Fig. 1. Schematic diagram of the CLEAR-I structure 1. Reactor core, 2. Central measuring column, 3. Heat exchanger, 4. Air cooler, 5. Safety container
Fig. 2. Heat exchanger composition structure diagram 1. Center downcormer, 2. Double layer heat exchange tube, 3. Shell of heat exchanger, 4. Pressure chamber, 5. Upper tube sheet, 6. Lower tube sheet, 7. Secondary side inlet, 8. Secondary side outlet, 9. Liquid metal inlet window, 10. Liquid metal outlet window, 11. Discharge chamber, 12. Flow distribution device, 13. Secondary side coolant mixing device, 14. Heat shielded housing
Fig. 3. Coolant flow direction diagram
Fig. 4. Variation of the number of heat exchanger tubes with the tube length
Fig. 5. Variation of total heat transfer coefficient with the tube length
Fig. 6. Effect of heat exchanger tube length the on shell-side (a) and tube-side (b) pressure drop
Fig. 7. Effect of heat exchanger tube length on the JF factor
Fig. 8. Variation of total heat transfer coefficient with the outer diameter
Fig. 9. Effect of the outer diameter of heat exchanger tube on shell-side pressure drop (a) and tube-side pressure drop (b)
Fig. 10. Effect of outer diameter of heat exchanger tube on the JF factor
Fig. 11. Variation of total heat transfer coefficient with wall thickness
Fig. 12. Effect of heat exchanger tube wall thickness on tube-side pressure drop
Fig. 13. Effect of heat exchanger tube wall thickness on the JF factor
Fig. 14. Effect of heat exchanger tube spacing on the shell-side pressure drop
Fig. 15. Effect of heat exchanger tube spacing on the JF factor
Fig. 16. Contribution ratio of each parameter
Fig. 17. Variation curve of JF factor (a) and CER (b) factor with number of iterations
热工水力参数Thermal hydraulic parameters | 数值Values |
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设计热功率Design thermal power / MW | 3 | 加压水质量流量Pressurized water mass flow rate / kg·s-1 | 40.21 | 铅铋质量流量Lead-bismuth mass flow rate / kg·s-1 | 158.844 | 加压水进出口温度Pressurized water inlet and outlet temperature / ℃ | 215/230 | 液态铅铋进出口温度Liquid lead and bismuth inlet and outlet temperature / ℃ | 390/260 |
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Table 1. Main thermal-hydraulic parameters of the primary heat exchanger
参数 Parameters | 换热管长度 Length of heat exchange tube / m | 换热管外径 Outer diameter of heat exchange tube / mm | 换热管壁厚 Heat exchange tube wall thickness / mm | 换热管管间距 Distance between heat exchange tubes / mm |
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初始值Initial values | 2.985 | 26 | 4 | 32 |
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Table 2. Preliminary design parameters of the main heat exchanger
设计参数Design parameters | 取值范围 Range of values |
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换热管外径Heat exchange tube outer diameter / mm | [19, 33] | 换热管壁厚Heat exchange tube wall thickness / mm | [3.5, 4.5] | 换热管长度Heat exchange tube length / m | [1.2, 4.8] | 换热管间距Heat exchange tube spacing / mm | [41, 43] |
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Table 3. Design parameter range of the heat exchanger tube
参数 Parameters | 初始参数 Initial parameters | JF因子最大时参数 Parameters at maximum JF factor | CER因子最大时参数 Parameters at maximum CER factor |
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换热管外径Heat exchange tube outer diameter / mm | 26 | 32.48 | 32.08 | 换热管壁厚Heat exchange tube wall thickness / mm | 4 | 3.5 | 3.5 | 换热管长度Heat exchange tube length / m | 2.985 | 1.573 | 1.768 | 换热管间距Heat exchange tube spacing / mm | 32 | 41.51 | 41.32 | 总传热系数Total heat transfer coefficient / W·(m2·K)-1 | 1 505 | 1 565.75 | 1 592.12 | 一回路压降First circuit pressure drop / Pa | 586.7 | 451.7 | 600.3 | JF因子JF factors | 1 | 1.14 | 1.05 | CER因子CER factors | 0.157 6 | 0.192 9 | 0.196 4 |
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Table 4. Comparison of heat exchanger performance before and after optimization