2,'/> Mechanical design and flow simulation of a steam generator for parabolic trough solar thermal energy harnessing plant
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Mechanical design and flow simulation of a steam generator for parabolic trough solar thermal energy harnessing plant

机译:抛物线槽式太阳能热利用设备蒸汽发生器的机械设计及流场模拟

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A steam generator is designed for a parabolic trough solar thermal plant of aperture area 22.3 m2, which uses Mobil Therm-605 as the heat transfer fluid (HTF). The potential energy input rate from the plant to the steam generator is 4.56 kW, and the flow rate and temperature of the HTF of the plant are 11 min-1and 268 °C respectively. The steam generator was designed as a shell and tube heat exchanger and the tubes are arranged in reflection symmetric configuration (n=6). Flow simulations was done by using SolidWorks CAD software, based on Finite Element Method were carried out for the steam generator design in order to find the optimum conditions by varying the parameters such as tube diameter, HTF flow velocity distribution and thickness of HTF thermal barrier, while minimizing the fluid pressure and maintaining even flow distribution through the tubes. The simulation scheme narrowed down to simulate for the commercially available sizes of food-grade stainless steel tube diameters of 1/8, 1/4, 3/8, 1/2 and 3/4 inch. Simulations reveal that the non-moving HTF layer (which acts as a thermal barrier) for the above tube diameters were 0.0 %, 0.0 %, 4.1 %, 10.7 % and 27.6% respectively. Adding cost factors to the simulation outputs, it was found that the minimum material cost of tube bundle can be achieved when the tubes of diameter 1/4 inch is used and the expected length of the tubes with that diameter is found to be 72 mm.
机译:蒸汽发生器是为孔径面积为22.3 m的抛物槽式太阳能热电厂设计的 2 ,它使用Mobil Therm-605作为传热流体(HTF)。从设备到蒸汽发生器的势能输入速率为4.56 kW,并且该设备的HTF的流量和温度为11分钟 -1 和268°C。蒸汽发生器设计为壳管式热交换器,并且管以反射对称配置(n = 6)布置。使用SolidWorks CAD软件进行了流动模拟,并基于有限元方法对蒸汽发生器进行了设计,以便通过改变诸如管径,HTF流速分布和HTF热障厚度等参数来找到最佳条件。同时将流体压力降至最低,并保持流经管道的流量均匀。模拟方案的范围缩小了,以模拟市售尺寸的食品级不锈钢管的直径,分别为1 / 8、1 / 4、3 / 8、1 / 2和3/4英寸。模拟显示,上述管直径的不可移动HTF层(用作隔热层)分别为0.0 \%,0.0 \%,4.1 \%,10.7 \%和27.6 \%。将成本因素添加到模拟输出中,发现当使用直径1/4英寸的管且发现该直径的管的预期长度为72毫米时,可以实现管束的最低材料成本。

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