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
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