SAPO-34 assisted C3 separation: Modeling and simulation

被引:21
作者
Agarwal, K. [1 ]
John, M. [2 ]
Pai, S. [2 ]
Newalkar, B. L. [2 ]
Bhargava, R. [1 ]
Choudary, N. V. [2 ]
机构
[1] Indian Inst Technol, Dept Chem Engn, Roorkee 247667, Uttar Pradesh, India
[2] Bharat Petr Corp Ltd, Corp R&D Ctr, Udyog Kendra 201306, Greater Noida, India
关键词
SAPO-34; C3; adsorption; Diffusion; Modeling; LIGHT OLEFINS; ZEOLITE; DIFFUSION; PERMEATION; MEMBRANE; SORPTION;
D O I
10.1016/j.micromeso.2010.02.024
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Chabazite (CHA) framework type SAPO-34 molecular sieve has been synthesized and its C3 (propane/propylene) uptake potential was evaluated in the temperature range of 303-323 K by measuring equilibrium and kinetic adsorption data using volumetric/gravimetric adsorption measurement technique. The measured data were analyzed by Langmuir-Freundlich isotherm model and Crank's equation respectively to estimate adsorption capacities, diffusivities and diffusion activation energies for C3 hydrocarbons. The estimated diffusivity data suggested a high kinetic selectivity for propylene over propane on SAPO-34 framework. A Wicke-Kallenbach cell for propane/propylene separation over SAPO-34 membrane was modeled, validated and used to investigate the effect of feed pressure, and composition on the selectivity of propylene over propane at 303 K. This model was further extended to simulate the performance of SAPO-34 tubular membrane for C3 separation for its practical utility. Based on the obtained results, SAPO-34 is found to be a potential candidate for kinetic separation of C3 mixtures at near ambient conditions. (C) 2010 Elsevier Inc. All rights reserved.
引用
收藏
页码:311 / 318
页数:8
相关论文
共 22 条
[1]  
AGARWAL K, 2009, THESIS INDIAN I TECH
[2]   Removal of propylene from fuel-grade propane [J].
Bryan, PF .
SEPARATION AND PURIFICATION REVIEWS, 2004, 33 (02) :157-182
[3]   Methanol conversion to light olefins over SAPO-34. Sorption, diffusion, and catalytic reactions [J].
Chen, D ;
Rebo, HP ;
Moljord, K ;
Holmen, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (11) :4241-4249
[4]  
CHENG LS, 1999, Patent No. 6296688
[5]  
Crank J., 1979, MATH DIFFUSION, V2nd
[6]  
DODGE, 1944, CHEM ENG THERMODYNAM
[7]   OLEFIN PARAFFIN SEPARATION TECHNOLOGY - A REVIEW [J].
ELDRIDGE, RB .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (10) :2208-2212
[8]   PROBLEMS AND PITFALLS IN THE USE OF THE FICK FORMULATION FOR INTRAPARTICLE DIFFUSION [J].
KRISHNA, R .
CHEMICAL ENGINEERING SCIENCE, 1993, 48 (05) :845-861
[9]   Analytic solution of the Maxwell-Stefan equations for multicomponent permeation across a zeolite membrane [J].
Krishna, R ;
Baur, R .
CHEMICAL ENGINEERING JOURNAL, 2004, 97 (01) :37-45
[10]   Modelling issues in zeolite based separation processes [J].
Krishna, R ;
Baur, R .
SEPARATION AND PURIFICATION TECHNOLOGY, 2003, 33 (03) :213-254