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严重事故专用卸压阀排放能力需求

武铃珺 邓坚 张航 王小吉 刘丽莉 青涛

武铃珺, 邓坚, 张航, 等. 严重事故专用卸压阀排放能力需求[J]. 强激光与粒子束, 2021, 33: 076001. doi: 10.11884/HPLPB202133.210062
引用本文: 武铃珺, 邓坚, 张航, 等. 严重事故专用卸压阀排放能力需求[J]. 强激光与粒子束, 2021, 33: 076001. doi: 10.11884/HPLPB202133.210062
Wu Lingjun, Deng Jian, Zhang Hang, et al. Discharge capacity requirements of severe accident depressurization valves[J]. High Power Laser and Particle Beams, 2021, 33: 076001. doi: 10.11884/HPLPB202133.210062
Citation: Wu Lingjun, Deng Jian, Zhang Hang, et al. Discharge capacity requirements of severe accident depressurization valves[J]. High Power Laser and Particle Beams, 2021, 33: 076001. doi: 10.11884/HPLPB202133.210062

严重事故专用卸压阀排放能力需求

doi: 10.11884/HPLPB202133.210062
详细信息
    作者简介:

    武铃珺(1982—),女,高级工程师,现主要从事严重事故及概率安全评价研究工作

    通讯作者:

    邓 坚(1981—),男,博士,高级工程师,现主要从事反应堆热工水力分析及严重事故策略研究工作

  • 中图分类号: TL364

Discharge capacity requirements of severe accident depressurization valves

  • 摘要: 二代加百万千万级核电站严重事故下卸压过程中高温流体流经卸压阀,可能造成流道变形,甚至造成阀杆下落使得排放流道封闭,造成卸压失败。对严重事故专用卸压阀在卸压过程中可能经历的高温流体状态进行谱分析,获得了不同卸压能力下阀门经受的高温流体状态。开展了高温可能引起的阀门流道变形对卸压效果的影响分析。第二类阀门虽然存在阀门流道变形的可能,但能够获得较长严重事故处置时间,从优化严重事故对策的角度,严重事故专用卸压阀推荐采用第二类阀门排放能力450~600 t/h范围。
  • 图  1  稳压器出口温度(第一类排量)

    Figure  1.  Temperature of pressurizer outlet (type 1)

    图  2  稳压器出口温度(第二类排量)

    Figure  2.  Temperature of pressurizer outlet (type 2)

    图  3  稳压器出口温度(第三类排量)

    Figure  3.  Temperature of pressurizer outlet (type 3)

    图  4  稳压器出口温度(第四类排量)

    Figure  4.  Temperature of pressurizeroutlet (type 4)

    图  5  RPV压力

    Figure  5.  RPV pressure

    图  6  稳压器水位

    Figure  6.  Pressurizer water level

    图  7  堆芯出口温度

    Figure  7.  Temperature of core outlet

    图  8  堆芯活性段水位

    Figure  8.  Core active zone water level

    图  9  RPV压力(工况1-1/2/3/4)

    Figure  9.  RPV pressure (case 1-1/2/3/4)

    图  10  RPV压力(工况1-5/6/7/8)

    Figure  10.  RPV pressure (case 1-5/6/7/8)

    图  11  RPV压力(工况2-1/2/3/4)

    Figure  11.  RPV pressure (case 2-1/2/3/4)

    图  12  RPV压力(工况4-1/2/3/4)

    Figure  12.  RPV pressure (case 4-1/2/3/4)

    表  1  事故主要进程时间节点

    Table  1.   Accident process of depressurization

    casetime/spressure/MPa
    open valves: Tout
    (reactor is 50 ℃)
    accumulator
    injection
    pressurizer
    drain
    accumulator
    drain
    Tout of pressurizer
    ≥1000 ℃
    RPV lower
    head failure
    RPV lower
    head failure
    case 1-0: 350 t/h 5750 6515 6575 12825 6625/18605 20925 1.39
    case 2-0: 450 t/h 5750 6350 6550 12600 18145 18800 0.78
    case 3-0: 600 t/h 5750 6200 6750 15425 0.99
    case 4-0: 1000 t/h 5750 6000 12375 6500 12410 14000 0.90
    下载: 导出CSV

    表  2  事故主要进程时间节点(阀门开启初期发生流道变形)

    Table  2.   Accident process of depressurization with valve channel deformation

    valve channel deformation(350 t/h:6625 s)time/spressure/MPa
    accumulator drainRPV lower head failureRPV lower head failure
    case 1-1:25%15565223001.35
    case 1-2:50%15980266502.32
    case 1-3:75%21050317004.14
    case 1-4:90%133007.62
    下载: 导出CSV

    表  3  事故主要进程时间节点(事故后期发生流道变形)

    Table  3.   Accident process of depressurization (with late valve channel deformation)

    valve channel deformationtime /spressure/MPa
    350 t/h:18605case 1-5:25% 19400 1.27
    case 1-6:50% 19410 1.56
    case 1-7:75% 19415 2.04
    case 1-8:90% 19400 2.51
    450 t/h:18145case 2-1:25% 18875 0.91
    case 2-2:50% 18880 1.11
    case 2-3:75% 18865 1.45
    case 2-4:90% 18890 1.93
    1000 t/h 13010case 4-1:25% 14000 1.52
    case 4-2:50% 14075 2.51
    case 4-3:75% 14150 3.82
    case 4-4:90% 14000 4.78
    下载: 导出CSV
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出版历程
  • 收稿日期:  2021-03-01
  • 修回日期:  2020-04-21
  • 网络出版日期:  2021-05-06
  • 刊出日期:  2021-07-15

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