Adsorption of SO2 from wet mixtures on hydrophobic zeolites

被引:26
作者
Rouf, SA [1 ]
Eic, M [1 ]
机构
[1] Univ New Brunswick, Dept Chem Engn, Fredericton, NB E3B 5A3, Canada
来源
ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY | 1998年 / 4卷 / 01期
基金
加拿大自然科学与工程研究理事会;
关键词
hydrophobic zeolites; breakthrough curves; adsorption; binary mixtures; modeling; overall mass transfer; roll-up;
D O I
10.1023/A:1008883219403
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Breakthrough curve measurements of SO2 and water vapor were carried out on a number of selected mordenite and pentasil zeolites from their binary and ternary mixtures with CO2 at 50 and 100 degrees C. SO2 capacities of these samples were found to be significantly reduced by the presence of water. Competitive adsorption led to unusually high overshoot peaks of SO2 breakthrough curves. On the other hand, SO2 was found to displace water on the samples with very high silica to alumina ratio. A linear driving force, isothermal model was used to predict the breakthrough curves. Langmuir and extended Langmuir equilibrium models were used to describe the equilibrium properties of water and SO2, respectively. The overall mass transfer resistance obtained from the model was compared to the values calculated from a simplified biporous adsorbent model to shed some light on the adsorption kinetics.
引用
收藏
页码:25 / 33
页数:9
相关论文
共 11 条
[1]   GAS DISPERSION IN PACKED BEDS [J].
EDWARDS, MF ;
RICHARDS.JF .
CHEMICAL ENGINEERING SCIENCE, 1968, 23 (02) :109-&
[2]  
GARIEPY RL, 1971, AICHE S SER, V117, P67
[3]   NUMERICAL-SIMULATION OF A PSA SYSTEM .1. ISOTHERMAL TRACE COMPONENT SYSTEM WITH LINEAR EQUILIBRIUM AND FINITE MASS-TRANSFER RESISTANCE [J].
RAGHAVAN, NS ;
HASSAN, MM ;
RUTHVEN, DM .
AICHE JOURNAL, 1985, 31 (03) :385-392
[4]  
ROUF S, 1995, THESIS U NEW BRUNSWI
[5]  
ROUX AJ, 1973, AICHE S SER 69, V134, P46
[6]  
RUTHVEN DM, 1984, PRINCIPLES ADSORPTIO, P242
[7]   CHROMATOGRAPHIC-SEPARATION AND CONCENTRATION OF SULFUR-DIOXIDE IN FLUE-GASES [J].
STENGER, HG ;
HU, KH ;
SIMPSON, DR .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (11) :2736-2739
[8]   BREAKTHROUGH STUDY OF THE ADSORPTION AND SEPARATION OF SULFUR-DIOXIDE FROM WET GAS-USING HYDROPHOBIC ZEOLITES [J].
TANTET, J ;
EIC, M ;
DESAI, R .
GAS SEPARATION & PURIFICATION, 1995, 9 (03) :213-220
[9]  
Tantet J, 1993, THESIS U NEW BRUNSWI
[10]   BOUNDARY CONDITIONS OF FLOW REACTOR [J].
WEHNER, JF ;
WILHELM, RH .
CHEMICAL ENGINEERING SCIENCE, 1956, 6 (02) :89-93