کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
155724 456909 2012 10 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Electrostatic characteristics in a large-scale triple-bed circulating fluidized bed system for coal gasification
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Electrostatic characteristics in a large-scale triple-bed circulating fluidized bed system for coal gasification
چکیده انگلیسی

Electrostatics charge generation by triboelectrification has significant implications for the proper design and operation of a circulating fluidized bed. In this study, electrostatics in the fully developed regions of both the riser and downer of a large-scale triple-bed combined circulating fluidized bed was characterized in terms of the equivalent currents over the cross section of the developed region. The average equivalent currents and solids holdup were measured under different superficial velocities in the riser, downer and gas-sealing bed. It was found that in the fast fluidization regime in the riser, the negative equivalent currents were comparable with the positive equivalent currents due to the typical core-annulus flow pattern. With increasing superficial velocities in the riser or in the gas-sealing bed, the flow pattern would approach dilute phase transport or dense suspension upflow regime. Thus, the positive equivalent currents became dominant because the backflow of sand particles were greatly suppressed. Some dominant frequencies for the equivalent currents in the riser were almost identical regardless of the magnitude of superficial velocities in the riser and the gas-sealing bed, indicating that they were determined by the inherent characteristics of electrostatics and/or signal noise, and were not affected by gas–solids flow behaviors. The frequencies in the downer were focused on the low value range, and the dominant frequencies were nearly zero. Both the solids mass flux and solids holdup had significant influence on the average equivalent currents. With increasing superficial velocities in the gas-sealing bed, the average equivalent currents first increased and then approached a constant. This led to the same trend in variation of solids mass flux, as well as solids holdup. With increasing air superficial velocities in the riser, the average equivalent currents in the riser increased, while the average equivalent currents decreased in the downer with increasing air superficial velocities in the downer.

Graphical AbstractElectrostatics in Triple-bed Combined Circulating Fluidized Bed.Figure optionsDownload high-quality image (48 K)Download as PowerPoint slideHighlights
► Experimental studies were conducted to investigate electrostatics.
► Different flow patterns led to different electrostatics characteristics.
► Average currents varied in the same trend with solids mass flux and holdup.
► Dominant frequency for equivalent currents kept almost constant in the riser.
► Equivalent currents in downer were characterized by low frequency fluctuations.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Science - Volume 75, 18 June 2012, Pages 435–444
نویسندگان
, , , , , , ,