کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
6467831 1423262 2017 13 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Characterising gas behaviour during gas-liquid co-current up-flow in packed beds using magnetic resonance imaging
ترجمه فارسی عنوان
ویژگی رفتار گاز در جریان جریان گاز-مایع در جریان بسته بندی شده با استفاده از تصویربرداری رزونانس مغناطیسی
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
چکیده انگلیسی


- Liquid and gas hold-up are measured during co-current gas-liquid up-flow in packed beds.
- Dynamic and static contributions to gas hold-up are identified.
- Bubble size and rise velocities determined as a function of gas and liquid flow rate and packing size.

Magnetic resonance (MR) imaging techniques have been used to study gas phase dynamics during co-current up-flow in a column of inner diameter 43 mm, packed with spherical non-porous elements of diameters of 1.8, 3 and 5 mm. MR measurements of gas hold-up, bubble-size distribution, and bubble-rise velocities were made as a function of flow rate and packing size. Gas and liquid flow rates were studied in the range of 20-250 cm3 s−1 and 0-200 cm3 min−1, respectively. The gas hold-up within the beds was found to increase with gas flow rate, while decreasing with increasing packing size and to a lesser extent with increasing liquid flow rate. The gas hold-up can be separated into a dynamic gas hold-up, only weakly dependent on packing size and associated with bubbles rising up the bed, and a 'static' hold-up which refers to locations within the bed associated with temporally-invariant gas hold-up, over the measurement times of 512 s, associated either with gas trapped within the void structure of the bed or with gas channels within the bed. This 'static' gas hold-up is strongly dependent on packing size, showing an increase with decreasing packing size. The dynamic gas hold-up is comprised of small bubbles - of order of the packing size - which have rise velocities of 10-40 mm s−1 and which move between the packing elements within the bed, along with much larger bubbles, or agglomerates of bubbles, which move with higher rise velocities (100-300 mm s−1). These 'larger' bubbles, which may exist as streams of smaller bubbles or 'amoeboid' bubbles, behave as a single large bubble in terms of the observed high rise velocity. Elongation of the bubbles in the direction of flow was observed for all packings.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Science - Volume 157, 10 January 2017, Pages 2-14
نویسندگان
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