System Design, Optimization and 2nd Law Analysis of a 100 MWe Double Reheat s-CO2 Power Plant at Full Load and Part Loads

Author:

Manavalla Sreekanth12ORCID,M. Feroskhan2ORCID,Daniel Joseph2,Ramasamy Sivakumar2,Yunus Khan T. M.3ORCID,Baig Rahmath Ulla4ORCID,Almakayeel Naif4ORCID,Voddin Tirumalapur Bhanu Kiran2

Affiliation:

1. Electric Vehicle Incubation, Testing and Research Centre, Vellore Institute of Technology Chennai, Chennai 600127, India

2. School of Mechanical Engineering, Vellore Institute of Technology Chennai, Chennai 600127, India

3. Department of Mechanical Engineering, College of Engineering, King Khalid University, Abha 61421, Saudi Arabia

4. Department of Industrial Engineering, College of Engineering, King Khalid University, Abha 61421, Saudi Arabia

Abstract

Super-critical Carbon dioxide (s-CO2) power plants are considered to be efficient and environmentally friendly compared to the traditional Rankine cycle-based steam power plants and Brayton cycle-based gas turbine power plants. In this work, the system design of a coal-fired 100 MWe double reheat s-CO2 power plant is presented. The system is also optimized for efficiency with turbine inlet pressures and the recompression ratio as the variables. The components needed, mass flow rates of various streams and their pressures at various locations in the system have been established. The plant has been studied based on 1st and 2nd laws at full load and at part loads of 80%, 60% and 40%. Operating parameters such as mass flow rate, pressure and temperature have considerably changed in comparison to full load operation. It was also observed that the 1st law efficiency is 53.96%, 53.93%, 52.63% and 50% while the 2nd law efficiency is 51.88%, 51.86%, 50.61% and 48.1% at 100%, 80%, 60% and 40% loads, respectively. The power plant demonstrated good performance even at part loads, especially at 80% load, while the performance deteriorated at lower loads. At full load, the highest amount of exergy destruction is found in the main heater (36.6%) and re-heaters (23.2% and 19.6%) followed by the high-temperature recuperator (5.7%) and cooler (4.1%). Similar trends were observed for the part load operation. It has been found that the recompression ratio should be kept high (>0.5) at lower loads in order to match the performance at higher loads. Combustion and heat exchange due to finite temperature differences are the main causes of exergy destruction, followed by pressure drop.

Funder

King Khalid University

Publisher

MDPI AG

Subject

Management, Monitoring, Policy and Law,Renewable Energy, Sustainability and the Environment,Geography, Planning and Development,Building and Construction

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