• NUCLEAR TECHNIQUES
  • Vol. 46, Issue 10, 100606 (2023)
Junkang YANG1, Kai WANG1, Pengcheng ZHAO1、*, and Guimei WANG2
Author Affiliations
  • 1School of Nuclear Science and Technology, University of South China, Hengyang 421001, China
  • 2China Nuclear Industry Huawei Engineering Design and Research Co., Ltd., Nanjing 210019, China
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    DOI: 10.11889/j.0253-3219.2023.hjs.46.100606 Cite this Article
    Junkang YANG, Kai WANG, Pengcheng ZHAO, Guimei WANG. Design and optimization analysis of a new double-layered tube-type main heat exchanger for lead-bismuth reactors[J]. NUCLEAR TECHNIQUES, 2023, 46(10): 100606 Copy Citation Text show less
    Schematic diagram of the CLEAR-I structure 1. Reactor core, 2. Central measuring column, 3. Heat exchanger, 4. Air cooler, 5. Safety container
    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
    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. 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
    Coolant flow direction diagram
    Fig. 3. Coolant flow direction diagram
    Variation of the number of heat exchanger tubes with the tube length
    Fig. 4. Variation of the number of heat exchanger tubes with the tube length
    Variation of total heat transfer coefficient with the tube length
    Fig. 5. Variation of total heat transfer coefficient with the tube length
    Effect of heat exchanger tube length the on shell-side (a) and tube-side (b) pressure drop
    Fig. 6. Effect of heat exchanger tube length the on shell-side (a) and tube-side (b) pressure drop
    Effect of heat exchanger tube length on the JF factor
    Fig. 7. Effect of heat exchanger tube length on the JF factor
    Variation of total heat transfer coefficient with the outer diameter
    Fig. 8. Variation of total heat transfer coefficient with the outer diameter
    Effect of the outer diameter of heat exchanger tube on shell-side pressure drop (a) and tube-side pressure drop (b)
    Fig. 9. Effect of the outer diameter of heat exchanger tube on shell-side pressure drop (a) and tube-side pressure drop (b)
    Effect of outer diameter of heat exchanger tube on the JF factor
    Fig. 10. Effect of outer diameter of heat exchanger tube on the JF factor
    Variation of total heat transfer coefficient with wall thickness
    Fig. 11. Variation of total heat transfer coefficient with wall thickness
    Effect of heat exchanger tube wall thickness on tube-side pressure drop
    Fig. 12. Effect of heat exchanger tube wall thickness on tube-side pressure drop
    Effect of heat exchanger tube wall thickness on the JF factor
    Fig. 13. Effect of heat exchanger tube wall thickness on the JF factor
    Effect of heat exchanger tube spacing on the shell-side pressure drop
    Fig. 14. Effect of heat exchanger tube spacing on the shell-side pressure drop
    Effect of heat exchanger tube spacing on the JF factor
    Fig. 15. Effect of heat exchanger tube spacing on the JF factor
    Contribution ratio of each parameter
    Fig. 16. Contribution ratio of each parameter
    Variation curve of JF factor (a) and CER (b) factor with number of iterations
    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
    设计热功率Design thermal power / MW3
    加压水质量流量Pressurized water mass flow rate / kg·s-140.21
    铅铋质量流量Lead-bismuth mass flow rate / kg·s-1158.844
    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
    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

    初始值Initial values2.98526432
    Table 2. Preliminary design parameters of the main heat exchanger
    设计参数Design parameters取值范围 Range of values
    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]
    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

    换热管外径Heat exchange tube outer diameter / mm2632.4832.08
    换热管壁厚Heat exchange tube wall thickness / mm43.53.5
    换热管长度Heat exchange tube length / m2.9851.5731.768
    换热管间距Heat exchange tube spacing / mm3241.5141.32
    总传热系数Total heat transfer coefficient / W·(m2·K)-11 5051 565.751 592.12
    一回路压降First circuit pressure drop / Pa586.7451.7600.3
    JF因子JF factors11.141.05
    CER因子CER factors0.157 60.192 90.196 4
    Table 4. Comparison of heat exchanger performance before and after optimization
    Junkang YANG, Kai WANG, Pengcheng ZHAO, Guimei WANG. Design and optimization analysis of a new double-layered tube-type main heat exchanger for lead-bismuth reactors[J]. NUCLEAR TECHNIQUES, 2023, 46(10): 100606
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