Absorption of VOCs in a rotating packed bed

被引：142

作者：

Chen, YS ^{[1
]}

Liu, HS ^{[1
]}

机构：

[1] Natl Taiwan Univ, Dept Chem Engn, Taipei, Taiwan

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH | 2002年 / 41卷 / 06期

关键词：

D O I：

10.1021/ie010752h

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

A Higee absorption process was developed to remove VOCs (volatile organic compounds) from air into an aqueous phase under a centrifugal field. The experimental results showed that the overall volumetric gas-phase mass-transfer coefficient (K(G)a) increased as a function of the gas Grashof number (Gr(G)) to the power of 0.18. In analyzing k(G) and a individually, it was found that the enhancement of mass transfer by the centrifugal force can mainly be attributed to an increase in the effective gas-liquid interfacial area. The values of k(G) lie in a range similar to that for conventional packed beds.

引用

页码：1583 / 1588

页数：6

共 15 条

[1]

GUO F, 1997, CHEM ENG SCI, V21, P3853

[2] Synchronous visual and RTD study on liquid flow in rotating packed-bed contactor [J].