环路 FASSIP 03 NT 加热罐段热交换器性能调查

D. Haryanto, A. Budiman, Muhammad Ganjar Putra, Putut Hery Setiawan, M. Juarsa
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摘要

被动系统模拟设施(FASSIP)环路是被动冷却系统的实验测试设施,用于回收反应堆堆芯在事故情况下产生的衰变余热。加热罐部分(HTS)是 FASSIP 03 NT 设施的组成部分之一。该部件配备有热交换器,有三种类型的热交换器可用于 HTS。即直管热交换器(SPHE)型、直管鳍片热交换器(SPFHE)型和螺旋管热交换器(HPHE)型。为了提高 HTS 的效率,对 HTS 进行了改装,即把 HTS 上的电加热器从陶瓷带加热器改为浸入式加热器。在进行这种改装后,有必要了解 HTS 上热交换器的性能及其达到工作温度的速度。HPHE 型热交换器的效率高于 SPHE 型和 SPFHE 型热交换器。HPHE 型热交换器的长度更大,达到 5.5 米,因此热阻(Rth)非常小,仅为 0.003926 ℃/W。要使工作流体温度达到 50 - 90 ℃,HPHE 型热交换器需要 35 - 86 分钟。
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Investigation of Heat Exchanger Performance in The Heating Tank Section of Loop FASSIP 03 NT
The Passive System Simulation Facility (FASSIP) loop is an experimental test facility for a passive cooling system to recover the residual heat from decay produced by the reactor core during accident conditions. The Heating Tank Section (HTS) is one of the components of the FASSIP 03 NT facility. This component is equipped with a heat exchanger, 3 types of heat exchangers can be applied to HTS. Namely heat exchangers of the Straight Pipe Heat Exchanger (SPHE) type, the Straight Pipe Fins Heat Exchanger (SPFHE) type, and the Helical Pipe Heat Exchanger (HPHE) type. A modification was made to increase the efficiency of HTS, namely replacing the electric heater on the HTS from a ceramic band heater type to an immersion heater type. With this modification, it is necessary to know the performance of the heat exchanger on HTS and its speed in reaching operational temperature. The HPHE-type heat exchanger is more efficient than the SPHE-type and SPFHE-type heat exchangers. The HPHE-type heat exchanger has a much larger length of 5.5 m, so the thermal resistance (Rth) is very small, namely 0.003926 ℃/W. To reach the working fluid temperature in the range of 50 – 90 ℃, the HPHE-type heat exchanger requires 35 – 86 minutes.
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