Binary adsorption of CO2/CH4 in binderless beads of 13X zeolite

被引:71
作者
Silva, Jose A. C. [1 ]
Cunha, Adelino F. [2 ]
Schumann, Kristin [3 ]
Rodrigues, Alirio E. [2 ]
机构
[1] Escola Super Tecnol & Gestao, Inst Politecn Braganca, P-5301857 Braganca, Portugal
[2] Univ Porto, Fac Engn, Dept Engn Quim, Lab Separat & React Engn, P-4100 Oporto, Portugal
[3] Chemiewerk Bad Kostritz GmbH, D-07586 Bad Kostritz, Germany
关键词
Binderless 13X zeolite; Binary adsorption of CO2/CH4; Fixed bed adsorption; Selectivity CO2/CH4; METAL-ORGANIC FRAMEWORKS; CARBON-DIOXIDE; GAS; SEPARATION; CO2; CAPTURE; METHANE; NITROGEN; CH4; EQUILIBRIUM;
D O I
10.1016/j.micromeso.2013.12.017
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The binary sorption CO2 and CH4 in binderless beads of 13X zeolite has been investigated between 313 and 473 K and total pressure up to 5 atm through fixed bed adsorption experiments. The amount adsorbed of CO2 and CH4 is around 4.7 mmol/g(ads) and 0.4 mmol/g(ads) respectively, at 313 K and 3.7 atm in a 50/50 equimolar mixture. In a 25(CO2)/75(CH4) mixture the amount adsorbed is 4.0 and 0.84 mmol/g at the same temperature and pressure. Experimental selectivities CO2/CH4 range from 37 at a low pressure of 0.667 atm to approximately 5 at the high temperature of 423 K. Comparing these values with the ones in literature CO2 adsorption capacity is 20% higher than in CECA 13X binder pellets. The CO2/CH4 binary isotherms were fitted with the extended Fowler model that takes into account interaction between adsorbed molecules at adjacent sites suggesting a moderate attraction between CO2 and CH4. The model is validated through a graphical method using the single component isotherm parameters. The breakthrough curves measured show a plateau of pure CH4 of approximately 6 min depending of the operating conditions chosen. AN (C) 2013 Elsevier Inc. All rights reserved.
引用
收藏
页码:100 / 107
页数:8
相关论文
共 32 条
[1]  
Bauer F., 2012, BIOGAS UPGRADING REV
[2]   Adsorption equilibrium of methane, carbon dioxide, and nitrogen on zeolite 13X at high pressures [J].
Cavenati, S ;
Grande, CA ;
Rodrigues, AE .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2004, 49 (04) :1095-1101
[3]   Upgrade of methane from landfill gas by pressure swing adsorption [J].
Cavenati, S ;
Grande, CA ;
Rodrigues, AE .
ENERGY & FUELS, 2005, 19 (06) :2545-2555
[4]   Metal organic framework adsorbent for biogas upgrading [J].
Cavenati, Simone ;
Grande, Carlos A. ;
Rodrigues, Alirio E. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (16) :6333-6335
[5]   Removal of carbon dioxide from natural gas by vacuum pressure swing adsorption [J].
Cavenati, Simone ;
Grande, Carlos A. ;
Rodrigues, Alirio E. .
ENERGY & FUELS, 2006, 20 (06) :2648-2659
[6]   Experimental Study on Adsorption of Carbon Dioxide by 5A Molecular Sieve for Helium Purification of High-Temperature Gas-Cooled Reactor [J].
Chang, Hua ;
Wu, Zong-Xin .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (09) :4466-4473
[7]  
Crespo P.S., 2011, CHEM MATER, V23, P2565
[8]   Carbon Dioxide Capture: Prospects for New Materials [J].
D'Alessandro, Deanna M. ;
Smit, Berend ;
Long, Jeffrey R. .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2010, 49 (35) :6058-6082
[9]   Separation of CO2/CH4 mixtures with the MIL-53(Al) metal-organic framework [J].
Finsy, V. ;
Ma, L. ;
Alaerts, L. ;
De Vos, D. E. ;
Baron, G. V. ;
Denayer, J. F. M. .
MICROPOROUS AND MESOPOROUS MATERIALS, 2009, 120 (03) :221-227
[10]  
Fowler RH., 1939, Statistical thermodynamics