Modeling Volatile Organic Compound Stripping in a Rotating Disk Contactor System
Document Type
Article
Publication Date
11-1-1991
Abstract
A rotating disk contactor (RDC) was used for studying the mass transfer of five volatile organic compounds from the liquid to the gas phase. The observed mass-transfer rates of these compounds were found to be a function of disk submergence and rotational speed. A theoretical model based on the combination of a completely mixed flow reactor and a plug flow reactor was developed. The apparent mass-transfer coefficient (Kapp) is theoretically affected by the disk characteristics (disk size and type), operational conditions (flow rate, disk submergence, and speed), and intrinsic VOC mass-transfer coefficient in the basin. Specifically, under high rotational speeds (0.6-1.5 rad/s), Kapp is a function of speed to the power of 1.5. © 1991, American Chemical Society. All rights reserved.
Identifier
0026314917 (Scopus)
Publication Title
Environmental Science and Technology
External Full Text Location
https://doi.org/10.1021/es00023a008
e-ISSN
15205851
ISSN
0013936X
First Page
1891
Last Page
1896
Issue
11
Volume
25
Recommended Citation
Hao, Oliver J.; Davis, Allen P.; Wu, Yuen C.; and Hsueh, Kal P., "Modeling Volatile Organic Compound Stripping in a Rotating Disk Contactor System" (1991). Faculty Publications. 17503.
https://digitalcommons.njit.edu/fac_pubs/17503
