초록 ▼

A Cascading Closed Loop Cycle (CCLC) system is described for recovering power in the form of mechanical or electrical energy from any thermal energy source whose temperature is sufficiently high to vaporize a pressurized light hydrocarbon medium such as propane or propylene. A light hydrocarbon medi

A Cascading Closed Loop Cycle (CCLC) system is described for recovering power in the form of mechanical or electrical energy from any thermal energy source whose temperature is sufficiently high to vaporize a pressurized light hydrocarbon medium such as propane or propylene. A light hydrocarbon medium is vaporized in multiple indirect heat exchangers; expanded in multiple cascading expansion turbines to generate useful power; and condensed to a liquid using a cooling system. The light hydrocarbon liquid medium is then pressurized with a pump and returned to the indirect heat exchangers to repeat the vaporization, expansion, liquefaction and pressurization cycle in a closed, hermetic process.

대표청구항 ▼

1. A method for converting heat to useful energy based on a Cascading Closed Loop Cycle (CCLC), said method comprising the following steps:A) supplying a primary liquid stream of propane to a primary indirect heat exchanger to vaporize said propane by utilizing the thermal energy derived from a heat

1. A method for converting heat to useful energy based on a Cascading Closed Loop Cycle (CCLC), said method comprising the following steps:A) supplying a primary liquid stream of propane to a primary indirect heat exchanger to vaporize said propane by utilizing the thermal energy derived from a heat source; B) expanding the primary stream of vaporized propane in a primary expansion turbine to produce useful energy; C) leading the primary vaporized propane stream leaving the primary expansion turbine to a secondary indirect heat exchanger; D) superheating a secondary stream of vaporized propane in the secondary indirect heat exchanger; E) expanding the secondary stream of superheated propane in a secondary expansion turbine to produce useful energy; F) leading the primary stream of vaporized propane exiting the secondary indirect heat exchanger to a stream mixer; G) leading the secondary stream of vaporized propane exiting the secondary expansion turbine to the stream mixer; H) combining the primary and secondary streams of vaporized propane in the stream mixer; I) leading the combined stream of vaporized propane to a tertiary indirect heat exchanger for vaporizing the secondary stream of liquid propane; J) leading the combined stream of vaporized propane to a condenser for cooling the same to a liquid; K) leading the combined stream of liquid propane exiting the condenser to a pump; L) pressurizing the combined stream of liquid propane in the pump; M) separating the pressurized combined stream of liquid propane from the discharge of the pump into a primary and secondary propane stream in the stream separator; N) leading the primary stream of pressurized liquid propane to Step A for vaporizing same; and O) leading the secondary stream of pressurized liquid propane to Step I for vaporizing same. 2. A method according to claim 1, wherein an ORC medium is propylene.3. A method according to claim 1, wherein an ORC medium is light hydrocarbons.4. A method according to claim 1, wherein an ORC medium is a mixture of light hydrocarbons.5. A method according to claim 1, wherein the discharge pressure of the expansion turbines is controlled to maintain the discharge pressure of the tertiary indirect heat exchanger above the vapor pressure of the ORC medium.