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首页> 外文期刊>International Journal of Mechanical Engineering and Applications >A Study on Energy Optimization of Heat Exchangers in a Gasification System
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A Study on Energy Optimization of Heat Exchangers in a Gasification System

机译:气化系统中换热器的能量优化研究

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The objective of this research is the optimization of energy parameters such as the temperature and flow rate of the fluid in heat exchangers in the gasification system in order to increase the recovery rate of energy in the system. A mathematical model of these heat exchangers is developed to predict their operating performance under the specified gasification system. The optimal flow rate and temperature of the fluid in the heat exchanger based on the effectiveness - number of transfer units(NTU) method is investigated. The result of the simulation shows that the optimal mass flow rate and temperature of the high pressure (HP) boiler feed water are determined at 175,907 kg/h and 110℃, respectively, while the optimal mass flow rate and temperature of high pressure saturated steam of boiler are determined at 238,430 kg/h, 290.5℃, respectively. At these values, the total heat amount obtained at these heat exchangers is highest with 169 MW. Besides, the total heat amount obtained at heat exchangers could be increased by 4.61% (7.8 MW) when sixty percent of the heat release amount from air cooler (12.78 MW) is used.
机译:这项研究的目的是优化能量参数,例如气化系统中热交换器中流体的温度和流量,以提高系统中能量的回收率。开发了这些热交换器的数学模型,以预测其在指定气化系统下的运行性能。研究了基于效率-传递单元数(NTU)方法的热交换器中流体的最佳流速和温度。仿真结果表明,高压锅炉给水的最佳质量流量和温度分别确定为175907 kg / h和110℃,而高压饱和蒸汽的最佳质量流量和温度分别确定为锅炉的最高温度分别为238,430 kg / h和290.5℃。在这些值下,在这些热交换器处获得的总热量最高,为169 MW。此外,如果使用空气冷却器(12.78 MW)释放的热量的百分之六十,则在热交换器处获得的总热量可以增加4.61%(7.8 MW)。

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