| US 7,458,218 B2 | ||
| Cascade power system | ||
| Alexander I. Kalina, Hillsborough, Calif. (US) | ||
| Assigned to Kalex, LLC, Belmont, Calif. (US) | ||
| Filed on Sep. 22, 2005, as Appl. No. 11/235,654. | ||
| Application 11/235654 is a continuation in part of application No. 11/099211, filed on Apr. 05, 2005. | ||
| Application 11/099211 is a continuation in part of application No. 10/983970, filed on Nov. 08, 2004, granted, now 7,398,651. | ||
| Prior Publication US 2008/0000225 A1, Jan. 03, 2008 | ||
| This patent is subject to a terminal disclaimer. | ||
| Int. Cl. F01K 25/06 (2006.01) | ||
| U.S. Cl. 60—649 [60/651; 60/671] | 38 Claims |

| 1. A cascade power system comprising:
an energy extraction subsystem,
a separation subsystem,
a heat exchange subsystem,
a heat recovery vapor generator (HRVG) subsystem and
a condensation thermal compression (CTCSS) subsystem,
where the system is adapted to establish two interacting working fluid cycles, one cycle utilizes a rich multi-component working
fluid stream having a higher concentration of a lower boiling component and the other cycle utilizes a lean working multi-component
working fluid stream having a lower concentration of the lower boiling component,
where each stream is derived from a fully condensed incoming multi-component stream,
where the separation subsystem is adapted to produce the lean working fluid stream and a rich make-up working fluid streams,
which is combined with the fully condensed incoming multi-component stream to form the rich multi-component working fluid
stream,
where the heat exchange subsystem and the heat recovery vapor generator (HRVG) subsystem are adapted to heat and vaporize
the lean working fluid stream and the rich working fluid stream from heat derived directly and/or indirectly from an external
flue gas stream,
where the energy extraction subsystem is adapted to extract energy from the lean working fluid stream and the rich working
fluid stream in separate turbine or turbine stages,
where the CTCSS subsystem is adapted to condense a spent rich stream to form the fully condensed incoming multi-component
stream,
where a flue gas flow rate is the same throughout the entire HRVG subsystem or is different in different portions of the HRVG
subsystem and
where an initial hot flue gas stream is cooled by a re-circulated portion of a spent flue gas stream exiting the HRVG subsystem
prior to the flue gas stream entering the HRVG subsystem.
|