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OPTIMIZATION OF START-UP PROCESSES AT HRSG WITH NATURAL CIRCULATION SYSTEM

机译:利用天然循环系统的HRSG启动过程优化

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The demand for high flexibility within a stable energy supply is nowadays required. Combined cycle power plants (CCPP) gain therefore more and more importance. Due to their rapid response on demand they are capable to compensate power-grid fluctuations. Within this study some parameters for the limits of start-up as well as load change behavior of heat recovery steam generators with natural circulation system will be discussed. In the first step a simulation model is developed which is compared and validated by measurements at different start-up processes of a HRSG. As one result it may be concluded that a relative simply quasi-steady approximation reveals appropriate results. However, still more exact findings are reached by means of a complete transient simulation. In the second step the optimization of the start-up process will be analyzed with aim to minimize this time period. For limitations as well as economic reasons beside the nature of the start-up process and the applied materials, all thick walled components e.g. steam drum and steam headers have to be considered for maximum allowable gradients. For boilers with requirements for short start-up times it can be helpful to conduct additionally a comprehensive FEM calculation. For a deeper detail discussion of some parts of this study it may be referred to [1] and [7]. Based on the analyses it is possible to specify parameters for a dynamic boiler simulation to estimate the start-up thereof. Ideally, one should in practice install a differential temperature measurement in the drum shell and assign the allowable temperature differences to the actual pressure to comply with the limits. In this way, it would be possible to optimally design the start-up process in relation to the start-up time according to actual values.
机译:现在需要在稳定的能源供应内对高灵活性的需求。综合循环发电厂(CCPP)因此越来越重要。由于它们对需求的快速响应,他们能够补偿电网波动。在这方面,将讨论用于初始启动的一些参数以及具有自然循环系统的热回收蒸汽发生器的负载变化行为。在第一步中,开发了模拟模型,其通过HRSG的不同启动过程进行比较和验证。作为一个结果,可以得出结论,相对简单的准稳态近似揭示了适当的结果。然而,通过完全瞬态仿真达到更具精确的发现。在第二步中,将分析启动过程的优化,以便最小化这段时间段。对于初始限制以及初创过程的性质和应用材料的经济原因,所有厚壁组件都是如此。必须考虑蒸汽滚筒和蒸汽头以获得最大允许梯度。对于具有短暂启动次数要求的锅炉,可以有助于进行全面的有限元计算。对于对本研究的某些部分的更深入的详细讨论,它可能被称为[1]和[7]。基于分析,可以指定动态锅炉模拟的参数以估计其启动。理想情况下,应该在实践中安装滚筒壳中的差分温度测量,并将允许的温度差异分配到实际压力以符合限制。以这种方式,可以根据实际值最佳地设计与启动时间相关的启动过程。

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