Thermal analysis of HTGR helical tube once through steam generators using 1D and 2D methods

Li, Xiaowei; Gao, Weikai; Yang, Shuangyan; Wu, Xinxin

doi:10.1016/j.nucengdes.2019.110352

Cited by 20 publications

(2 citation statements)

References 18 publications

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“…Various researchers have implemented their study on heat transfer through the helical coils with the assumption of constant heat flux and constant working fluid properties, which are idealized ones [2]. Geometrical and thermal-hydraulic deviations in an HTGR steam generator will result in temperature deviations from the ideal design cases [3]. The helical coil heat exchanger should use a small diameter coil and large diameter pipe because it gives desirable pressure and temperature drop [4].…”

Section: Introduction mentioning

confidence: 99%

Design of Helical Type Steam Generator for Experimental Power Reactor

Putri,

Darmanto,

Subekti

2023

Tri Dasa Mega

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Reaktor Daya Eksperimental (RDE) is a high-temperature gas-cooled reactor (HTGR) for electricity generation, heat generation, and hydrogen production by Batan. Empirical and numerical calculations are needed to strengthen the existing design. The numerical method by computational fluid dynamic (CFD) analyzes temperature distribution and pressure drop along the pipe. The Batan RDE steam generator design has a seven-layer helical pipe model, while this research uses a one-layer helix pipe. In empirical calculations, the heat transfer region has three sections; single-phase liquid, two-phase, and single-phase vapor heat transfer. In numerical calculations, apply the assumption of constant heat flux and constant working fluid properties. The results of empiric calculations data showed that the helical pipe height was 3.98 m, shorter than the Batan design, which is 4.97 m. This considerable difference due to empirical calculations did not cover the safety factor. The results of numerical calculations show that in the single-phase, empiric calculation data were acceptable since the different values of numerical calculations for empiric calculations data were below 10%. Meanwhile, the case of the two-phase numerical calculations is not satisfactory and needs further research to obtain optimal results.

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Section: Introduction mentioning

confidence: 99%

Design of Helical Type Steam Generator for Experimental Power Reactor

Putri,

Darmanto,

Subekti

2023

Tri Dasa Mega

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“…Works have been conducted to investigate the in-unit temperature non-uniformity (among the helical heat transfer tubes). It has been reported that the wall effect, helical effect, temperature mixing effect, reverse winding of adjacent helical tube layers in the tube bundle, and geometrical parameter variations induced by the fabrication tolerance are the main reasons for in-unit temperature non-uniformity (Li and Wu, 2013;Olson et al, 2014;Li et al, 2014;Iacovides et al, 2014;Li et al, 2019b;da Silva et al, 2019;Gao et al, 2020). Furthermore, the above-mentioned in-unit temperature non-uniformity has also been experimentally verified in the 10-MW engineering test facility-steam generator (ETF-SG) for the HTR-PM (Zhang et al, 2016).…”

Section: Introductionmentioning

confidence: 99%

Numerical Investigation of Hot Helium Flow Homogenizer on Inter-Unit Flow Rate Uniformity of HTGR Once Through Steam Generator

Qin

Luo

et al. 2022

Front. Energy Res.

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High working temperature is a major feature of the high temperature gas-cooled reactor (HTGR). The helical tube once through steam generator (OTSG) should maintain appropriate temperature uniformity. The temperature non-uniformity of the HTGR OTSG includes the in-unit and inter-unit temperature non-uniformity, while the latter is mainly induced by the inter-unit flow rate non-uniformity of primary-side hot helium, which is significantly affected by the inlet structure. In this work, a new inlet structure with a hot helium flow homogenizer is designed, and its flow distribution characteristics are numerically investigated. Accordingly, the optimal geometrical parameters are determined, such as the circular hole diameter on the end wall, the square hole size, and arrangement on the cylinder wall. Increasing the resistance of the flow homogenizer with non-uniformly arranged square holes (NUASHs) can improve inter-unit flow rate uniformity because it decreases the effect of static pressure difference caused by dynamic pressure. Two design parameters (resistance coefficient and flow area ratio of the square hole on both sides) are introduced to evaluate the structure effect of the hot helium flow homogenizer on inter-unit flow rate distribution. They are recommended within the ranges of (7.81–22.42) and (0.53–1.64), respectively. In these recommended ranges, the suction phenomenon near the hot helium inlet can be effectively suppressed, with the critical resistance coefficient of 7.63. By coupling with 19 heat exchange units, the overall performance of the hot helium flow homogenizer is better than that of the current inlet structure with a baffle, with the maximum inter-unit flow rate deviation decreased from 2.97% to 0.30%. This one-magnitude enhancement indicates that the hot helium flow homogenizer with NUASHs is a promising solution to improve inter-unit flow rate uniformity of the HTGR OTSG.

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