Elsevier

Fusion Engineering and Design

Volume 146, Part B, September 2019, Pages 1520-1523
Fusion Engineering and Design

Analysis of supercritical CO2 Brayton power cycles in nuclear and fusion energy

https://doi.org/10.1016/j.fusengdes.2019.02.119Get rights and content

Abstract

The first part of this article focuses on proposal of the appropriate cooling cycle for the specific fusion reactor. Furthermore, cooling technology of fusion power plant, two supercritical CO2 Brayton cycles and its positive and negative aspects are described. Additionally, comparison of cycles in terms of difficulty and possibilities of using more resources at once are depicted. This work also gives a principal preview of main technical parameters of supercritical CO2 cooling system. The second part describes the optimization of suggested design in order to maximize power of a fusion power plant and new computational software for optimization of the cooling cycles therewith, which would be also useful in the field of nuclear power engineering. The results of this article is comparison of efficiencies, power and other physical parameters of two layouts.

Introduction

The possibility of using supercritical carbon dioxide(S-CO2) as a cooling medium was first introduced by E.G. Feher in 1967, which is described in the literature, e.g. [1]. From that time many investigations were done in the field of supercritical CO2 as a cooling medium in fission and fusion reactors as well. For instance Hejzlar et al. described supercritical CO2 Re-compression Brayton cycle as a promising power conversion system for sodium fast reactor (Generation IV fission reactors) [2]. The goal is to increase operating temperature, which means to increase the efficiency of nuclear power reactors, that is nowadays lower than efficiency of fossil power plants [3]. The computational analysis also proves that varieties of the supercritical CO2 power cycle brings many benefits compared to Rankine steam cycles and also Helium cycles [1], [4].

Against Rankine steam cycles supercritical CO2 power cycles are more compact and they are simpler in some respect. Benefits compared to conventional Rankine steam cycle are also in finances. For turbine inlet temperature 550 °C and compressor outlet pressure 20 MPa is the cost of the power plant reduced by approximately 18% [1].

Against Helium cooling cycles supercritical CO2 cycles work on lower temperatures with the same efficiency and work of compressors is lower by up to 33% [1].

It means that there is a possibility of using supercritical CO2 as a power conversion cycle for fusion reactors.

Power conversion cycles heavily influence the efficiency of fusion power plants. The analysis of supercritical CO2 Brayton cycle power conversion system is being intensively solved in previous research, e.g. [5], where was concluded that the Re-compression supercritical CO2 Brayton cycle using Breeding Blanket, First Wall and Divertor as a heat source is an optimal version of Brayton cycle.

The work that leads to a design of a fusion power plant with supercritical CO2 power conversion cycle stands on the grounds of the studies that were made by Angelino, Feher, Verhivker, Gokhstein [1] and by actual works of Linares [4].

Section snippets

Comparison of supercritical CO2 Brayton and Rankine steam power conversion cycles

As many researchers described, there is a variety of advantages of supercritical CO2 against water and helium as well. The supercritical CO2 is more compact than water and helium. The compactness is clearly visible in the high operating pressure (more than 10 MPa), which positively influences robustness of the components [6].

For instance the difference of the size of the turbine is vast. This advantage is depicted in the literature, e.g. [1]. It was concluded, that the supercritical CO2 turbine

Technical specification of DEMO2 fusion power plant

Parameters for DEMO2 fusion power plant are available in open source literature, e.g. [7], and the main characteristics are depicted in the following Table 1. Important values are thermal power of heat sources (Blanket and First Wall (BNK), Divertor (D) and Vacuum Vessel (VV)) which, in the case of the multiple heat source, equals to 2500 MW.

Description of supercritical CO2 power cycle

Supercritical CO2 power cycles are based on Simple Brayton cycles and subsequent cycles are only variations and improvements of this basic cycle. It is possible to increase efficiencies of the cycles by including the second turbine or more compressors. Each option influences cycle efficiency, but the improvement is not always positive in all aspects which will be summarized in this paper.

Optimization software

In order to gain better and more detailed results, new computational software (CCOCS: Cooling Cycles Optimization Computational Software) was developed with experience from previous research [12].

The main benefit of this software is deeper and more detailed results, which were compared with the results of the previous research. It also gives more information about heat flux in recuperators, thermal conditions in recuperators and it is possible to optimize the cycle on any physical value,

Optimization of supercritical CO2 power cycles

The first compressor inlet temperature was chosen in order to avoid the critical temperature as t1 = 33 °C. Turbine inlet temperature was set tT = 480 °C.

The occurrence of pinch point was also studied and each cycle has been computed with a conditions that prevent negative temperature difference in pinch point. It means that negative difference between high temperature recuperator and low temperature recuperator was forbidden moreover the difference must not have exceeded 5 °C.

Additionally, for

Results

The exact model of the power plant is not the objective of this article thus the efficiency is computed only from the results of the power consumption of the compressors.

In Table 4 are the results of the calculation and in Table 3 are computed efficiencies of the recuperators.

The single Brayton cycle is usually taken as a reference cycle [11] therefore it serves for comparison with other cycles. The outcome efficiency does not have to be the lowest and whereas other cycles may have higher

Conclusion and future work

Main supercritical CO2 power conversion cycles and their optimization for DEMO2 fusion power plant were described in this article. New computational software (CCOCS) was invented which will be useful in the future research.

From the previous sentences it is visible that the most suitable cycle is the Re-compression cycle due to the highest calculated efficiency. It is also notable that the difference between efficiencies of the cycles for the multiple heat source assembly are minor and this

Acknowledgment

The work has been carried out within the framework of the project of “Centre for Advanced Applied Sciences” No. CZ.02.1.01/0.0/0.0/16_019/0000778 co-funded from European structural and investment funds and from the state budget of the Czech Republic.

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