Optimum operating conditions of the small-scale open and direct solar thermal Brayton cycle at various steady-state conditions

dc.contributor.upauthorBello-Ochende, Tunde
dc.contributor.upauthorLe Roux, Willem Gabriel
dc.contributor.upauthorMeyer, Josua P.
dc.date.accessioned2014-06-27T07:37:18Z
dc.date.available2014-06-27T07:37:18Z
dc.date.issued2011
dc.description.abstractPaper presented at the 8th International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics, Mauritius, 11-13 July, 2011.en_US
dc.description.abstractA heat source can be considered as the Brayton cycle’s life support. This heat source can be extracted from solar energy. The small-scale open and direct solar thermal Brayton cycle with recuperator has several advantages, including lower cost, low operation and maintenance costs and it is highly recommended. The main disadvantages of this cycle are the pressure losses in the recuperator and receiver, turbo-machine efficiencies and recuperator effectiveness, which limit the net power output of such a system. The irreversibilities of the solar thermal Brayton cycle are mainly due to heat transfer across a finite temperature difference and fluid friction. Thermodynamic optimization can be applied to address these disadvantages to optimize the receiver and recuperator and to maximize the net power output of the system at any steady-state condition. The dynamic trajectory optimization method is applied to maximize the net power output of the system by optimizing the geometries of the receiver and recuperator limited to various constraints. Standard micro-turbines and parabolic dish concentrator diameters of 6 to 18 meters are considered. An optimum system geometry and maximum net power output is generated for each operating condition of each micro-turbine and concentrator combination. Results show the optimum operating conditions as a function of system mass flow rate. The optimum operating point of a specific micro-turbine is at a point where the internal irreversibilities are approximately three times the external irreversibilities. For a specific environment and parameters there exists an optimum receiver and recuperator geometry so that the system produces maximum net power output.en_US
dc.description.librarianmp2014en_US
dc.format.extent10 pagesen_US
dc.format.mediumPDFen_US
dc.identifier.citationLe Roux, WG, Bello-Ochende, T, & Meyer JP 2011, 'Optimum operating conditions of the small-scale open and direct solar thermal Brayton cycle at various steady-state conditions', Paper presented to the 8th International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics, Mauritius, 11-13 July, 2011.en_US
dc.identifier.urihttp://hdl.handle.net/2263/40433
dc.language.isoenen_US
dc.publisherInternational Conference on Heat Transfer, Fluid Mechanics and Thermodynamicsen_US
dc.relation.ispartofHEFAT 2011en_US
dc.rightsUniversity of Pretoriaen_US
dc.subjectHeat transferen_US
dc.subjectFluid mechanicsen_US
dc.subjectThermodynamicsen_US
dc.subjectOptimum operating conditionsen_US
dc.subjectSolar thermal Brayton cycleen_US
dc.subjectSteady-state conditionsen_US
dc.subjectSmall-scale open and directen_US
dc.subjectRecuperatoren_US
dc.subjectDynamic trajectory optimizationen_US
dc.subjectMicro-turbinesen_US
dc.subjectParabolic dish concentratoren_US
dc.subjectOptimum operating conditionsen_US
dc.subjectExternal irreversibilitiesen_US
dc.subjectInternal irreversibilitiesen_US
dc.subjectMaximum net power outputen_US
dc.titleOptimum operating conditions of the small-scale open and direct solar thermal Brayton cycle at various steady-state conditionsen_US
dc.typePresentationen_US

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