Ethylene/ethane separation by gas-phase SMB in binderfree zeolite 13X monoliths

被引:28
作者
Seabra, Rute [1 ]
Martins, Vanessa F. D. [1 ]
Ribeiro, Ana M. [1 ]
Rodrigues, Alirio E. [1 ]
Ferreira, Alexandre P. [1 ]
机构
[1] Univ Porto, Fac Engn, LSRE Lab Separat & React Engn, Associate Lab LSRE LCM, Rua Dr Roberto Frias, P-4200465 Porto, Portugal
关键词
binderfree zeolite 13X; Honeycomb monoliths; Adsorption equilibrium; SMB; SIMULATED MOVING-BED; PROPANE/PROPYLENE SEPARATION; ADSORPTION; PERFORMANCE; TECHNOLOGY; ISOBUTANE; PROPYLENE; KINETICS; PROPANE; METHANE;
D O I
10.1016/j.ces.2020.116006
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, binderfree zeolite 13X monoliths were tested as a new promising material for high purity ethylene production from olefin/paraffin mixtures by gas-SMB technology. To characterize the adsorbent and its potential for the target separation, the equilibrium isotherms of ethane, ethylene, and propane were measured gravimetrically, in a temperature range from 323 K to 423 K, and pressure up to 7 bar. Dynamic studies were performed at 373 K and 1.5 bar in the gas-SMB bench-scale unit. For the experiment with 0.48/0.52 ethane/ethylene (molar based) feed composition, an ethylene purity of 97.7% was obtained, with a recovery above 90% and productivity of 16.9 kg(C2H4) center dot h(-1) center dot m(bed)(-3). Furthermore, the mathematical SMB model and the regions of separation were determined based on experimental data. This work experimentally demonstrated it is possible to produce high purity grade ethylene with a high recovery using binderfree zeolite 13X monoliths as adsorbent and propane as desorbent. (c) 2020 Elsevier Ltd. All rights reserved.
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页数:11
相关论文
共 37 条
[1]   Structuring adsorbents and catalysts by processing of porous powders [J].
Akhtar, Farid ;
Andersson, Linnea ;
Ogunwumi, Steven ;
Hedin, Niklas ;
Bergstrom, Lennart .
JOURNAL OF THE EUROPEAN CERAMIC SOCIETY, 2014, 34 (07) :1643-1666
[2]   Adsorption of methane, ethane, and ethylene on titanosilicate ETS-10 zeolite [J].
Al-Baghli, NA ;
Loughlin, KF .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2005, 50 (03) :843-848
[3]   Adsorption kinetics and dynamic behavior of a carbon monolith [J].
Brandani, F ;
Rouse, A ;
Brandani, S ;
Ruthven, DM .
ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 2004, 10 (02) :99-109
[4]  
Broughton D. B, 1961, U.S. Patent, Patent No. [US2985589, 2985589]
[5]   Gas phase SMB for propane/propylene separation using enhanced 13X zeolite beads [J].
Campo, M. C. ;
Baptista, M. C. ;
Ribeiro, A. M. ;
Ferreira, A. ;
Santos, J. C. ;
Lutz, C. ;
Loureiro, J. M. ;
Rodrigues, A. E. .
ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 2014, 20 (01) :61-75
[6]  
Do D.D., 1998, ADSORPTION ANAL EQUI, V2
[7]  
Dubinin M.M., 1960, RUSS CHEM B+, V9, P1072, DOI 10.1007/BF01161525
[8]  
Freitas F.A.d.S., 1999, Cyclic Adsorption Processes: Application to Propane/Propylene Separation
[9]   Simulated moving bed technology: old and new [J].
Gomes, Pedro Sa ;
Minceva, Mirjana ;
Rodrigues, Alirio E. .
ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 2006, 12 (5-6) :375-392
[10]   Design of a gas phase simulated moving bed for propane/propylene separation [J].
Gomes, Pedro Sa ;
Lamia, Nabil ;
Rodrigues, Alirio E. .
CHEMICAL ENGINEERING SCIENCE, 2009, 64 (06) :1336-1357