کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
46801 46449 2011 8 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Catalytic hydrothermal gasification of activated sludge
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی کاتالیزور
پیش نمایش صفحه اول مقاله
Catalytic hydrothermal gasification of activated sludge
چکیده انگلیسی

In this paper, Raney nickel is used as catalyst to gasify activated sludge in near-critical water (NCW) at a temperature range of 320–410 °C and a corresponding pressure range of 11.3–28.1 MPa in a batch reactor. At 380 °C and with 15 min reaction time, carbon gasification ratios (CGR) increased with increasing catalyst loading and reached 69% at 1.8 g catalyst/g dry sludge. Methane yield also linearly increased with catalyst loading while hydrogen production exhibited a maximum at about 1.5 g catalyst/g dry sludge. The gaseous product in this case consisted of 46% hydrogen, 25% methane and 29% carbon dioxide with trace amounts of carbon monoxide. The amount of generated gas as well as its composition did not change significantly after 30 min; however, increasing the temperature had a positive effect on the total yield up to 380 °C. The addition of sulfur to activated sludge resulted in a significant reduction of the carbon gasification ratio. CGR dropped by about 25% as the sulfur content of the feed increased from 0.8% to 3.0%. The deactivation of the catalyst due to hydrothermal sintering was also examined. Raney nickel significantly lost its activity upon pre-exposure to near-critical water at 380 °C for 8 min. This loss in activity had a major impact on methane production where methane yield dropped by six folds to a level similar to the catalyst-free gasification reaction and hydrogen yield was decreased by 50%. The decrease in catalytic activity of Raney nickel was likely due to an increase in average nickel crystallite size caused by hydrothermal sintering.

Near-critical water gasification of municipal activated sludge at 380 °C.Figure optionsDownload as PowerPoint slideHighlights
► Raney nickel exhibited good activity to gasify municipal activated sludge in near-critical water.
► At 380 °C and with 1.8 g catalyst/g dry sludge, carbon and hydrogen gasification ratios were 69% and 113%; respectively, after 15 min reaction time.
► Raney nickel lost half of its activity after 8 min exposure to NCW at 380 °C.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Applied Catalysis B: Environmental - Volume 105, Issues 1–2, 9 June 2011, Pages 136–143
نویسندگان
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