Weight and size characteristics of heat exchange equipment of hybrid Flash/ORC power plants: case of application in WHR cogeneration plants

Andriy Redko, Serhii Pavlovskyi, Oleksandr Redko, Adam Ujma, Vadym Zadiranov
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Abstract

Calculations of the characteristics concerning the heat exchange equipment of the Flash/ORC power plant for the usage in waste heat recovery (WHR) cogeneration plants are presented. The use of hybrid power plants with water steam and organic working fluids, on the one hand, leads to an increase in the mass of the heat exchange equipment, and on the other hand, it ensures the generation of electrical energy and heat at high temperatures of the heat source, when the use of high-temperature working fluids is limited their thermal stability (for example, the thermal stability of silaxanes is about 300 ºC). Calculations are performed for a heat source with temperatures of 250ºC and 350 ºC. The generated electrical power of the power plant at a heat source temperature of 350ºC is 460 kW. The generated thermal power by capacitors is 1755.3 kW. The mass of the capacitors of the second and third circuits is 5000 kg and 14500 kg, respectively. It is shown that when the temperature of the heat source decreases to 250ºC with a double-circuit design, the mass of the heat exchange equipment decreases. Thus, the mass of the condenser is 12700 kg, and the generated thermal power is 1430.2 kW. The values of the heat exchange surface area of a direct-flow steam generator with flue gases, and an intermediate steam generator between the stages of the thermal circuit of a regenerative heat exchanger, as well as a water-cooled condenser are given. When the condenser is cooled by atmospheric air, the surface area of the condenser increases significantly. A characteristic feature of organic working fluids is the low efficiency of heat exchange in heat exchangers, especially at low temperatures. The heat transfer coefficient in heat exchangers with organic working fluids is about 1500-2800 W/(m2•K), which causes an increase in the heat exchange surface area. In this case, it is necessary to reduce the diameters of pipes in the heat exchangers of the steam generator, to use the pipes with internal ribs, and coil pipes in order to reduce the pipe length. The use of steam generators with coil steam-generating channels, characterized by a higher heat exchange intensity, is promising. The selection of the optimal structure and parameters of the ORC installation is carried out taking into account the mutual influence of steam turbine units on the efficiency of working processes in general.
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闪蒸/ORC 混合发电厂热交换设备的重量和尺寸特征:WHR 热电联产厂的应用案例
本文介绍了闪蒸/ORC 发电厂热交换设备在废热回收(WHR)热电联产设备中使用的相关特性计算。使用水蒸汽和有机工作流体的混合动力设备一方面会导致热交换设备的质量增加,另一方面,当使用高温工作流体的热稳定性受到限制时(例如,硅烷的热稳定性约为 300 ºC),它能确保在热源的高温下产生电能和热量。对温度为 250 ºC 和 350 ºC 的热源进行了计算。热源温度为 350ºC 时,发电厂的发电功率为 460 千瓦。电容器产生的热功率为 1755.3 千瓦。第二和第三回路电容器的质量分别为 5000 千克和 14500 千克。双回路设计表明,当热源温度降低到 250 摄氏度时,热交换设备的质量会减少。因此,冷凝器的质量为 12700 千克,产生的热功率为 1430.2 千瓦。文中给出了烟气直流蒸汽发生器、蓄热式热交换器热回路各级之间的中间蒸汽发生器以及水冷式冷凝器的热交换表面积值。当冷凝器由大气空气冷却时,冷凝器的表面积会显著增加。有机工作流体的一个特点是热交换器的热交换效率较低,尤其是在低温条件下。使用有机工作流体的热交换器的传热系数约为 1500-2800 W/(m2-K),这导致热交换表面积增大。在这种情况下,有必要减小蒸汽发生器热交换器的管道直径,使用带内肋的管道和盘管,以减少管道长度。使用具有较高热交换强度的盘管蒸汽发生器很有前途。在选择 ORC 设备的最佳结构和参数时,要考虑到蒸汽轮机组对整个工作流程效率的相互影响。
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