Characterization of carbon molecular sieves using methane and carbon dioxide as adsorptive probes

被引:43
作者
Rutherford, SW
Nguyen, C
Coons, JE
Do, DD
机构
[1] Los Alamos Natl Lab, Engn Sci & Applicat Div, Los Alamos, NM 87545 USA
[2] CSIRO Mfg & Infrastruct Technol, Clayton, Vic 3168, Australia
[3] Univ Queensland, Dept Chem Engn, St Lucia, Qld 4072, Australia
关键词
D O I
10.1021/la034472d
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Nitrogen adsorption at 77 K is the current standard means for pore size determination of adsorbent materials. However, nitrogen adsorption reaches limitations when dealing with materials such as molecular sieving carbon with a high degree of ultramicroporosity. In this investigation, methane and carbon dioxide adsorption is explored as a possible alternative to the standard nitrogen probe. Methane and carbon dioxide adsorption equilibria and kinetics are measured in a commercially derived carbon molecular sieve over a range of temperatures. The pore size distribution is determined from the adsorption equilibrium, and the kinetics of adsorption is shown to be Fickian for carbon dioxide and non-Fickian for methane. The non-Fickian response is attributed to transport resistance at the pore mouth experienced by the methane molecules but not by the carbon dioxide molecules. Additionally, the change in the rate of adsorption with loading is characterized by the Darken relation in the case of carbon dioxide diffusion but is greater than that predicted by the Darken relation for methane transport. Furthermore, the proposition of inkbottle-shaped micropores in molecular sieving carbon is supported by the determination of the activation energy for the transport of methane and subsequent sizing of the pore-mouth barrier by molecular potential calculations.
引用
收藏
页码:8335 / 8342
页数:8
相关论文
共 33 条
[11]  
Lacava A.I., 1989, Gas Sep. Purif, V3, P180
[12]  
LIU H, 1996, P 5 INT C FUND ADS
[13]  
LOUGHLIN KF, 1993, GAS SEP PURIF, V7, P264, DOI DOI 10.1016/0950-4214(93)80028-U
[14]   Micropore size distributions of activated carbons and carbon molecular sieves assessed by high-pressure methane and carbon dioxide adsorption isotherms [J].
Lozano-Castelló, D ;
Cazorla-Amorós, D ;
Linares-Solano, A ;
Quinn, DF .
JOURNAL OF PHYSICAL CHEMISTRY B, 2002, 106 (36) :9372-9379
[15]   New method for the characterization of porous materials [J].
Nguyen, C ;
Do, DD .
LANGMUIR, 1999, 15 (10) :3608-3615
[16]   Dual Langmuir kinetic model for adsorption in carbon molecular sieve materials [J].
Nguyen, C ;
Do, DD .
LANGMUIR, 2000, 16 (04) :1868-1873
[17]   Adsorption of supercritical gases in porous media: Determination of micropore size distribution [J].
Nguyen, C ;
Do, DD .
JOURNAL OF PHYSICAL CHEMISTRY B, 1999, 103 (33) :6900-6908
[18]   Adsorption rate of methane and carbon dioxide on activated carbon by the semi-batch constant molar flow rate method [J].
Prasetyo, I ;
Do, DD .
CHEMICAL ENGINEERING SCIENCE, 1998, 53 (19) :3459-3467
[19]   Adsorption of gases on a carbon molecular sieve used for air separation: Linear adsorptives as probes for kinetic selectivity [J].
Reid, CR ;
Thomas, KM .
LANGMUIR, 1999, 15 (09) :3206-3218
[20]   Adsorption of gases on carbon molecular sieves used for air separation. Spherical adsorptives as probes for kinetic selectivity [J].
Reid, CR ;
O'koye, IP ;
Thomas, KM .
LANGMUIR, 1998, 14 (09) :2415-2425