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Effect of a diffuser on performance enhancement of a cylindrical methanol steam reformer by computational fluid dynamic analysis

机译:计算流体动力学分析扩散器对圆柱形甲醇蒸汽重整器性能提升的影响

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Proton exchange membrane fuel cells (PEMFC) connected with a methanol steam reformer designed to enhance its performance is considered as a promising future power source. Enhancing the performance of a cylindrical methanol steam reformer due to diffuser effects was then investigated applying three-dimensional computational fluid dynamics by the SIMPLE-C algorithm and an Arrhenius form of reaction model. The effect of the angle and length of the diffuser, and wall temperature have been explored on heat and fluid flow, methanol conversion, hydrogen production, carbon monoxide reduction, as well as estimated net power of fuel cell with the same catalyst volume and entrance condition in a cylindrical methanol steam reformer. The results indicate that the diffuser obviously enhances methanol conversion and hydrogen production of a cylindrical methanol steam reformer. In comparison with a traditional reformer, the reformer with a diffuser of theta(d) = degrees 6 and L-d = 75 mm obtains the maximum enhancement of 22.96% in methanol conversion, 44.62% in hydrogen production, and 24.59% in estimated net power of fuel cell at wall temperature of 250 degrees C. In addition, the novel reformer with a diffuser of theta(d) = degrees 9 and L-d = 100 mm generates the maximum reduction of 44.17% in CO production at T-w = 250 degrees C.
机译:质子交换膜燃料电池(PEMFC)与设计用于增强其性能的甲醇蒸汽重整器相连,被认为是有前途的未来动力源。然后,利用SIMPLE-C算法和Arrhenius形式的反应模型,利用三维计算流体动力学,研究了因扩散效应而引起的圆柱形甲醇蒸汽重整器性能的提高。研究了扩散器的角度和长度以及壁温对热和流体流量,甲醇转化率,产氢量,一氧化碳还原量以及在相同催化剂体积和入口条件下估计的燃料电池净功率的影响在圆柱形甲醇蒸汽重整器中结果表明,该扩散器明显提高了圆柱形甲醇蒸汽重整器的甲醇转化率和产氢量。与传统的重整器相比,扩散器为theta(d)= 6度且Ld = 75 mm的重整器在甲醇转化率,氢气生产中的最大转化率和氢气的估计净功率方面最大提高了22.96%,氢气产量为44.62%,最大为24.59%。壁温度为250℃的燃料电池。此外,新型重整器的扩散器为theta(d)= 9,Ld = 100 mm,在Tw = 250℃时,CO产生的最大减少量为44.17%。

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