System and method of waste heat recovery
A Rankine cycle system useful for the conversion of waste heat into mechanical and/or electrical energy is provided. The system features a novel configuration in which a first closed loop thermal energy recovery cycle comprising a first working fluid stream and a second closed loop thermal energy recovery cycle comprising a second working fluid stream interact but do not mix. The two thermal energy recovery cycles interact thermally via heat exchangers, a first heat exchanger configured to transfer heat from the first working fluid stream to the second working fluid stream, and a second heat exchanger configured to transfer heat from the second working fluid stream to the first working fluid stream. In one or more embodiments, the Rankine cycle system is adapted for the use of supercritical carbon dioxide as the working fluid.
1. A Rankine cycle system comprising:
(a) a first closed loop thermal energy recovery cycle comprising a first working fluid stream;
(b) a second closed loop thermal energy recovery cycle comprising a second working fluid stream;
(c) a first heat exchanger configured to transfer heat from the first working fluid stream to the second working fluid stream;
(d) a second heat exchanger configured to transfer heat from the second working fluid stream to the first working fluid stream;
wherein the first closed loop thermal energy recovery cycle further comprises:
(i) a heater configured to transfer heat from a first waste heat-containing stream to the first working fluid stream to produce a vaporized first working fluid stream and a second waste heat-containing stream;
(ii) a first expander configured to receive the vaporized first working fluid stream and to produce therefrom mechanical energy and an expanded first working fluid stream;
(iii) a first condenser configured to cool a heat depleted first working fluid stream and produce therefrom a chilled first working fluid stream; and
(iv) a pump configured to pressurize the chilled first working fluid stream;
wherein the second closed loop thermal energy recovery cycle further comprises:
(v) a second expander configured to expand a vaporized second working fluid stream and to produce therefrom mechanical energy and an expanded second working fluid stream;
(vi) a second condenser configured to cool a heat depleted second working fluid stream and to produce therefrom a chilled second working fluid stream;
(vii) a pump configured to pressurize the chilled second working fluid stream;
(viii) a second-working-fluid-stream splitter configured to divide the expanded second working fluid stream into a first portion of the expanded second working fluid stream and a second portion of the expanded second working fluid stream; and
(ix) a second-working-fluid-stream combiner configured to combine a heat depleted first portion of the second working fluid stream with a heat depleted second portion of the second working fluid stream;
wherein the first heat exchanger is configured to produce the vaporized second working fluid stream, the heat depleted first working fluid stream and the heat depleted first portion of the second working fluid stream; and
wherein the second heat exchanger is configured to produce a thermally enhanced first working fluid stream and the heat depleted second portion of the second working fluid stream.
2. The Rankine cycle system according to claim 1 , further comprising a generator.
3. The Rankine cycle system according to claim 1 , further comprising a generator mechanically coupled to the first expander and the second expander.
4. The Rankine cycle system according to claim 1 , wherein the first working fluid and the second working fluid are essentially identical.
5. The Rankine cycle system according to claim 1 , wherein the system is configured to accommodate supercritical carbon dioxide.
6. The Rankine cycle system according to claim 1 , wherein both the first working fluid and the second working fluid are carbon dioxide.
7. The Rankine cycle system according to claim 1 , wherein the first condenser and the second condenser are incorporated into a single condenser unit.
8. The Rankine cycle system according to claim 1 , wherein the first pump and the second pump are incorporated into a single pump unit.
9. The Rankine cycle system according to claim 1 , wherein the first closed loop thermal energy recovery cycle further comprises a working fluid stream splitter.
10. The Rankine cycle system according to claim 1 , wherein the first closed loop thermal energy recovery cycle further comprises a working fluid stream splitter and a second heater.
11. The Rankine cycle system according to claim 1 , further comprising a second heater.
12. The Rankine cycle system according to claim 1 , comprising at least one plate-fin condenser.
13. The Rankine cycle system according to claim 1 , comprising at least one printed circuit condenser.
14. The Rankine cycle system according to claim 1 , wherein at least one of the first expander and the second expander is configured to drive at least one of, the first pump and the second pump.
15. The Rankine cycle system according to claim 1 , further comprising a generator configured to be driven by the first expander and at least one of, the first pump and the second pump configured to be driven by the second expander.
16. The Rankine cycle system according to claim 2 , wherein the generator is mechanically coupled to the first expander.
17. The Rankine cycle system according to claim 2 , wherein the generator is mechanically coupled to the second expander.
18. The Rankine cycle system according to claim 3 , wherein the first expander and the second expander, share a common drive shaft.