Testing of a 40-kWth Counterflow Particle-Supercritical Carbon Dioxide Narrow-Channel, Fluidized Bed Heat Exchanger
DOI:
https://doi.org/10.52825/solarpaces.v1i.634Keywords:
Concentrating Solar Power, Particle Heat Exchangers, Fluidized Bed Heat TransferAbstract
Particle-based primary heat exchangers (HXs) must deliver sCO2 fluid temperatures above 700°C to couple particle-based concentrating solar receivers and thermal energy storage (TES) sub-systems with efficient sCO2 power cycles. Particle-sCO2 HX designs have struggled to meet DOE cost targets (≤ $150/kWth) due to the amount of expensive nickel alloys necessary for manufacturing full-scale, particle-sCO2 HXs. Our team has demonstrated that mild bubbling fluidization of falling particles in a counterflow narrow-channel fluidized bed can reduce required HX surface area and thus, costs by increasing particle-wall heat transfer coefficients hT,w > 800 W m-2 K-1. This paper reports on the fabrication and testing of a stainless steel, particle-sCO2 HX with 12 fluidized-bed channels approximately 10.5 mm deep spaced between diffusion-bonded, micro-channel sCO2 plates. The HX with a core length of ≈0.56 m is fed with CARBOBEAD HSP particles through a short, fluidized freeboard zone just above the core. Testing to date in the National Solar Thermal Test Facility (NSTTF) at Sandia National Laboratories has shown that parallel bed fluidization maintains uniform particle inventory across the instrumented channels. Heat transfer thermal duty between the particle and sCO2 flows exceeds 30 kWth with sCO2 inlet temperatures of 200ºC and particle inlet temperatures up to 440ºC and mass flow rates of 0.2 kg s-1 fluidized by counterflowing gas flow rates of 0.005 kg s-1. Tests at higher particle and sCO2 inlet temperatures (600ºC and 400ºC respectively) are targeted to achieve > 40 kWth with model-predicted overall heat transfer coefficients U > 400 W m-2 K-1.
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Mehos M, Turchi C, Vidal J, Wagner M, Ma Z, Ho C, et al., "Concentrating Solar Power Gen3 Demonstration Roadmap"., NREL Technical Report #NREL/TP-5500-67464 , National Renewable Energy Laboratory, US Dept. of Energy 2017. DOI: https://doi.org/10.2172/1338899.
Ho CK, Carlson M, Garg P, Kumar P., "Technoeconomic Analysis of Alternative Solarized s-CO2 Brayton Cycle Configurations.", Journal of Solar Energy Engineering-Transactions of the ASME. 2016;138. DOI: https://doi.org/10.1115/1.4033573.
Albrecht KJ, Ho CK. "Design and operating considerations for a shell-and-plate, moving packed bed, particle-to-sCO2 heat exchanger.", Solar Energy., 2019;178:331-40. DOI: https://doi.org/10.1016/j.solener.2018.11.065.
Baumann T, Zunft S, Tamme R. "Moving Bed Heat Exchangers for Use With Heat Storage in Concentrating Solar Plants: A Multiphase Model." Heat Transfer Engineering., 2014;35:224-31. DOI: https://doi.org/10.1080/01457632.2013.825154.
Albrecht KJ, Carlson MD, Laubscher HF, Crandell R, DeLovato N, Ho CK. "Testing and model validation of a prototype moving packed-bed particle-to-sCO2 heat exchanger.", AIP Conference Proceedings, 2020;2303:030002.
Keplinger T, Haider M, Steinparzer T, Patrejko A, Trunner P, Haselgrübler M. "Dynamic simulation of an electric arc furnace waste heat recovery system for steam production.", Applied Thermal Engineering. 2018;135:188-96. DOI: https://doi.org/10.1016/j.applthermaleng.2018.02.060.
Yu Q, Yang Y, Wang Z, Zhu H. "Modeling and parameter sensitivity analysis of fluidized bed solid particle/sCO2 heat exchanger for concentrated solar power plant.", Applied Thermal Engineering., 2021;197:117429. DOI: https://doi.org/10.1016/j.applthermaleng.2021.117429.
Miller DC, Pfutzner CJ, Jackson GS. "Heat transfer in counterflow fluidized bed of oxide particles for thermal energy storage.", International Journal of Heat and Mass Transfer. , 2018;126:730-45. DOI: https://doi.org/10.1016/j.ijheatmasstransfer.2018.05.165.
Fosheim JR, Hernandez X, Abraham J, Thompson A, Jesteadt B, Jackson GS, et al. "Narrow-channel fluidized beds for particle-sCO2 heat exchangers in next generation CPS plants.", AIP Conference Proceedings, 2022;2445:160007.
Molerus O. "Heat-transfer in gas fluidized beds 2. Dependence of heat transfer on gas velocity.", Powder Technology, 1992;70:15-20. DOI: https://doi.org/10.1016/0032-5910(92)85049-2.
Fosheim JR, Hernandez X, Arthur-Arhin WJ, Thompson AB, Bowen CP, Albrecht KJ, et al. "Design of a 40-kWth Counterflow Particle-Supercritical Carbon Dioxide Narrow-Channel Fluidized Bed Heat Exchanger.", In: R. B, editor. SolarPACES 2021: International Conference on Concentrating Solar Power and Chemical Energy Systems2021.
K. J. Albrecht, H. F. Laubscher, C. P. Bowen, and C. K. Ho, “Performance Evaluation of a Prototype Moving Packed-Bed Particle / sCO2 Heat Exchanger,” Sandia Report, SAND2022-12615, September 2022. DOI: https://doi.org/10.2172/1887943.
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Copyright (c) 2024 Winfred Arthur-Arhin, Jesse R. Fosheim, Keaton J. Brewster, Azariah Thompson, Kevin J. Albrecht, Dereje Amogne, Gregory S. Jackson
This work is licensed under a Creative Commons Attribution 4.0 International License.
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Solar Energy Technologies Office
Grant numbers DE-EE0008538