柴油机余热回收甲醇重整制氢系统的设计与性能优化

H. Jia, Yuanchi Tan, Zhiling Chen, Yi Jian, Bifeng Yin
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引用次数: 0

摘要

为柴油发动机设计了壳管式甲醇蒸汽转化器(MSR)系统。研究了甲醇转化器中螺旋挡板的结构和运行参数对传热和制氢性能的影响。此外,还采用响应面方法进行了多目标优化,研究了间距和厚度以及液体时空速度和蒸汽-甲醇比对甲醇转化率、氢气浓度和氢气产量的交互影响。结果表明,减小挡板间距和增加挡板厚度可进一步提高传热效率。最佳条件是间距为 30 毫米,厚度为 2 毫米,甲醇转化率为 64.2%。将蒸汽-甲醇比率从 0.5 提高到 2,甲醇转化率从 50.6% 提高到 79.7%,氢气浓度随之下降。将液体时空速度从 635 h-1 提高到 1905 h-1,甲醇转化率从 94.5 % 显著降低到 64.2 %,但氢气产量从 0.111 mol/s 提高到 0.228 mol/s。优化结果表明,液体时空速度和蒸汽-甲醇比对甲醇转化炉的制氢效率影响更大。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Design and performance optimization of diesel engine waste heat recovery methanol reforming hydrogen generation system
A shell-and-tube Methanol Steam Reformer (MSR) system was designed for diesel engines. The effects of structural and operational parameters of the spiral baffles in the methanol reformer on heat transfer and hydrogen production performance were investigated. Additionally, a multi-objective optimization using response surface methodology was conducted to study the interactive effects of spacing and thickness, as well as liquid hourly space velocity and steam–methanol ratio, on the methanol conversion rate, hydrogen concentration and hydrogen production. The results indicated that reducing the baffle spacing and increasing the baffle thickness further improved heat transfer efficiency. Optimal conditions were achieved at a spacing of 30 mm and a thickness of 2 mm, resulting in a methanol conversion rate of 64.2 %. Increasing the steam–methanol ratio from 0.5 to 2 increased the methanol conversion rate from 50.6 % to 79.7 %, with a subsequent decrease in hydrogen concentration. Increasing the liquid hourly space velocity from 635 h−1 to 1905 h−1 significantly reduced the methanol conversion rate from 94.5 % to 64.2 %, but the hydrogen production increased from 0.111 mol/s to 0.228 mol/s. Optimization results indicate that the liquid hourly space velocity and steam–methanol ratio have a greater influence on the hydrogen production efficiency of the methanol reformer.
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