Fig. 1. Geometric structure
Fig. 2. Schematic diagram of sub-channel numbering
Fig. 3. Distribution of liner power of fuel element
Fig. 4. Mesh sensitivity analysis (a) Subchannel 49, (b) Subchannel 21
Fig. 5. Schematic diagram of the block geometry
Fig. 6. Effect of blockage area on axial cladding temperature (a) Inner channel, (b) Outer channel
Fig. 7. Distribution of axial velocity field around blockage of case B2, B3, B4
Fig. 8. Radial temperature distribution at blockage (a) Inner channel, (b) Outer channel
Fig. 9. Effect of blockage thickness on axial cladding temperature (a) 25% blockage of inner channel, (b) 25% blockage of outer channel, (c) 75% blockage of inner channel, (d) 75% blockage of outer channel
Fig. 10. Distribution of axial velocity field around blockage of case A2, A4
Fig. 11. Radial temperature distribution at blockage (a) 25% blockage of inner channel, (b) 25% blockage of outer channel, (c) 75% blockage of inner channel, (d) 75% blockage of outer channel
Fig. 12. Effect of axial position of the blockage on axial cladding temperature (a) Inner channel, (b) Outer channel
参数 Parameter | 数值 Values |
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燃料棒数量 Rod number | 25 | 内包壳内径 Inner diameter of inner cladding / mm | 3.643 | 内包壳外径 Outer diameter of inner cladding / mm | 4.243 | 燃料芯块内径 Inner diameter of fuel pellet / mm | 4.393 | 燃料芯块外径 Outer diameter of fuel pellet / mm | 6.427 | 外包壳内径 Inner diameter of outer cladding / mm | 6.577 | 外包壳外径 Outer diameter of outer cladding / mm | 7.177 | 活性区长度 Length of active region / mm | 1 200 | 栅径比 Pitch to diameter ratio | 1.070 |
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Table 1. Geometry parameters of annular fuel assembly
结构材料 Structural material | 参数 Parameter | 数值 Values |
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液态铅铋 合金 LBE | 比热容 Specific heat | | 密度 Density | | 热导率 Thermal conductivity | | 粘性 Viscosity | 4.56 | 包壳 Cladding | 比热容 Specific heat | 509.61 | 密度 Density | 7 959.8 | 热导率 Thermal conductivity | 14.646 | 气隙 Gap | 比热容 Specific heat | 5 191 | 密度 Density | 2.425 | 热导率 Thermal conductivity | 0.51 | 氧化铀钚 MOX | 比热容 Specific heat | 307 | 密度 Density | 10 994 | 热导率 Thermal conductivity | 3.919 2 |
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Table 2. Material properties
参数Parameter | 数值Values |
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冷却剂类型 Type of coolant | LBE | 冷却剂进口温度 Coolant inlet temperature / K | 673.15 | 质量流量 Mass flow rate / kg·s-1 | 54.8 |
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Table 3. Operating parameters
工况编号 Case No. | 堵块厚度 Thickness / mm | 子通道编号 Subchannel number | 堵块起始高度 Start / mm | 占通道面积比例 Area percentage / % |
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A1 | 10 | 49 | 0 | 25 | B1 | 10 | 21 | 0 | 25 | A2 | 10 | 49 | 595 | 25 | B2 | 10 | 21 | 595 | 25 | A3 | 10 | 49 | 595 | 50 | B3 | 10 | 21 | 595 | 50 | A4 | 10 | 49 | 595 | 75 | B4 | 10 | 21 | 595 | 75 | A5 | 20 | 49 | 590 | 25 | B5 | 20 | 21 | 590 | 25 | A6 | 20 | 49 | 590 | 75 | B6 | 20 | 21 | 590 | 75 | A7 | 30 | 49 | 585 | 25 | B7 | 30 | 21 | 585 | 25 | A8 | 30 | 49 | 585 | 75 | B8 | 30 | 21 | 585 | 75 |
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Table 4. Selected cases of blockage accident
子通道编号 Subchannel number | 堵塞面积 Area percentage / % | 工况编号 Case No. | 流量 Mass flow / kg·s-1 | 流量损失 Mass flow loss / % | 外通道热量份额 Outer channel heat share / % | 内通道热量份额 Inner channel heat share / % |
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49 | 0 | 正常工况 Normal | 0.744 363 40 | 0 | 60 | 40 | 25 | A2 | 0.716 657 13 | 3.722 1 | 62.5 | 37.5 | 50 | A3 | 0.592 132 28 | 20.451 2 | 66 | 34 | 75 | A4 | 0.260 966 99 | 64.940 9 | 73.7 | 26 | 21 | 0 | 正常工况Normal | 36.233 992 | 0 | 60 | 40 | 25 | B2 | 36.233 344 | 0.06 | 59.2 | 40.8 | 50 | B3 | 36.213 120 | 0.05 | 55.7 | 44.3 | 75 | B4 | 36.188 448 | 0.13 | 54.2 | 45.8 |
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Table 5. Effect of blockage area on mass flow and heat split in inner and outer channel
子通道编号 Subchannel number | 堵塞面积 Area percentage / % | 工况编号 Case No. | 流量 Mass flow / kg·s-1 | 流量损失 Mass flow loss / % | 外通道热量份额 Outer channel heat share / % | 内通道热量份额 Inner channel heat share / % |
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49 | 0 | 正常工况 Normal | 0.744 363 4 | 0 | 60 | 40 | 25 | A2 | 0.716 657 0 | 3.722 | 62.5 | 37.5 | A5 | 0.713 416 3 | 4.157 | 62.6 | 37.4 | A7 | 0.713 340 0 | 4.167 | 62.8 | 37.2 | 75 | A4 | 0.260 966 99 | 64.940 9 | 73.7 | 26.3 | A6 | 0.247 804 44 | 66.709 0 | 73.8 | 26.2 | A8 | 0.235 041 71 | 68.424 0 | 74 | 26 | 21 | 0 | 正常工况 Normal | 36.233 992 | 0 | 60 | 40 | 25 | B2 | 36.233 344 | 0.001 78 | 59.2 | 40.8 | B5 | 36.220 002 | 0.038 00 | 59.1 | 40.9 | B7 | 36.218 691 | 0.042 00 | 58.9 | 41.1 | 75 | B4 | 36.188 448 | 0.13 | 54.2 | 45.8 | B6 | 36.171 942 | 0.17 | 53.3 | 46.7 | B8 | 36.167 840 | 0.18 | 52.4 | 47.6 |
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Table 6. Effect of blockage thickness on mass flow and heat split in inner and outer channel
子通道编号 Subchannel number | 堵塞面积 Area percentage / % | 堵块厚度 Blockage thickness / mm | 工况编号 Case No. | 流量 Mass flow / kg·s-1 | 流量损失 Mass flow loss / % |
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49 | 0 | 10 | 正常工况 Normal | 0.744 363 4 | 0 | 25 | 10 | A1 | 0.702 245 92 | 5.645 1 | 10 | A2 | 0.716 657 13 | 3.722 1 | 21 | 0 | 10 | 正常工况 Normal | 36.233 992 | 0 | 25 | 10 | B1 | 36.227 118 | 0.68 | 10 | B2 | 36.233 344 | 0.001 |
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Table 7. Effect of axial position of the blockage on mass flow in inner and outer channel