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Studies on Heat Exchangers using Miscible System

机译:利用混溶系统的换热器研究

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An experimental investigation on comparative heat transfer study on a solvent and solution were made using Cross flow and Shell and Tube Heat Exchangers. Steam is the hot fluid, whereas Wafer and Acetic acid-Water miscible solution serves as cold fluid, A series of runs were made between steam and water, steam and Acetic acid solution. In addition to, the volume fraction of Acetic acid was varied and the experiment was held. The flow rate of the cold fluid is maintained from 30 lph to 300 lph for Cross flow Heat Exchanger, for Shell and Tube Heat Exchanger maintained from 120 lph to 720 lph, and the volume fraction of Acetic acid is varied from 10%-50%. Experimental results such as exchanger effectiveness, overall heat transfer coefficients were compared for both the flow systems of Cross flow and Shell and Tube Heat Exchangers. A steady state model for the outlet temperature of both the cold and hot fluid and overall heat transfer coefficient of a plate-fin cross flow heat exchanger for Acetic acid solution- steam system at various compositions of Acetic acid is developed and simulated using MATLAB, which was verified with the experiments conducted. A mathematical model was developed for the outlet temperatures of both the Shell and Tube side fluids, and was simulated using MATLAB program. The model was compared with the experimental findings and found to be valid.
机译:使用横流式换热器和壳管式换热器进行了溶剂和溶液的传热比较研究。蒸汽是热流体,而硅片和醋酸与水的可混溶溶液用作冷流体,在蒸汽和水,蒸汽和乙酸溶液之间进行了一系列运行。另外,改变乙酸的体积分数并进行实验。对于错流式热交换器,冷流体的流量保持在30 lph至300 lph;对于管壳式热交换器,冷流体的流量保持在120 lph至720 lph,乙酸的体积分数在10%-50%之间变化。 。比较了横流和壳管式换热器的流动系统的实验结果,例如交换器效率,总传热系数。利用MATLAB建立并模拟了乙酸溶液-蒸汽系统在乙酸的各种组成下冷热流体出口温度以及板翅式错流热交换器总传热系数的稳态模型。已通过实验验证。针对壳和管侧流体的出口温度建立了数学模型,并使用MATLAB程序进行了仿真。将模型与实验结果进行比较,发现是有效的。

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