Absorption of toluene in silicone oil: Effect of the solvent viscosity on hydrodynamics and mass transfer

被引:26
作者
Guillerm, Maxime [1 ,2 ]
Couvert, Annabelle [1 ,2 ]
Amrane, Abdeltif [1 ,2 ]
Norrant, Edith [3 ]
Lesage, Nicolas [4 ]
Dumont, Eric [5 ]
机构
[1] Ecole Natl Super Chim Rennes, UMR CNRS 6226, 11 Allee Beaulieu,CS 50837, F-35708 Rennes 7, France
[2] Univ Europeenne Bretagne, Rennes, France
[3] UCB BioPharma Sprl, Ave Ind B, B-1420 Braine Lalleud, Belgium
[4] Total SA, CSTJF, Ave Larribau,CA 374, F-64018 Pau, France
[5] Ecole Mines Nantes, UMR CNRS GEPEA 6144, 4 Rue Alfred Kastler,BP 20722, F-44307 Nantes 3, France
关键词
Absorption; PDMS; Silicone oil; Mass transfer; Toluene; Hydrodynamics; 2-PHASE PARTITIONING BIOREACTORS; VOLATILE ORGANIC-COMPOUNDS; VOLUME FRACTION; TECHNOLOGY; REMOVAL; LIQUID;
D O I
10.1016/j.cherd.2015.12.028
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The purpose of this study was to compare toluene absorption performances using two PDMS of different viscosities (eta = 5 and 50 mPa s, respectively) in terms of hydrodynamics and mass transfer. Three types of packing were tested in a counter-current packed gas-liquid contactor, Raschig rings, IMTP (R), and Flexipac (R). Hydrodynamic results showed that the viscosity of PDMS 50 is not a hurdle to be used with IMTP (R) or Flexipac (R); the pressure drop being around 288 Pa m(-1) for Flexipac (R) at the flooding point (F-G = 0.99 Pa-1/2; L'= 4.95 kg m(-2) s(-1)), which corresponds to an acceptable value for an industrial application. The determination of the loading zones showed that Raschig rings were not suitable for solvents having a high viscosity, such as PDMS 50; they resulted in high pressure drops if compared to IMTP (R) and Flexipac (R). The mass transfer study showed that 100% removal efficiency can be reached for both PDMS using Flexipac (R). For IMTP (R), the removal efficiency is limited to 88% in the presence of PDMS 50. As a result, PDMS 50 should be a relevant absorbing liquid for the removal of toluene in the absorption-biodegradation process, and Flexipac (R) packing should be preferred to IMTP (R). (c) 2016 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:32 / 40
页数:9
相关论文
共 19 条
[11]  
Mackay D., 2010, Handbook of physical-chemical properties and environmental fate for organic chemicals
[12]  
Mackowiak J, 2010, FLUID DYNAMICS OF PACKED COLUMNS: PRINCIPLES OF THE FLUID DYNAMIC DESIGN OF COLUMNS FOR GAS/LIQUID AND LIQUID/LIQUID SYSTEMS, P1, DOI 10.1007/b98397
[13]   Two-phase partitioning bioreactors in fermentation technology [J].
Malinowski, JJ .
BIOTECHNOLOGY ADVANCES, 2001, 19 (07) :525-538
[14]   Recent advances in two-phase partitioning bioreactors for the treatment of volatile organic compounds [J].
Munoz, Raul ;
Daugulis, Andrew J. ;
Hernandez, Maria ;
Quijano, Guillermo .
BIOTECHNOLOGY ADVANCES, 2012, 30 (06) :1707-1720
[15]  
Piché S, 2001, CHEM ENG TECHNOL, V24, P373, DOI 10.1002/1521-4125(200104)24:4<373::AID-CEAT373>3.0.CO
[16]  
2-0
[17]   Two-phase partitioning bioreactors in environmental biotechnology [J].
Quijano, Guillermo ;
Hernandez, Maria ;
Thalasso, Frederic ;
Munoz, Raul ;
Villaverde, Santiago .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 2009, 84 (05) :829-846
[18]  
Sinnott R.K., 2005, CHEM ENG DESIGN
[19]   Fate and effects of polydimethylsiloxane (PDMS) in marine environments [J].
Stevens, C ;
Powell, DE ;
Mäkelä, P ;
Karman, C .
MARINE POLLUTION BULLETIN, 2001, 42 (07) :536-543