催化作用
镍
化学计量学
选择性
甲烷
无机化学
硫黄
铜
程序升温还原
化学
摩尔比
二氧化硫
材料科学
有机化学
作者
Seyyed Ebrahim Mousavi,Hassan Pahlavanzadeh,Masoud Khani,H. Ale Ebrahim,Abbas Mozaffari
出处
期刊:Iranian Journal of Chemical Engineering(IJChE)
日期:2018-09-01
卷期号:15 (3): 94-107
被引量:4
摘要
The catalytic reduction of sulfur dioxide with methane to form elemental sulfur has been studied. Al2O3, Cu-Al2O3 and Ni-Al2O3 were examined as catalysts and their performances were compared in terms of SO2 conversion and selectivity. Performance of the catalyst extremely enhanced when nickel and copper were added as promoters. The effects of temperature, SO2/CH4 molar ratio, and reaction time on SO2 reduction were studied. The operating temperature range was 550–800 °C and it was observed that the reaction is strongly temperature dependent. At temperatures lower than 700 °C, Al2O3-Cu (10%) catalyst showed the best performance of all the catalysts. But, at 700° and higher, performances of Al2O3-Cu (10%) and Al2O3-Ni(10%) catalysts were similar. Complete conversion and selectivity (more than 99.5%) was achieved by Al2O3-Cu (10%) and Al2O3-Ni(10%) catalyst, at 750 °C. Effect of molar feed ratio of SO2/CH4= 1-3 was studied and stoichiometric feed ratio showed the best performance. Also, investigation of reaction time for Al2O3-Cu(10%) and Al2O3-Ni(10%) catalysts showed a good long-term stability for SO2 reduction with methane.
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