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Using turbine thermal kit data to benchmark condenser performance calculations

机译:使用涡轮热套件数据来基准电容性能计算

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In the past, the performance of a condenser has been judged by empirical criteria such as cleanliness factor, terminal temperature difference and/or cooling water pressure drop. However, these criteria vary with load, cooling water inlettemperature and cooling water flow rate. Thus, to base maintenance or operating decisions on deviations in the empirical criteria requires that these other factors be taken into account.One way to avoid this is to develop a benchmark or reference condenser duty. A source for this reference can be found in the analysis of turbine thermal kit data to create a design model of the turbine LP stage. Provided that the turbogenerator isoperating with the equipment configuration on which the thermal kit data was based; and that the boiler operating conditions are close to design for a given load; then the exhaust enthalpy and flow entering the condenser can be calculated as a function of load and back pressure, and these used to estimate present condenser duty. Thus, the performance of a condenser can be compared against a calibrated and stable frame of reference, which changes only very slowly over time.The method allows cooling water flow rates to be estimated and compared; while tube fouling factors and condenser ambient heat discharges can also be quantified. Further, the excess heat discharges due to the fouling of the condenser and its effect on the turbogenerator are initially calculated in MBTU/h. However, they can also be converted to the equivalent economic loss in s/h; as well as the equivalent lbs. of excess CO{sub}2 emissions per hour.
机译:过去,通过诸如清洁因子,末端温差和/或冷却水压降等经验标准来判断冷凝器的性能。然而,这些标准随着负载,冷却水的温度和冷却水流量而变化。因此,基于实证标准中的偏差的基础维护或操作决策要求将这些其他因素考虑在内。避免这一点是开发基准或参考冷凝器义务。可以在涡轮机热套件数据的分析中找到该参考的源,以创建涡轮机LP阶段的设计模型。如果涡轮机驱动器与热套件数据所基于的设备配置等待;并且锅炉操作条件靠近设计给定负荷;然后,进入冷凝器的排气焓和流量可以作为负载和背部压力的函数来计算,并且这些用于估计呈现的冷凝器占空比。因此,可以将冷凝器的性能与校准和稳定的参考框架进行比较,这仅随时间变化非常缓慢。方法允许估计和比较冷却水流速;虽然管污垢因子和冷凝器环境热量放电也可以量化。此外,由于冷凝器的污垢和其对湍流器的效果引起的过热排出最初在MBTU / H中计算。但是,它们也可以转换为S / H的等同经济损失;以及等同的磅。多余的CO {SUB}每小时2个排放量。

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