Characterization of flow regime transition in trickle bed reactor accounted by gas phase permeability
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Characterization of flow regime transition in trickle bed reactor accounted by gas phase permeability
CIESC JournalIssue 7, Pages: 1770-1776(2010)
作者机构:
华东理工大学化学工程联合国家重点实验室
作者简介:
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DOI:
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Online First:05 July 2010,
Published:05 July 2010
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CHENG Zhenmin, KONG Xiangming, CAO Xin, et al. Characterization of flow regime transition in trickle bed reactor accounted by gas phase permeability[J]. CIESC Journal, 2010, (7): 1770-1776.
DOI:
CHENG Zhenmin, KONG Xiangming, CAO Xin, et al. Characterization of flow regime transition in trickle bed reactor accounted by gas phase permeability[J]. CIESC Journal, 2010, (7): 1770-1776.DOI:
Characterization of flow regime transition in trickle bed reactor accounted by gas phase permeability
Since the Ergun equation is applicable for calculation of gas-liquid pressure drop in the cases without interphase interaction
and the pressure drop ratio of single gas phase to gas-liquid concurrent flow can be accounted for as the relative permeability of the gas phase
the Ergun equation is proposed to characterize the flow regime transition based on the gas-liquid interaction in a trickle bed. To check the validity of this methodology
experimental work was conducted in a plexiglass column of 140 mm ID packed with glass beads of different diameters (1.9
3.6
5.2 and 9.3 mm) by applying air and water as the working media. The transient data under pulsing flow were obtained by applying pressure transducers and electrical capacitance tomography (ECT).The comparison of pressure drops from experiment and prediction showed that the Ergun equation was inappropriate to the pulsing flow
in which the gas-liquid interaction is significant. Therefore
the experimental two-phase pressure drop was used instead of the theoretical one for the calculation of gas relative permeability. It was found that the permeability of gas under various gas and liquid flow rates as well as different particle diameters was lower than 0.08 if pulsing flow was reached.