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哈尔滨工程大学核安全与仿真技术国防重点学科实验室
纸质出版日期:2013-09-01
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[1]法丹,阎昌琪,孙立成,孙露,赵行斌.熔盐堆水冷却非能动余热排出系统换热器稳态特性研究[J].核技术,2013,36(09):71-76.
FA Dan, YAN Changqi, SUN Licheng, et al. Steady-state characteristic study of heat exchanger in water-cooled passive heat removal system for molten salt reactor[J]. Nuclear techniques, 2013, 36(9): 090602
[1]法丹,阎昌琪,孙立成,孙露,赵行斌.熔盐堆水冷却非能动余热排出系统换热器稳态特性研究[J].核技术,2013,36(09):71-76. DOI: 10.11889/j.0253-3219.2013.hjs.36.090602.
FA Dan, YAN Changqi, SUN Licheng, et al. Steady-state characteristic study of heat exchanger in water-cooled passive heat removal system for molten salt reactor[J]. Nuclear techniques, 2013, 36(9): 090602 DOI: 10.11889/j.0253-3219.2013.hjs.36.090602.
在熔盐堆水冷却非能动余热排出系统中
通过自然循环
燃料产生的衰变热可最终由放置在水箱中的换热器导出。在换热器管内发生蒸汽冷凝过程
而管外则先依靠水的自然对流换热
当水温达到饱和后
热量则依靠水的沸腾蒸发被导出。本文通过对换热器进行设计计算
对换热器的稳态换热特性进行研究。根据系统工作过程建立相应数学模型
使用C++语言编程
得到了换热器的传热性能。结果表明
设计的换热器能够满足换热要求
同时具有一定的自调节性。另外得到了换热器压力、水箱内水质量等参数的变化规律。
Background:In the water-cooled passive heat removal system for molten salt reactor
the decay heat generated in molten salt can finally be transferred to the heat exchanger placed in water tank by natural circulation.Purpose:Based on the principles of high safety and simplification
there is a need to transfer the decay heat passively without using external power.Methods:The heat exchanger consists of a set of bundles submerged into the water tank with a tube header at each side.Based on the flow process
corresponding numerical model was constructed in the code of C++.Then the total heat exchange coefficient is got and the heat transfer area is calculated.Continually iterate the heat transfer area until the iteration stopping criterion is met
after that the dimensions of water tank are figured out.Results:While the decay power is 100 kW in the initial of the operation
the power of heat exchanger reaches the maximum value of 130 kW due to the low-temperature water in water tank.Then it drops quickly for the decrease of heat exchanger pressure and the rise of water temperature in water tank.When the heat exchanger pressure begins to rise
the heat exchanger power drops slower than before.The heat transfer ability begins to decrease quickly as the temperature difference between inside and outside of heat exchanger tubes lowers.Then it drops gradually as a result of the slowly changed pressure.During early operation
the heat exchanger pressure decreases because the steam generation rate is lower than the steam condensation rate.Then the condition varies as the heat exchanger power declines gradually.When boiling happens inside the water tank
the steam condensation rate raises due to the increasing heat transfer ability which makes the pressure of heat exchanger drops quickly.Afterwards
the heat exchanger pressure changes very slowly as the steam generation rate is approximate to the steam condensation rate.The mass of water in water tank remains unchanged essentially until the water begins to boil
then it starts to evaporate as the heat is transferred.The variation trend of the mass flow of condensate is similar to the heat exchange power of condenser.It decreases first and rises when the water reaches saturation.Then it lowers as the condenser pressure declines.Conclusions:The parameters of heat exchanger are calculated and the result shows that it can meet the requirements for heat exchange and has the self-regulation to some extent.The water tank can transfer the heat for a long time.Meanwhile the power can be adjusted by changing the water level in water tank.
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