Single flow cascade power system
A cascade power system is disclosed where a single basic working composition (BWC) of a multi-component working fluid stream is fully vaporized in a vaporization subsystem utilizing heat derived from a heat source stream such as a combustion gas stream and energy is extracted from the stream in a multi-stage energy extraction system. The energy extraction subsystem is designed to produce a fully spent BWC stream and a partially spent BWC stream. The fully spend BWC stream is then divided into a fully condensed lean stream and a fully condensed rich stream in a Condensation-Thermal Compression Subsystem. The partially spent stream and stream derived therefrom are used to form a second lean stream and a second rich stream and to heat the fully condensed lean stream and a combined rich stream prior to vaporization.
1. A power system comprising:
a vaporization subsystem,
an energy extraction subsystem, and
a Condensation-Thermal Compression Subsystem (CTCSS),
a two cycle heating and separating subsystem,
where:
the vaporization subsystem is designed to fully heat a combined lean stream, which is then combined with a combined rich stream to form the single composition of a multi-component working fluid BWC stream which is then fully vaporized,
the energy extraction subsystem is designed to convert a portion of thermal energy in the fully vaporized stream of a single composition of a multi-component working fluid BWC stream to useable energy in two stages with a portion of an intermediate spent stream being diverted to heat a lean and rich stream formed in the CTCSS in the heating and separating subsystem and to form second rich and lean stream,
the CTCSS is designed to convert the spent BWC stream into a fully condensed lean stream and fully condensed rich stream using one or more external coolant streams, and
the two cycle heating and separating subsystem is designed to support two interacting thermodynamically different working fluid cycles, a lean stream cycle and a rich stream cycle.
2. A method comprising the steps of:
forwarding a fully vaporized basic working composition stream to an energy extraction subsystem, where a portion of its thermal energy is converted into a usable form of energy in a two stage process to produce a spent basic working composition stream and a diverted partially spent basic working composition stream,
forwarding the spent stream to a Condensation-Thermal Compression Subsystem (CTCSS), where the spent stream is divided and cooled in a series of heat exchange, separation, throttling and pressurizing steps to form a fully condensed first lean stream and a fully condensed first rich stream using one or more external coolant stream,
using the diverted partially spent basic working composition stream to form a second rich stream and a second lean stream,
combining the second rich stream with the first rich stream to form a combined rich stream,
heating the combined rich stream with heat derived from the diverted partially spent basic working composition stream and streams derived therefrom,
heating the first lean stream with heated derived from the diverted partially spent basic working composition stream and streams derived therefrom,
combining the heated first lean stream with the second lean stream to form a combined lean stream,
heating the combined lean stream in a lower portion of the vaporization subsystem,
combining the heated combined lean stream with the combined rich stream at a mid-location of the vaporization subsystem to form a basic working composition stream composition stream, and
fully vaporizing the basic working composition stream in top portion of the vaporization subsystem using an external heat source stream.
3. The method of claim 2 , wherein in the vaporization subsystem, an initial combustion gas stream is mixed with a portion of the spent combustion gas stream to form a combustion gas stream having a temperature below a temperature that cause undue stress on the heat exchange elements of the vaporization subsystem.
4. The method of claim 2 , wherein the external heat source stream is a combustion gas stream.
5. The method of claim 4 , wherein the combustion gas stream is derived from the combustion of a low value fuel.