Power generation with a centrifugal compressor
View Patent ↗A machine designed as a centrifugal compressor is applied as an organic rankine cycle turbine by operating the machine in reverse. In order to accommodate the higher pressures when operating as a turbine, a suitable refrigerant is chosen such that the pressures and temperatures are maintained within established limits. Such an adaptation of existing, relatively inexpensive equipment to an application that may be otherwise uneconomical, allows for the convenient and economical use of energy that would be otherwise lost by waste heat to the atmosphere.
1. A method of using a centrifugal compressor of the type having an impeller, a diffuser and a collector in serial outboard radial flow relationship comprising the steps of:
introducing a high pressure, high temperature vapor in said collector such that it flows radially inwardly through the diffuser to said impeller, with said diffuser acting as a nozzle;
allowing said vapor to engage the impeller such that the impeller is caused to rotate; and drivingly connecting said impeller to a generator to cause the generation of electricity
wherein said vapor is introduced at pressures in the range of 130–330 psia.
2. A method of using a centrifugal compressor of the type having an impeller, a diffuser and a collector in serial outboard radial flow relationship comprising the steps of:
introducing a high pressure, high temperature vapor in said collector such that it flows radially inwardly through the diffuser to said impeller, with said diffuser acting as a nozzle;
allowing said vapor to engage the impeller such that the impeller is caused to rotate; and
drivingly connecting said impeller to a generator to cause the generation of electricity
wherein said vapor is introduced at saturation temperatures in the range of 210–270°F.
3. An organic rankine cycle system of the type having in serial flow relationship a pump, an evaporator, a turbine and a condenser, wherein said turbine comprises:
an arcuately disposed volute for receiving an organic refrigerant vapor medium from the evaporator and for conducting the flow of said vapor radially inwardly;
a plurality of nozzles circumferentially spaced and disposed around the inner periphery of said volute for receiving a flow of vapor therefrom and conducting it radially inwardly, each of said nozzles having their radially inner and outer boundaries defined by radii R 1 and R 2 , respectively, and wherein R 2 /R 1 >1.25; and
an impeller disposed radially within said nozzles such that the radial inflow of vapor from said nozzles impinges on the plurality of circumferentially spaced blades on said impeller to cause rotation of said impeller; and
discharge flow means for conducting the flow of vapor from said turbine to the condenser.
4. An organic rankine cycle system as set forth in claim 3 wherein said plurality of nozzles are of the vaned type.
5. An organic rankine cycle system as set forth in claim 4 wherein said nozzles are each comprised of a frustro-conical passageway.
6. An organic rankine cycle system as set forth in claim 3 wherein the pressure of a vapor entering said volute is in the range of 180–330 psia.
7. An organic rankine cycle system as set forth in claim 3 wherein the saturation temperature of the vapor entering the volute is in the range of 210–270°F.
8. An organic rankine cycle system as set forth in claim 3 wherein the evaporator receives heat from an internal combustion engine.
9. An organic rankine cycle system as set forth in claim 8 wherein the heat derived from said internal combustion engine is derived from the exhaust thereof.
10. An organic rankine cycle system as set forth in claim 8 wherein the heat derived from said internal combustion engine is derived from its liquid coolant being circulated within said internal combustion engine.
11. An organic rankine cycle system as set forth in claim 3 wherein said condenser is of the water cooled type.
12. An organic rankine cycle system as set forth in claim 3 wherein said organic refrigerant is R-245fa.