Cogeneration Plant : Optimization of Heat Recovery Steam Generator (HRSG)

Filian Arbiyani, Stefanus Randy Raharja, Wegie Ruslan
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Abstract

This research discusses the optimization of cogeneration plant at PT. Dian Swastatika Sentosa while the CFBs are eliminated in the steam production process, thus the steam is only produced by HRSG A, and HRSG B. The research has been conducted experimentally by adjusting the steam mass flow rate of 51% for HRSG A and 49% for HRSG B according to the scenario 2 and condition which have been determined in the pre experiment calculation. During the experiment, the total mass flow rate supplied for paper mill is 10.776 kg/s, which consists of 5.482 kg/s from HRSG A and 5.294 kg/s from HRSG B. The optimization results in the nett power of 3344.63 kW for PLTG A and 3328.33 kW for PLTG B, the required heat of combustion chamber are 13990.76 kW for PLTG A and 13466.462 kW for PLTG B, and the waste heat from the gas turbine are 10646.086 kW from PLTG A and 10138.132 kW from PLTG B.
热电厂:热回收蒸汽发生器(HRSG)的优化
本研究探讨了圣淘沙PT. Dian Swastatika Sentosa热电联产厂在蒸汽生产过程中取消循环流化床锅炉,只由HRSG A和HRSG B产生蒸汽的优化问题。根据实验前计算确定的情景2和条件,将HRSG A和HRSG B的蒸汽质量流量分别调整为51%和49%,进行了实验研究。在实验期间,造纸厂的总质量流量提供10.776公斤/ s,由5.482公斤/ s从余热锅炉余热锅炉和5.294公斤/ s B .优化结果的净功率为3344.63千瓦PLTG PLTG B和3328.33千瓦,所需的燃烧室热13990.76 kW PLTG PLTG B和13466.462千瓦,和废热从燃气轮机是10646.086千瓦PLTG PLTG B和10138.132千瓦。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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