Rankine cycle plant and process for the regasification of liquefied gas
A Rankine cycle plant for the regasification of liquefied gas, includes: a Rankine closed loop system; a source of liquefied gas at a cryogenic temperature operatively coupled to a condenser to receive heat from a working fluid from an expansion turbine to take the liquefied gas to the gaseous state; a source of a heating fluid at a temperature higher than the cryogenic temperature operatively coupled to an evaporator to transfer heat to the working fluid coming from the condenser. The expansion turbine is radial centrifugal with at least one auxiliary outlet interposed between successive stages. The condenser is multilevel and has at least two condensing chambers, wherein a lower chamber being connected to an outflow opening of the expansion turbine and an upper chamber connected to the auxiliary outlet of the expansion turbine.
1. A Rankine cycle plant for the regasification of liquefied gas, comprising:
a Rankine closed loop system comprising at least:
one evaporator;
an expansion turbine provided with an inflow opening, an outflow opening and at least one auxiliary outlet;
a generator operatively connected to the expansion turbine;
a condenser;
a pump;
conduits configured to connect the evaporator, the expansion turbine, the condenser and the pump according to a closed cycle in which a working fluid circulates;
a source of liquefied gas at a cryogenic temperature, wherein the source of liquefied gas is operatively coupled to the condenser to receive heat from the working fluid flowing out from the expansion turbine so as to take the liquefied gas to the gaseous state;
a source of a heating fluid at a higher temperature than the cryogenic temperature, wherein the source of heating fluid is operatively coupled to the evaporator to transfer heat to the working fluid coming from the condenser;
wherein the expansion turbine is a radial centrifugal turbine, wherein said at least one auxiliary outlet is interposed between successive stages of said expansion turbine, and
wherein the condenser is a multilevel condenser and comprises at least two condensing chambers, a lower chamber of said at least two condensing chambers is connected to the outflow opening and an upper chamber of said at least two condensing chambers is connected to said at least one auxiliary outlet, and
wherein the expansion turbine comprises a single rotor disc and a plurality of stages radially arranged one after the other at a front face of the rotor disc, and wherein the auxiliary outlet opens between two of said stages.
2. The plant according to claim 1 , wherein the expansion turbine comprises a plurality of auxiliary outlets each interposed between successive stages.
3. The plant according to claim 1 , wherein the multilevel condenser comprises a casing delimiting therein said at least two condensing chambers and an outflow duct connecting the upper chamber to the lower chamber.
4. The plant according to claim 3 , wherein the multilevel condenser comprises a plurality of condensing chambers arranged one over the other and a plurality of ducts connecting said condensing chambers to each other in a cascade fashion.
5. The plant according to claim 1 , wherein the condenser has a series of inner septa that partition it internally in said condensing chambers.
6. The plant according to claim 3 , wherein the casing of the condenser has an elongated shape and mainly a vertical extension.
7. The plant according to claim 4 , wherein rising upwards with respect to the condenser, successive chambers are connected to auxiliary outlets of the expansion turbine at increasing pressure.
8. The plant according to claim 1 , wherein the condenser comprises at least one tube or tube bundle connected to the source of liquefied gas; wherein said at least one tube or tube bundle passes through said at least two condensing chambers; wherein the liquefied gas flows from the bottom upwards through said at least one tube or tube bundle.
9. The plant according to claim 1 , wherein the pump is only one and it is operatively arranged between the lower chamber of the condenser and the evaporator for pumping the condensed working fluid up to said evaporator.
10. The plant according to claim 1 , wherein the conduits comprise a conduit connecting the lower chamber of the condenser and the evaporator, wherein a section of said conduit passes through at least one chamber of the condenser.
11. The plant according to claim 1 , comprising a first and a second expansion turbine, wherein an outflow opening of the first expansion turbine is connected to an inflow opening of the second expansion turbine, wherein the first and/or the second expansion turbine has at least one auxiliary outlet.
12. The plant according to claim 11 , comprising a heat exchanger located between the outflow opening of the first expansion turbine and the inflow opening of the second expansion turbine and operatively coupled to the source of heating fluid.
13. The plant according to claim 1 , wherein the working fluid is selected from the group comprising: organic fluids, hydrocarbons, CO 2 , N 2 O.
14. The plant according to claim 1 , wherein the heating fluid entering into the evaporator has a temperature (T hf ) comprised between 5° C. and 70° C.
15. The plant according to claim 1 , wherein the heating fluid is seawater.
16. The plant according to claim 1 , wherein the liquefied gas flowing into the condenser has a temperature (T lg ) comprised between −155° C. and −173° C.
17. A Rankine cycle plant for the regasification of liquefied gas, comprising:
a Rankine closed loop system comprising at least:
one evaporator;
a single expansion turbine provided with an inflow opening, an outflow opening and at least one auxiliary outlet;
a generator operatively connected to the expansion turbine;
a condenser;
a pump;
conduits configured to connect the evaporator, the expansion turbine, the condenser and the pump according to a closed cycle in which a working fluid circulates;
a source of liquefied gas at a cryogenic temperature, wherein the source of liquefied gas is operatively coupled to the condenser to receive heat from the working fluid flowing out from the expansion turbine so as to take the liquefied gas to the gaseous state;
a source of a heating fluid at a higher temperature than the cryogenic temperature, wherein the source of heating fluid is operatively coupled to the evaporator to transfer heat to the working fluid coming from the condenser;
wherein the expansion turbine is a radial centrifugal turbine, wherein said at least one auxiliary outlet is interposed between successive stages of said expansion turbine, and
wherein the condenser is a multilevel condenser and comprises at least two condensing chambers, wherein a lower chamber of said at least two condensing chambers is connected to the outflow opening and an upper chamber of said at least two condensing chambers is connected to said at least one auxiliary outlet.
18. The plant according to claim 17 , wherein the expansion turbine comprises a single rotor disc and a plurality of stages radially arranged one after the other at a front face of the rotor disc, and wherein the auxiliary outlet opens between two of said stages.
19. The plant according to claim 18 , wherein the two stages between which the auxiliary outlet opens, are radially spaced to define a chamber for extracting the working fluid.
20. The plant according to claim 18 , wherein the expansion turbine comprises a fixed housing, wherein the rotor disc is rotatably inserted into the fixed housing, wherein the auxiliary outlet is obtained in a front wall of the fixed housing.