Abstract

Supercritical carbon dioxide (sCO2) cycles can achieve higher efficiencies than an equivalent steam Rankine cycle at higher turbine inlet temperatures (>550 °C) with a compact footprint (tenfold). sCO2 cycles are low-pressure ratio cycles (~4–7), therefore recuperation is necessary, which reduces the heat-addition temperature range. Integration of sCO2 cycles with the boiler requires careful management of low-temperature heat to achieve higher plant efficiency. This study analyses four novel sCO2 cycle configurations which capture the low-temperature heat in an efficient way and the performance is benchmarked against the state-of-the-art steam Rankine cycle. The process parameters (13–16 variables) of all the cycle configurations are optimised using a genetic algorithm for two different turbine inlet temperatures (620 °C and 760 °C) and their techno-economic performance are compared against the advanced ultra-supercritical steam Rankine cycle. A sCO2 power cycle can achieve a higher efficiency than a steam Rankine cycle by about 3–4% points, which is correspond to a plant level efficiency of 2–3% points, leading to cost of electricity (COE) reduction. Although the cycle efficiency has increased when increasing turbine inlet temperature from 620 °C to 760 °C, the COE does not notably reduce owing to the increased capital cost. A detailed sensitivity study is performed for variations in compressor and turbine isentropic efficiency, pressure drop, recuperator approach temperature and capacity factor. The Monte-Carlo analysis shows that the COE can be reduced up to 6–8% compared to steam Rankine cycle, however, the uncertainty of the sCO2 cycle cost functions can diminish this to 0–3% at 95% percentile cumulative probability.

Highlights

  • A flexible thermal power plant has a significant role in the future energy view to maximise higher penetration of variable renewable en­ ergy generation into the grid

  • This paper investigates four novel thermodynamic cycle configura­ tions, which are the variants of recompression, partial cooling cycle, and cascade cycle for two different turbine inlet temperature (TIT) (620 ◦C and 760 ◦C)

  • The plant efficiency of all the four cycles are roughly similar for a TIT of 620 ◦C, partial cooling cycle is preferred owing to its superior off-design performance than recompression cycle at higher ambient temperatures [20]

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Summary

Introduction

A flexible thermal power plant has a significant role in the future energy view to maximise higher penetration of variable renewable en­ ergy generation into the grid. Wei et al [27] performed a techno-economic analysis of sCO2 cycle integrated coal/biomass fired power plant with oxycombustion, concluding that efficiency of 30.5% is achievable using coal as a fuel at a cost of 84.2 €/MWh. Huang and Sonwane [28] has modelled a double recuperation recompression Brayton cycle and concluded that the TIT is the main driver to increase the efficiency than the turbine inlet pressure. This cycle is developed for two reasons, 1) to provide an additional degree of freedom which fa­ cilitates the better matching of the T-Q profile (Fig. 4) in the recuperator and primary heat exchanger, reducing the exergy destruction 2) to reduce the heat load of the HTR, which uses an expensive material when the maximum temperature goes over 550 ◦C, so that the cost of recu­ perators can be lowered. The temperature-heat duty (T-Q) diagram of the low temperature recuperator (LTR), high temperature recuperator (HTR)

Thermodynamic modelling
Modelling assumptions
Metaheuristic optimisation
Model validation
Thermal performance comparison
Economic performance
Monte-Carlo uncertainty analysis
Conclusions
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