A case of study of a concentrating solar power plant with unfired Joule-Brayton cycle
Table Of Contents
Chapter ONE
INTRODUCTION
- 1.1Introduction
- 1.2Background of the Study
- 1.3Problem Statement
- 1.4Objective of the Study
- 1.5Limitation of Study
- 1.6Scope of Study
- 1.7Significance of Study
- 1.8Structure of the Research
- 1.9Definition of Terms
Chapter TWO
LITERATURE REVIEW
- 2.1Overview of Concentrating Solar Power Plants
- 2.2History of Solar Power Technologies
- 2.3Joule-Brayton Cycle in Power Generation
- 2.4Advantages of Concentrating Solar Power Plants
- 2.5Challenges in Implementing CSP with Unfired Joule-Brayton Cycle
- 2.6Economic Viability of CSP Projects
- 2.7Environmental Impact of CSP Plants
- 2.8Technological Innovations in CSP
- 2.9Global Trends in CSP Development
- 2.10Future Prospects of CSP Technology
Chapter THREE
RESEARCH METHODOLOGY
- 3.1Research Design and Approach
- 3.2Data Collection Methods
- 3.3Sampling Techniques
- 3.4Research Instrumentation
- 3.5Data Analysis Procedures
- 3.6Ethical Considerations
- 3.7Validity and Reliability
- 3.8Limitations of the Methodology
Chapter FOUR
DATA PRESENTATION AND ANALYSIS
- 4.1Overview of Research Findings
- 4.2Analysis of Data Collected
- 4.3Comparison of Results with Literature Review
- 4.4Interpretation of Findings
- 4.5Implications of the Results
- 4.6Recommendations for Future Research
- 4.7Practical Applications of the Findings
- 4.8Areas for Further Investigation
Chapter FIVE
SUMMARY, CONCLUSION AND RECOMMENDATIONS
- 5.1Summary of Research
- 5.2Conclusions Drawn
- 5.3Contributions to Knowledge
- 5.4Practical Implications
- 5.5Recommendations for Industry
- 5.6Suggestions for Policy Makers
- 5.7Reflections on the Research Process
- 5.8Future Research Directions
Project Abstract
<p> <b>ABSTRACT</b></p><p>A solar closed air Brayton cycle, with rated power of 50 MW, was considered. The system is composed of a concentrating solar tower with volumetric receiver, an intercooling and regenerating gas turbine and an evaporative tower cooling system. The characteristic feature of the system is a control strategy able to adjust the plant in a large range of load, maintaining net electric conversion efficiency almost constant. The concentrating solar power (CSP) plant operates without adding fuel and can heat air up to a maximum temperature of 850 °C, at the solar tower outlet. The numerical analysis was performed by SAM for the solar tower and by Thermoflex © for the assessment of the performance of the whole system. The thermal energy input was calculated on the basis of the DNI of the TMY from Seville. Results show an electricity production greater than 75GWh per year, with a significant sparing fossil fuel consumption and avoided CO2 emissions. <br></p>
Project Overview
<p>
<b>1.0 INTRODUCTION</b></p><p><b>1.1 BACKGROUND STUDY</b> </p><p>The solar source, as known, is not a resource that ensures regularity of energy production;
consequently, its random nature leads to the search of systems able to capture the incident energy on the
terrestrial sphere in an effective and continuous manner. A particular category of systems that are suitable
for this application and are currently being developed in installations at an experimental stage [1] [7], or in
certain cases also commercial [2] are known as concentrating solar Brayton cycle. They are promising in
term of efficiency, low emissions and limited consumption of cooling water.
<br></p><p>
To compensate the lack of thermal power during the clouds transient, generally in this kind of systems
fuel is used by combustors to make always at nominal values the operating point. In this article the
possibility of combining an innovative control system for a solar concentrator closed intercooled
regenerated Brayton cycle, is analysed. Among the expected benefits of such a system, there is a good
energy yield, which is almost constant regardless of the intensity of solar radiation, without the emission
of greenhouse gases.
This technology, in fact, avoids the use of combustors, and thus it increases the heat energy from fossil
fuels, ensuring, at the same time, a large margin of regulation </p><p>
Nomenclature </p><p> Product of heat exchange coefficient global for the exchange surface </p><p>Avg Average value calculate for every months Opt </p><p>Opt Optimal value
i Represent the number of the month on thesum
ܲ </p><p>P. Average pressure of the air on cycle </p><p>Vc Volume control
MW Molecular weight of the air </p><p>R Universal constant of ideal gases </p><p>T Average temperature of the air in the principal cycle </p><p>TIT Temperature Intel Turbin
<br></p>