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Simulation of the supercritical CO2 recompression Brayton power cycle with a high-temperature regenerator

Journal Article · · Energy Conversion and Management
 [1];  [2];  [2];  [2];  [3]
  1. Colorado School of Mines, Golden, CO (United States). Dept. of Mechanical Engineering; Colorado School of Mines, Golden, CO (United States)
  2. Univ. of Wisconsin, Madison, WI (United States). Dept. of Mechanical Engineering
  3. Colorado School of Mines, Golden, CO (United States). Dept. of Mechanical Engineering
The supercritical carbon dioxide (sCO2) recompression Brayton cycle promises higher efficiency and lower capital cost than traditional steam Rankine power cycles. However, achieving high efficiency requires large, highly effective recuperators. Regenerators may be a low-cost alternative to printed circuit and micro-tube heat exchangers for recuperation in sCO2 power cycles. Regenerators are a periodic heat exchanger in which thermal energy is extracted from the hot stream, stored in solid media, and then released to the cold stream at a later time. Fixed bed regenerators with valves to direct fluid are the preferred method for implementing regenerators in power cycles, but the inherently transient nature of these systems has not been characterized for this application. This study presents the simulation of a high-temperature regenerator within a 10 MWe sCO2 recompression Brayton cycle. A transient, one-dimensional regenerator model presented in a previous study is used to simulate the regenerator. Dynamic heat exchanger models are also developed for the precooler, low-temperature recuperator, and primary heat exchanger, and the compressors and the turbine are modeled with off-design performance maps. We assess two regenerator-valve design options; one for fast switching, and one for reduced flow rate fluctuations. System simulation finds that both designs see significant fluctuations in turbomachinery flow rate, turbomachinery and system power, and regenerator discharge process outlet temperature. While designing the regenerator-valve subsystem for lower fluctuations is possible, the regenerator cold discharge temperature and net power still fluctuate by ±77.6°C and 6%, respectively. Increasing buffer volume is not effective at sufficiently reducing these fluctuations, but adding a packed bed in between the regenerator and the primary heat exchanger can reduce regenerator discharge process outlet temperature fluctuations to 6.4°C. Further reductions could be possible by increasing the size of this packed bed.
Research Organization:
Sarasota County, Inc., FL (United States)
Sponsoring Organization:
USDOE; USDOE Office of Energy Efficiency and Renewable Energy (EERE)
Grant/Contract Number:
EE0001720
OSTI ID:
1848394
Alternate ID(s):
OSTI ID: 1777011
Journal Information:
Energy Conversion and Management, Journal Name: Energy Conversion and Management Journal Issue: C Vol. 229; ISSN 0196-8904
Publisher:
ElsevierCopyright Statement
Country of Publication:
United States
Language:
English

References (23)

A solution to the periodic-flow regenerative heat exchanger problem journal January 1961
The supercritical thermodynamic power cycle journal September 1968
The regenerative heat exchanger computer representation journal September 1969
Transient response of periodic-flow regenerators journal July 1977
Asymmetric-unbalanced counterflow thermal regenerator problem: solution by the Galerkin method and meaning of dimensionless parameters journal February 1991
Recuperative and regenerative techniques at high temperature journal January 1983
Cost comparison of printed circuit heat exchanger to low cost periodic flow regenerator for use as recuperator in a s-CO2 Brayton cycle journal December 2017
Optimal design of microtube recuperators for an indirect supercritical carbon dioxide recompression closed Brayton cycle journal April 2018
Three-dimensional simulation of rotary air preheater in steam power plant journal December 2014
Modeling and analysis of a printed circuit heat exchanger for supercritical CO2 power cycle applications journal October 2016
Methodology to develop off-design models of heat exchangers with non-ideal fluids journal December 2018
One-dimensional, transient modeling of a fixed-bed regenerator as a replacement for recuperators in supercritical CO2 power cycles journal August 2020
Conceptual study of a high efficiency coal-fired power plant with CO2 capture using a supercritical CO2 Brayton cycle journal January 2013
Design, dynamic modeling, and control of a multistage CO2 compression system journal July 2017
High-efficiency thermodynamic power cycles for concentrated solar power systems journal February 2014
Mathematical models for the simulation of thermal regenerators: A state-of-the-art review journal May 2016
Supercritical carbon dioxide power cycle design and configuration optimization to minimize levelized cost of energy of molten salt power towers operating at 650 °C journal March 2019
Thermodynamic Study of Advanced Supercritical Carbon Dioxide Power Cycles for Concentrating Solar Power Systems journal June 2013
Multiscale Transient Thermal, Hydraulic, and Mechanical Analysis Methodology of a Printed Circuit Heat Exchanger Using an Effective Porous Media Approach journal October 2013
Design Considerations for Supercritical Carbon Dioxide Brayton Cycles With Recompression journal July 2014
Dry-Cooled Supercritical CO 2 Power for Advanced Nuclear Reactors journal August 2014
Thermal and Transport Properties of NaCl–KCl–ZnCl2 Eutectic Salts for New Generation High-Temperature Heat-Transfer Fluids journal June 2016
Concentrating Solar Power Gen3 Demonstration Roadmap report January 2017