Steam Rankine plant

1. A steam Rankine cycle plant, comprising:

a higher-pressure steam turbine with an outlet for exhausting exhaust steam;

a reheater fluidly connected to the higher-pressure steam turbine;

a lower-pressure steam turbine, with an inlet fluidly connected to the reheater; and

a bypass fluidly connecting the outlet of the higher-pressure steam turbine and the inlet of the lower-pressure steam turbine so as to bypass the reheater,

wherein the higher-pressure steam turbine includes an intermediate stage and the reheater is fluidly connected to the intermediate stage so as to enable an extraction of extraction steam from the intermediate stage and direct it to the reheater, and

wherein the extraction steam is extracted from the higher-pressure steam turbine, before the extraction steam leaves a last stage of the higher-pressure steam turbine as the exhaust steam via the outlet of the higher-pressure steam turbine.

2. The plant according to claim 1 , wherein the outlet of the higher-pressure steam turbine is fluidly connected to the reheater so as to enable the exhaust steam from the higher-pressure steam turbine to be fed to the reheater.

3. The plant according to claim 2 , further comprising:

a controller configured and arranged to vary a flow ratio defined as a ratio of steam passing through the reheater to steam passing through the bypass.

4. The plant according to claim 2 , further comprising:

a measurement device, located in a line downstream of the bypass, configured and arranged to measure the superheat of steam fed to the lower-pressure steam turbine.

5. The plant according to claim 2 , further comprising:

a water extraction unit fluidly located between the higher-pressure steam turbine and the reheater.

6. The plant according to claim 1 , further comprising a controller that is configured and arranged to vary a flow ratio defined as a ratio of steam passing through the reheater to steam passing through the bypass.

7. The plant according to claim 6 , wherein the controller is configured to adjust the flow ratio based on measurements taken by a measurement device.

8. The plant according to claim 6 , further comprising:

a measurement device, located in a downstream of the bypass, configured and arranged to measure the superheat of steam fed to the lower-pressure steam turbine.

9. The plant according to claim 6 , further comprising:

a water extraction unit fluidly located between the higher-pressure steam turbine and the reheater.

10. The plant according to claim 1 , further comprising a measurement device, located in a line downstream of the bypass, configured and arranged to measure an amount of superheat in the steam fed to the lower-pressure steam turbine.

11. The plant according to claim 10 , further comprising a controller is configured to adjust a flow ratio defined as a ratio of steam passing through the reheater to steam passing through the bypass based on measurements taken by the measurement device.

12. The plant according to claim 1 , further comprising a water extraction unit that is fluidly located between the higher-pressure steam turbine and the reheater.

13. The plant according to claim 1 , wherein the bypass includes a water extraction unit for removing water from steam in the bypass.

14. An operating method for a steam Rankine cycle plant, comprising the steps of:

feeding, by a bypass, steam from a higher-pressure steam turbine to an inlet of a lower-pressure steam turbine; and

superheating, by a reheater, a portion of the steam before it is fed to the lower-pressure steam turbine, wherein the portion of the steam that is superheated is extracted from an intermediate stage of the higher-pressure steam turbine and directed to the reheater,

wherein the portion of the steam is extracted from the higher-pressure steam turbine, before the extracted portion of the steam leaves a last stage of the higher-pressure steam turbine as an exhaust steam via an outlet of the higher-pressure steam turbine.

15. The method according to claim 14 , further comprising:

measuring a degree of superheat in the steam as it is fed to the lower-pressure steam turbine; and

varying a flow ratio defined as a ratio of steam passing through the reheater to steam passing through the bypass.

16. The method according to claim 15 , further comprising:

extracting, by a water extraction unit, water from the bypass so that the steam fed to the lower-pressure steam turbine, independent of the flow ratio, is moisture free.

17. The method according to claim 15 , further comprising:

extracting, by a water extraction unit, water from the steam before it passes through the reheater.

18. The method according to claim 15 , further comprising:

varying the flow ratio so that the steam fed to the lower-pressure steam turbine is dry steam.

19. The method according to claim 15 , further comprising:

varying the flow ratio so that the steam fed to the lower-pressure steam turbine is superheated steam.

20. An operating method for a steam Rankine cycle plant comprising:

extracting a portion of steam, before the steam leaves a last stage of a higher-pressure steam turbine via an outlet of the higher-pressure steam turbine;

superheating the extracted portion of the steam; and

feeding to a lower-pressure steam turbine, the superheated portion of the steam along with a remaining portion of the steam that leaves via the outlet of the higher-pressure steam turbine.