which the refrigerant is chosen from the group consisting of:
5% by weight of difluoromethane, 3.3% by weight of pentafluoroethane and 91.7% by weight of 2,3,3,3-tetrafluoropropene;
5% by weight of difluoromethane, 3% by weight of pentafluoroethane and 92% by weight of 2,3,3,3-tetrafluoropropene;
5% by weight of difluoromethane, 3.1% by weight of pentafluoroethane and 91.9% by weight of 2,3,3,3-tetrafluoropropene;
5% by weight of difluoromethane, 3.2% by weight of pentafluoroethane and 91.8% by weight of 2,3,3,3-tetrafluoropropene;
6% by weight of difluoromethane, 3% by weight of pentafluoroethane and 91% by weight of 2,3,3,3-tetrafluoropropene; and
6% by weight of difluoromethane, 2.5% by weight of pentafluoroethane and 91.5% by weight of 2,3,3,3-tetrafluoropropene.
18. The process as claimed in claim 1 , wherein the process prevents air from entering the evaporator of the refrigerating loop on starting up the compressor when an external temperature is −12° C.
19. The process as claimed in claim 1 , wherein the process prevents air from entering the evaporator of the refrigerating loop on starting up the compressor when an external temperature is −29° C.
20. The process as claimed in claim 1 , wherein the process prevents air from entering the evaporator of the refrigerating loop on starting up the compressor when a temperature at the evaporator is −15° C.
21. The process as claimed in claim 1 , wherein the process prevents air from entering the evaporator of the refrigerating loop on starting up the compressor when a temperature at the evaporator is −32° C.