Gas turbines are the primary technology used for the purpose of power generation nearly everywhere. In this thesis, the Makkah Power Plant, running on a Brayton cycle, is considered for analysis. The peak demand for electric power in the City of Makkah occurs in the middle of the day during the summer and is almost double the off-peak demand. The plant employs turbines of two world renowned manufacturers. However, there are many mechanical and electrical issues related to the overall insufficient operation of the plant. From the balancing of mass, entropy, energy, exergy and cost equations, a greater understanding of the systems as well as their efficiencies is achieved. The parametric study and plant optimization are performed to investigate the effects of the variation of specific input parameters such as fuel mass flow rate, air volume flow rate and compressor inlet air temperature, on the overall operating efficiency of the system. Through this study, the overall plant energetic and exergetic efficiencies are increased by 20% and 12% respectively with cooling down the compressor inlet temperature to 10oC. Furthermore, exergy and exergoeconomic analyses are conducted to obtain that the largest exergy destruction occurs in the combustion chamber, followed by the turbine. The optimization results demonstrate that CO2 emissions can be reduced by increasing the exergetic efficiency and using a low fuel injection rate into the combustion chamber. Finally, this study will assist efforts to understand the thermodynamic losses in the cycle, and to improve efficiency as well as provide future recommendations for better performance, sustainability and lessen environmental impact. / UOIT

The shift towards renewable energy has steered the focus of power plant operation towards flexibility and fast response which are more attainable through the use of combined-cycle power plants. These aspects are required to account for the fluctuation of the supply as well as the demand of power that is associated with renewable energy. Combined-cycle power plants consist of a gas turbine as the topping cycle, forming the core of the plant, and a Rankine cycle with a steam turbine as the bottoming cycle. A component called the Heat Recovery Steam Generator (HRSG) forms a connection point between the two cycles. It uses the heat released from the gas turbine to produce high pressure and temperature steam to be sent to the steam turbine. The objective of this project is to develop a model of a combined-cycle power plant in Flownex which can be solved in off-design conditions in order to compare it to plant data. The verification of this model will show that Flownex can be used to effectively and efficiently model a combined-cycle power plant. The process of development of the final Flownex model was achieved using various additional software. Initially, an analytical model was developed in Mathcad (software used for engineering calculations). This software provides a tool for understanding knowns, unknowns and what is being calculated in the system. Manual calculations of the Heat Recovery Steam Generator (HRSG) were done using heat balance equations. A temperature profile of the gas and water/steam in the HRSG was developed so that the duties of each component (economiser, evaporator, superheater) could be calculated. The overall conductance (UA) of each component was calculated in the design mode for the system to be evaluated in off-design mode. The development of an analytical model provided detailed understanding of the process of mathematical modelling used in commercial tools. Thereafter, a model was built in Virtual Plant, a thermodynamic modelling software for assessing plant performance. Virtual Plant uses plant design information and first engineering principles to predict plant performance. Finally, the Flownex model was designed. Flownex uses endpoint values (initial pressure and temperature and outgoing mass flow) and the UA of each component to calculate the characteristics of the flow at each intermediate point. For the single-, double-, and triple-pressure combined-cycle power plant systems, the analytical, Virtual Plant and Flownex models were compared. The results of all the models agreed closely with one another. The triple-pressure design and off-design Virtual Plant and Flownex models were also compared to plant data and it was concluded that Flownex was successful in modelling the design and off-design conditions of a combined-cycle power plant.

No description available.

Recently, attention has been drawn to the viability of using S-CO(2) as a working fluid in modern reactor designs. Near the critical point, CO2 has a rapid rise in density allowing a significant reduction in the compressor work of a closed Brayton Cycle. Therefore, 45% efficiency can be achieved at much more moderate temperatures than is optimal for the helium Brayton cycles. An additional benefit of the S-CO2 system is its universal applicability as an indirect secondary Power Conversion System (PCS) coupled to most GEN-IV concept reactors, as well as fusion reactors. The United States DOE's GNEP is now focusing on the liquid Na cooled primary as an alternative to conventional Rankine steam cycles. This primary would also benefit from being coupled to an S-CO2 PCS. Despite current progress on designing the S-CO2 PCS, little work has focused on the principal supporting systems required. Many of the required auxiliary systems are similar to those used in other nuclear or fossil-fired units; others have specialized requirements when CO2 is used as the working fluid, and are therefore given attention in this thesis. Auxiliary systems analyzed within this thesis are restricted to those specific to using CO2 as the working fluid. Particular systems discussed include Coolant Make-up and Storage, Coolant Purification, and Coolant Leak Detection. / Contract number: N62271-97-G-0026. / US Navy (USN) author

Thesis (M. App. Sc.)--Carleton University, 2005. / Includes bibliographical references. Also available in electronic format on the Internet.

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[pt] O presente trabalho trata da determinação experimental dos parâmetros de desempenho de um compressor rotativo de deslocamento positivo,que faz parte de um motor de refrigeração em desenvolvimento. Este opera segundo o ciclo de Brayton invertido utilizando o ar como fluido de trabalho. A vazão mássica real de ar em escoamento pelo compressor, eventuais vazamentos, potência de eixo entregue ao compressor e a potência desenvolvida pelo mesmo são obtidas com base em procedimentos experimentais. A vazão e a potência teóricas foram determinadas com base em uma simulação do funcionamento do compressor. A partir destes resultados, determinaram-se as eficiências isentrópica,mecânica e volumétrica, permitindo uma análise das condições de operação do compressor. Usando resultados experimentais, realizou-se uma análise termodinâmica convencional de disponibilidade associada ao processo real ocorrido no compressor para explicar a natureza das irreversibilidades envolvidas e indicar as condições ótimas de funcionamento. Com base na filosofia de análise utilizada, este novo tipo de máquina de refrigeração foi criteriosamente analisada. Sugestões de melhoria são apresentadas no sentido de melhor qualificar este novo tipo de compressor para trabalhar com sistemas que operem segundo o ciclo de Brayton invertido. Neste trabalho é apresentado uma proposta otimizada de um novo projeto de expansor. / [en] The present work describe tests of performance of a positive displacement rotary compressor which is part of a new type of refrigerating machine under development. The working fluid is air and the machine operates at the Brayton Cycle. The mass flow rate, eventual mass leakages, the power delivered to the compressor shaft and the actual power developed are obtained based upon experimental procedures. The theorectical mass flow rate and the isentropic power was calculed through a theorectical simulation, and, from these results, the isentropic mechanical and volumetric efficiencies have been evaluated allowing the determination of the favorable and critical conditions of operation. An uncertainty analysis is developed in order to control the experimental procedures and acuracy of the experiments conducted. Using experimental results as an input, a classical avaiability thermodynamics analysis of the process was developed in order to explain the nature of the associated irreversibilities and to indicate the optimum conditions of operation of the compressor. Based upon the described approach, this new type of refrigerating machine has been carefully analysed. Aiming better performance, design modifications are suggested as an attempt to better qualify this type of compressor for operation in systems which operate in the Brayton Cycle. Finalle, an improved design of an expander is discussed.

Master thesis is concerned with gas turbines from Siemens company. The thesis consists of two main parts. In the first part describes the different types of turbines, their characteristics and use in practice. The following is a detailed description of components and systems the biggest industrial gas turbine SGT-800. The second part discusses about the necessary steps for commissioning turbine. These particulars are managing software, testing, commissioning and phasing of the turbine generator to the distribution network. The conclusion is devoted to the example of calculating return investment on the overall gas turbine project.