Method for power generation during the regasification of a fluid by supercritical expansion

1. A device for power generation during regasification, comprising:

a tank for a cryogenic fluid,

a first pump which is connected to the tank via a first line,

a first heat exchanger which is connected to the first pump via a second line and a second heat exchanger which is arranged downstream of the first heat exchanger, and

a first turbine which is arranged directly downstream of the second heat exchanger,

wherein a third line branches off from the first turbine and opens in the first heat exchanger and a fourth line branches off from this first heat exchanger and opens in the second line between the first pump and second heat exchanger upstream of the first heat exchanger,

wherein a second pump is connected in the fourth line,

wherein a third heat exchanger is connected in the second line and in the fourth line upstream of the second pump.

2. The device as claimed in claim 1 , wherein a fifth line branches off from the first turbine and opens in a pipeline.

3. The device as claimed in claim 2 , wherein a fourth heat exchanger is connected in the fifth line.

4. The device as claimed in claim 3 , wherein a second turbine is connected in the fifth line and the fourth heat exchanger is arranged downstream of the second turbine.

5. The device as claimed in claim 4 , wherein a fifth heat exchanger is arranged upstream of the second turbine in the fifth line.

6. The device as claimed in claim 1 , wherein the first heat exchanger, third heat exchanger and introduction location of the fourth line into the second line are arranged in an integrated heat exchanger.

7. The device as claimed in claim 1 , wherein the tank contains liquid natural gas.

8. A method for power generation, comprising:

bringing a fluid to a first pressure and consequently producing a high-pressure flow,

combining the high-pressure flow with a second fluid flow which is greater than the high-pressure flow, into a total fluid flow,

guiding the total fluid flow to a first heat exchanger, and heating the total fluid flow by the second fluid flow, resulting in a heated total fluid flow,

subsequently further heating the heated total fluid flow in a second heat exchanger by introducing ambient heat and/or waste heat from other processes, resulting in a further heated total fluid flow,

expanding the further heated total fluid flow in a first turbine to a lower but supercritical pressure, resulting in an expanded total fluid flow,

dividing the expanded total fluid flow, which is discharged from the first turbine, into the second fluid flow and into a smaller third fluid flow,

wherein the second fluid flow, after it has discharged heat to the total fluid flow, is brought to a pressure level of the high-pressure flow, and combined with the high-pressure flow upstream of the first heat exchanger,

wherein the second fluid flow, before it is brought to the pressure level of the high-pressure flow, is further cooled by a third heat exchanger, wherein the high-pressure flow is heated.

9. The method as claimed in claim 8 , wherein the fluid is removed from a tank.

10. The method as claimed in claim 9 , wherein by means of a first pump the fluid removed from the tank is brought to a pressure of over 150 bara.

11. The method as claimed in claim 8 , wherein the ambient heat is removed from air or seawater.

12. The method as claimed in claim 8 , wherein the further heating is carried out to at least 5° C. below ambient temperature.

13. The method as claimed in claim 8 , wherein the lower, but supercritical pressure is over 70 bara.

14. The method as claimed in claim 8 , wherein the third fluid flow is introduced into a pipeline.

15. The method as claimed in claim 8 , wherein multi-stage expansion and intermediate heating are carried out in the first turbine.

16. The method as claimed in claim 9 , wherein the fluid removed from the tank is liquid air, liquid natural gas, liquid nitrogen, liquid oxygen or liquid argon.