کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
148381 456411 2013 7 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Simultaneous catalytic hydrolysis of low concentration of carbonyl sulfide and carbon disulfide by impregnated microwave activated carbon at low temperatures
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Simultaneous catalytic hydrolysis of low concentration of carbonyl sulfide and carbon disulfide by impregnated microwave activated carbon at low temperatures
چکیده انگلیسی


• Simultaneous catalytic hydrolysis activity of COS and CS2 over Fe–Cu–Ni/MCSAC was notable.
• Low generation of K3Na(SO4)2 was in the Fe–Cu–Ni/MCSAC catalyst.
• High specific surface areas and more micropores enhanced catalytic hydrolysis activity.
• XPS results showed that most of COS and CS2 hydrolysis products were S/SO42-.

The blank microwave coal-based activated carbons (MCAC) and blank microwave coconut shell activated carbons (MCSAC) were tested for simultaneous catalytic hydrolysis of carbonyl sulfide (COS) and carbon disulfide (CS2) at relatively low temperature (at 50 °C). MCAC and MCSAC loaded by Fe–Cu–Ni metal mixed oxides were prepared by sol–gel method, and also tested for the simultaneous catalytic hydrolysis process. The results showed that Fe–Cu–Ni/MCSAC catalyst had the superior activity for the simultaneous catalytic hydrolysis of COS and CS2. These modified catalysts were characterized by XRD, BET, EDS and XPS, the results of which can help us to understand the reasons of the superior catalytic activity and the reasons of catalyst deactivation. Lower generation of sulfate (K3Na(SO4)2), high specific surface areas and more pore sizes of 0.3–1.2 nm and 3.5–4.0 nm may be the important role in COS and CS2 catalytic hydrolysis reaction. The XPS results showed that most of products on the exhausted catalysts were S/SO42- species which accumulated on the active carbon’s surface and had a negative effect on the hydrolysis activity, and the contents of S/SO42- species of exhausted Fe–Cu–Ni/MCAC were higher than which of exhausted Fe–Cu–Ni/MCSAC catalysts.

For sample Fe–Cu–Ni/MCAC, 100% COS conversion and 100% CS2 conversion are observed for about 330 min and 360 min respectively, and for sample Fe–Cu–Ni/MCSAC, 100% COS conversion and 100% CS2 conversion are observed for about 540 min and 600 min respectively.Figure optionsDownload as PowerPoint slide

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Journal - Volume 230, 15 August 2013, Pages 220–226
نویسندگان
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