Use of biodegradable hydrocarbon fluids as heat-transfer media
The invention relates to the use, as a liquid phase heat-transfer medium, of a fluid having a boiling point in the range of from 200° C. to 400° C. and a boiling range below 80° C., said fluid comprising more than 95% by weight isoparaffins and less than 3% by weight of naphthens, a biocarbon content of at least 95% by weight, containing less than 100 ppm by weight aromatics.
1. Method for transferring heat, said method comprising:
introducing a liquid fluid into a closed loop system, the fluid having an initial boiling point and a final boiling point in the range of from 200° C. to 400° C. and a boiling range below 80° C., said fluid comprising more than 95% by weight of isoparaffins, less than 3% by weight of naphthenes, a biocarbon content of at least 95% by weight, and less than 100 ppm by weight aromatics; and
transferring heat by the fluid in a car engine,
wherein the step of transferring heat comprises a step of cooling the car engine,
wherein the boiling range of the fluid is 240° C.-275° C. or 250° C.-295° C. or 285° C.-335° C. wherein the fluid has a flash point higher than 115° C.
2. Method of claim 1 , wherein the step of transferring heat is performed at a temperature ranging from −50° C. to 260° C.
3. Method of claim 2 , wherein the fluid in the step of transferring heat has a boiling range of 240° C.-275° C. or a boiling range of 250° C.-295° C.
4. Method of claim 1 , wherein the step of transferring heat is performed at a temperature ranging from −30° C. to 315° C.
5. Method of claim 4 , wherein the fluid in the step of transferring heat has a boiling range of 285° C.-335° C.
6. Method of claim 1 , wherein the fluid contains less than 50 ppm aromatics.
7. Method of claim 1 , wherein the fluid contains less than 1% by weight of naphthenes.
8. Method of claim 1 , wherein the fluid further contains less than 5 ppm sulphur.
9. Method of claim 1 , wherein the fluid has a biodegradability at 28 days of at least 60%, as measured according to the OECD 306 standard.
10. Method of claim 1 , wherein the fluid contains less than 20 ppm by weight of aromatics and less than 500 ppm by weight of naphthenes and wherein the fluid has an initial boiling point and a final boiling point in the range of from 240° C. to 340° C.
11. Method of claim 1 , wherein the closed-loop system is a non-pressurized closed-loop system.
12. The method of claim 1 , wherein the fluid further comprises less than 4% by weight of n-paraffins.
13. Method for transferring heat, said method comprising:
introducing a liquid fluid into a dosed-loop system, the fluid having an initial boiling point and a final boiling point in the range of from 200° C. to 400° C. and a boiling range below 80° C., said fluid comprising at least 95.1% by weight of isoparaffins, less than 3% by weight of naphthenes, a biocarbon content of at least 95% by weight, and less than 50 ppm by weight aromatics,
transferring heat by the fluid in a car engine,
wherein the step of transferring heat comprises a step of cooling the car engine,
wherein the step of transferring heat is operated at a temperature ranging from −50° C. to 260° C. and wherein the fluid has a boiling range of 240° C.-275° C. or a boiling range of 250° C.-295° C. wherein the fluid has a flash point higher than 115° C.
14. The method of claim 13 , wherein the fluid further comprises less than 4% by weight of n-paraffins.
15. Method for transferring heat, said method comprising:
introducing a liquid fluid into a closed-loop system, the fluid haying an initial boiling point and a final boiling point in the range of from 200° C. to 400° C. and a boiling range below 80° C. said fluid comprising at least 95.1% by weight of isoparaffins, less than 1% by weight of naphthenes, a biocarbon content of at least 95% by weight, and less than 50 ppm by weight aromatics,
transferring heat by the fluid in a car engine,
wherein the step of transferring heat comprises a step of cooling the car engine,
wherein the step of transferring heat is operated at a temperature ranging from −30° C. to 315° C. and wherein the fluid has a boiling range of 285° C.-335° C. wherein the fluid has a flash point higher than 115° C.
16. The method of claim 15 , wherein the fluid further comprises less than 4% by weight of n-paraffins.