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Thermodynamic analysis of hydrogen production from raw coke oven gas via steam reforming

机译:蒸汽重整制焦炉煤气制氢的热力学分析

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The steam reforming processes of raw coke oven gas (RCOG) for hydrogen production without and with CO2 adsorption were studied via the thermodynamic analysis. Ordinary pressure (1 bar) was found as the best reaction pressure for RCOG steam reforming. The hydrogen yield increased with the increases in temperature and S/RCOG ratio and then flatted out around 160 mol per 100 mol RCOG at the temperature above 700 degrees C and S/RCOG ratio above 0.8, yet with hydrogen concentration of just about 70 %. After the addition of CaO as CO2 sorbent, the hydrogen yields increased on the whole as the CaO/C ratio and S/RCOG ratio rose, and the temperature range with the hydrogen yield around 160 mol and even higher was widened and moved to low temperature. The optimal conditions of sorption-enhanced RCOG steam reforming for hydrogen production were S/RCOG ratio above 0.8, CaO/C ratio above 2.0 and the temperature from 550 to 700 degrees C, with the hydrogen yield and concentration reaching around 160 mol and over 90 %, respectively.
机译:通过热力学分析研究了不带CO 2和带CO 2吸附的生焦炉煤气(RCOG)的蒸汽重整过程。发现普通压力(1巴)是RCOG蒸汽重整的最佳反应压力。氢气产率随温度和S / RCOG比的增加而增加,然后在高于700摄氏度的温度和S / RCOG比高于0.8的情况下在每100 mol RCOG中约160 mol趋于平坦,而氢气浓度仅为约70%。加入CaO作为CO2吸附剂后,随着CaO / C比和S / RCOG比的增加,氢的产率总体上增加,并且氢产率在160 mol左右甚至更高的温度范围扩大并移至低温。用于产氢的吸附增强型RCOG蒸汽重整的最佳条件是S / RCOG比大于0.8,CaO / C比大于2.0和温度在550至700摄氏度之间,氢的收率和浓度达到160 mol左右且超过90 %, 分别。

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