Optimization of a supercritical carbon dioxide solar thermal power system

dc.contributor.advisorGroenwold, A. A.en_ZA
dc.contributor.advisorVan der Spuy, A. A.en_ZA
dc.contributor.advisorDobson, R. T.en_ZA
dc.contributor.authorVan der Westhuizen, Ruanen_ZA
dc.contributor.otherStellenbosch University. Faculty of Engineering. Dept. of Mechanical and Mechatronic Engineering.en_ZA
dc.date.accessioned2020-11-26T15:21:41Z
dc.date.accessioned2021-01-31T19:46:53Z
dc.date.available2020-11-26T15:21:41Z
dc.date.available2021-01-31T19:46:53Z
dc.date.issued2020-12
dc.descriptionThesis (PhD)--Stellenbosch University, 2020.en_ZA
dc.description.abstractENGLISH ABSTRACT: A new procedure for the optimal design of a solar thermal power system that uses a supercritical carbon dioxide (sCO2) Brayton cycle is developed. The design procedure is compatible with different types of component models, solution methods and design constraints. The variables of the system, and the objectives and constraints of the system design, are managed through a comprehensive computational architecture. Multi-objective optimization of 23 thermodynamic-, geometric- and performance design variables of the system is achieved.The design procedure is based on a specific series of design decisions that continually reduce the design spaces of the turbo machinery and heat exchanger sub-systems, in such a way that Pareto-optimality ofthe final system design is ensured. For computational expediency, initial design decisions are made based on the analysis of a thermodynamic model. It is demonstrated that the optimal thermodynamic design of the system is influenced by the performance values of the turbo machinery and recuperator. Subsequent design decisions are made based on the independent analyses of detailed turbo machinery and heat exchanger models.The turbo machinery is modeled in Matlab® with a mean-line analytical approach that uses specified performance coefficients. Explicit constraints ensure that the turbo machinery designs are within established limits.The heat exchangers are modeled in Flownex® using a control-volume-based convection-diffusion approach that can accurately represent the internal pinch-point of the recuperator. All models make use of realistic thermodynamic properties for supercritical carbon dioxide and are extensively validated with published data.A formal derivation shows that there are two distinct operating regions for the heat exchangers of the system. A successful system design depends on the region in which the heat exchangers function. This region can be controlled by changing the value of the nominal flow area, which is considered the most important design variable of the system. Six designs of the same basic system, but with different objectives and constraints, are presented. These designs are evaluated and compared to each other through a detailed quantitative investigation that highlights which factors contribute most to the inefficiency of each design. The best design achieves a thermal-to-mechanical efficiency of 40% at a turbine inlet temperature of 550◦C. This efficiency is demonstrated to be near the practical maximum for an sCO2system that employs the recuperated cycle configuration with a linear solar receiver. Future developments of the design procedure could consider the addition of a financial model as well as constraints to account for the structural integrity of the system.en_ZA
dc.description.abstractAFRIKAANSE OPSOMMING: Raadpleeg teks vir opsommingaf_ZA
dc.description.versionDoctoralen_ZA
dc.format.extent211 pagesen_ZA
dc.identifier.urihttp://hdl.handle.net/10019.1/109366
dc.language.isoen_ZAen_ZA
dc.publisherStellenbosch : Stellenbosch Universityen_ZA
dc.rights.holderStellenbosch Universityen_ZA
dc.subjectBrayton Cycleen_ZA
dc.subjectSupercritical Carbon Dioxide (sCO2)en_ZA
dc.subjectMultidisciplinary Design Optimization (MDO)en_ZA
dc.subjectConcentrated Solar Power (CSP)en_ZA
dc.subjectUCTDen_ZA
dc.titleOptimization of a supercritical carbon dioxide solar thermal power systemen_ZA
dc.typeThesisen_ZA
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