Numerical simulation of the flow instability between two heated parallel channels with supercritical water

2014 ◽  
Vol 64 ◽  
pp. 57-66 ◽  
Author(s):  
Xi Xi ◽  
Zejun Xiao ◽  
Xiao Yan ◽  
Ting Xiong ◽  
Yanping Huang
Author(s):  
Jingjing Li ◽  
Tao Zhou ◽  
Mingqiang Song ◽  
Yanping Huang

3-D simulation of supercritical water flow instability in parallel channels and a natural circulation loop are presented. Results are obtained for various heating powers. The results show that, in the natural circulation loop the steady state mass flow will firstly increase with the heating power and then decrease. And mass flow grows with the growing of the inlet temperature, decreases with the growing of system pressure. Under a large heat flux, the parallel channels will experience the flow instability of out phase mass flow oscillation. And the oscillation amplitude will grow with the growing of heating power. At last, the numerical simulations are validated by B.T. Swapnalee’s experience formula.


2016 ◽  
Vol 2 (3) ◽  
Author(s):  
Yuzhou Chen ◽  
Chunsheng Yang ◽  
Minfu Zhao ◽  
Keming Bi ◽  
Kaiwen Du

An experiment of natural circulation of supercritical water in parallel channels was performed in bare tubes of inner diameter 7.98 mm and heated length 1.3 m, covering the ranges of pressure of 24.7–25.5 MPa, mass flux of 400–1000  kg/m2 s, and heat flux of up to 1.83  MW/m2. When the heat flux reached 1.12  MW/m2, the outlet water temperature jumped from 325°C to 360°C, associated with a decrease in the flow rate and an initiation of dynamic instability. When the heat flux exceeded 1.39  MW/m2, the flow instability was stronger, and the flow rate increased in one channel and decreased in another one. Until the heat flux reached 1.61  MW/m2, the outlet water temperatures of two channels reached the pseudocritical point, and the flow rates of two channels tended to close each other. The experiment with a single heated channel was also performed for comparison. The measurements on the heat-transfer coefficients (HTCs) were compared to the calculations by the Bishop et al., Jackson’s, and Mokry et al. correlations, showing different agreements within various conditions.


2012 ◽  
Vol 48 ◽  
pp. 60-67 ◽  
Author(s):  
Ting Xiong ◽  
Xiao Yan ◽  
Zejun Xiao ◽  
Yongliang Li ◽  
Yanping Huang ◽  
...  

2017 ◽  
Vol 110 ◽  
pp. 196-207 ◽  
Author(s):  
Edward Shitsi ◽  
Seth Kofi Debrah ◽  
Vincent Yao Agbodemegbe ◽  
Emmanuel Ampomah-Amoako

2013 ◽  
Vol 68 ◽  
pp. 169-176 ◽  
Author(s):  
Yali Su ◽  
Jian Feng ◽  
Hao Zhao ◽  
Wenxi Tian ◽  
Guanghui Su ◽  
...  

2020 ◽  
Vol 144 ◽  
pp. 107586
Author(s):  
Jialun Liu ◽  
Huixiong Li ◽  
Xianliang Lei ◽  
Zongrui Feng ◽  
Yun Hao

Author(s):  
Yali Su ◽  
Jian Feng ◽  
Wenxi Tian ◽  
Suizheng Qiu ◽  
Guanghui Su

For the flow of the supercritical water (SCW), the fierce variation of density and specific volume possibly cause flow instability. Based on the structure of parallel channels, mathematical and physical models were established to simulate the flow and heat transfer characteristics of the supercritical water in the parallel channels with semi-implicit scheme and staggered mesh scheme. Flow instability of super-critical water was obtained by using the little perturbation method. Pseudo-subcooling number (NSUB) and pseudo-phase change number (NPCH) are defined based on the property of SCW. The marginal stability boundary (MSB) is obtained with using the NSUB and NPCH. The effects of mass flow rate, inlet temperature and system pressure on the flow instability boundary were also investigated. When increasing the mass flows and system pressure, decreasing the heat flux, the stability in the parallel channels increases. The effect of inlet temperature in the low pseudo-subcooling number region is different from that in high pseudo-subcooling number region.


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