4.7 Article

Transient analysis and control of a heat to power conversion unit based on a simple regenerative supercritical CO2 Joule-Brayton cycle

Journal

APPLIED THERMAL ENGINEERING
Volume 183, Issue -, Pages -

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.applthermaleng.2020.116214

Keywords

Supercritical CO2 power cycle; Waste heat recovery; Power generation; Transient modelling; Turbine inlet temperature control; Inventory control system

Funding

  1. European Union [680599]
  2. Engineering and Physical Sciences Research Council (EPSRC) of the UK [EP/P004636/1]
  3. Centre for Sustainable Energy Use in Food Chains (CSEF), an End Use Energy Demand Centre
  4. Research Councils UK [EP/K011820/1]

Ask authors/readers for more resources

Supercritical carbon dioxide (sCO(2)) heat to power systems are considered a promising technology, but their dynamic behavior during part-load and transient operation is still not well understood and further research is needed. The current research aims to fill these gaps by proposing a one-dimensional transient modeling formulation and demonstrating the system's flexibility.
Supercritical carbon dioxide (sCO(2)) heat to power systems are a promising technology thanks to their potential for high efficiency and operational flexibility. However, their dynamic behaviour during part-load and transient operation is still not well understood and further research is needed. Additionally, there is not enough literature addressing suitable control approaches when the objective is to follow the dynamics of heat load supplied by the topping process to maximise the power recovery. The current research aims to fill these gaps by proposing a one-dimensional transient modelling formulation calibrated against the major components of a 50 kW(e) sCO(2) test facility available at Brunel University London. The dynamic analysis showed that the system quickly adapts to a 2800s transient heat load profile, proving the flexible nature of the sCO(2) system investigated. The turbine bypass, during startup and shutdown modes of operation, enabled gradual and safe build-up/decline of the pressures and temperatures throughout the loop. The regulation of the inventory in the range 20-60 kg allowed a 30% variation of the turbine inlet temperature with lower penalties on system performance than the turbomachinery speed control. The designed proportional-integral inventory controller showed a rapid response in the control of the turbine inlet temperature around the set point of 773 K during large variations of the heat load.

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