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DEVELOPMENT OF HIGH-TEMPERATURE HEAT EXCHANGER FOR HYDROGEN COMBUSTION TURBINE SYSTEM

机译:氢气燃烧汽轮机系统高温换热器的研制

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New Rankine Cycle and Topping Regenerative Cycle shown in Fig. A-1 and Fig. A-2 are representative 500 MW power generation systems for a hydrogen combustion turbine (HCT). The energy efficiency based on HHV of these is expected to be over 60% because the inlet temperature of turbine can be increased to 1970 K. These systems comprise various heat exchangers. Especially, the development of high temperature heat exchanger dealing with the high temperature and pressure steam is very important to realize the hydrogen combustion turbine system. The high-temperature heat exchanger of New Rankine Cycle is a supercritical heat recovery steam generator operating at pressure of 36 MPa. This heat exchanger is heated by steam at temperature of 1390 K. On the other hand, Topping Regenerative Cycle has two high-temperature heat exchangers. One is a regenerator operating at pressure of 37 MPa. The other is a regenerator operating at pressure of 5 MPa. Both regenerators are heated by steam at temperature of 1030 K. The followings are the principal development subject of high-temperature heat exchanger. 1) Improving the heat transfer characteristics to achieve the compact heat exchanger. 2) Planning the heat exchanger structure suitable for the high thermal stress. To improve a heat transfer characteristic of the high-temperature heat exchangers, a parameter survey is conducted to optimize a tube arrangement and a fin configuration on tube outside and/or inside. The heat transfer areas are minimized through using the tubes with an extended heat transfer surface on the both sides of a tube. Structural integrity is also estimated by conducting a structural analysis for the critical parts of the high-temperature heat exchangers.
机译:图2中所示的新朗肯循环和顶部再生循环。A-1和图1。A-2是用于氢气燃烧涡轮机(HCT)的代表500 MW发电系统。基于HHV的能量效率预计超过60%,因为涡轮机的入口温度可以增加到1970k。这些系统包括各种热交换器。特别是,处理高温和压力蒸汽的高温热交换器的发展非常重要,实现氢燃烧涡轮机系统。新的朗肯循环的高温热交换器是一个超临界热回收蒸汽发生器,在36MPa的压力下工作。该热交换器在1390k的温度下通过蒸汽加热。另一方面,顶部再生循环具有两个高温热交换器。一个是在37MPa的压力下操作的再生器。另一个是在5MPa的压力下操作的再生器。两个再生器在1030K的温度下通过蒸汽加热。以下是高温换热器的主要开发主体。 1)改善传热特性以实现紧凑型热交换器。 2)规划适用于高热应力的热交换器结构。为了改善高温热交换器的传热特性,进行参数测量以优化管装置和管道外部和/或内部的翅片配置。通过在管的两侧上使用具有延伸的传热表面的管子,传热区域最小化。还通过对高温热交换器的关键部件进行结构分析,估计结构完整性。

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