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Figure 3 – Heat Recovery Power Plant Using an Intermediate Heat Transfer Loop A. Thermodynamic Cycle For moderate enthalpy heat sources, ORC cycles offer many advantages over the conventional steam cycle, primarily due to the simplicity of the turbine, the control system, and the balance of plant. The distinguishing features of an ORC cycle have been treated in numerous papers (Ref. 1, 2, 3, 4). For an ORC plant the turbine and piping sizes are smaller and thus less costly due to the fluid density differences. The condensing pressure in an organic cycle is generally above atmospheric thus eliminating the need for complex vacuum and gas purging equipment that is utilized in a steam condensing cycle. Also, note that when the organic vapor expands in the turbine it becomes superheated or dryer, unlike steam which becomes wetter during the expansion process. Therefore, superheating of the organic vapor prior to delivery to the turbine is not required. Since organic fluids have a low freezing temperature, there is no freezing in the condenser, even at extremely low ambient temperatures. B. Practical Characteristics of the ORMAT ORC The ORMAT ORC based systems on ORMAT Energy Converter (OEC) has been designed to operate in heat recovery systems converting the low-temperature heat sources available in the cement and other industries into electricity, with design criteria as follows: (a) matching of the OEC design to the specific characteristics of the heat source; (b) no interference with normal operating modes of the host cement plant, to avoid clinker production setbacks; (c) simplicity in operation and maintenance; (d) modular construction to ensure rapid implementation and low erection costs; (e) low maintenance costs and high system availability; (f) flexibility toPDF Image | ORGANIC RANKINE CYCLE POWER PLANT FOR WASTE HEAT RECOVERY
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