Adsorption of CO2, CH4, CO2/N2 and CO2/CH4 in Novel Activated Carbon Beads: Preparation, Measurements and Simulation

被引:100
作者
Shao, Xiaohong [1 ,2 ]
Feng, Zhenhe [2 ]
Xue, Ruisheng [3 ]
Ma, Congcong [1 ]
Wang, Wenchuan [1 ]
Peng, Xuan [4 ]
Cao, Dapeng [1 ]
机构
[1] Beijing Univ Chem Technol, Minist Educ, Key Lab Nanomat, Beijing 100029, Peoples R China
[2] Beijing Univ Chem Technol, Coll Sci, Beijing 100029, Peoples R China
[3] Beijing Univ Chem Technol, Minist Educ, Key Lab Carbon Fiber & Funct Polymers, Beijing 100029, Peoples R China
[4] Beijing Univ Chem Technol, Coll Informat Sci, Beijing 100029, Peoples R China
关键词
absorption; materials; simulation; molecular; environmental engineering; METAL-ORGANIC FRAMEWORKS; CAPILLARY CONDENSATION; MESOCARBON MICROBEADS; METHANE ADSORPTION; STORAGE; DIOXIDE; HYDROGEN; GAS; SEPARATION; EQUILIBRIA;
D O I
10.1002/aic.12515
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A series of high performance carbonaceous mesoporous materials: activated carbon beads (ACBs), have been prepared in this work. Among the samples, ACB-5 possesses the BET specific surface area of 3537 m 2 g(-1) and ACB-2 has the pore volume of 3.18 cm 3 g(-1). Experimental measurements were carried out on the intelligent gravimetric analyzer (IGA-003, Hiden). Carbon dioxide adsorption capacity of 909 mg g(-1) has been achieved in ACB-5 at 298 K and 18 bar, which is superior to the existing carbonaceous porous materials and comparable to metal-organic framework (MOF)-177 (1232 mg g(-1), at 298 K and 20 bar) and covalent-organic framework (COF)-102 (1050 mg g(-1) at 298 K and 20 bar) reported in the literature. Moreover, methane uptake reaches 15.23 wt % in ACB-5 at 298 K and 18 bar, which is better than MOF-5. To predict the performances of the samples ACB-2 and ACB-5 at high pressures, modeling of the samples and grand canonical Monte Carlo simulation have been conducted, as is presented in our previous work. The adsorption isotherms of CO2/N-2 and CO2/CH4 in our samples ACB-2 and 5 have been measured at 298 and 348 K and different compositions, corresponding to the pre- and postcombustion conditions for CO2 capture. The Dual-Site Langmuir-Freundlich (DSLF) model-based ideal-adsorbed solution theory (IAST) was also used to solve the selectivity of CO2 over N-2 and CH4. The selectivities of ACBs for CO2/CH4 are in the range of 2-2.5, while they remain in the range of 6.0-8.0 for CO2/N-2 at T = 298 K. In summary, this work presents a new type of adsorbent-ACBs, which are not only good candidates for CO2 and CH4 storage but also for the capture of carbon dioxide in pre- and postcombustion processes. (C) 2011 American Institute of Chemical Engineers AIChE J, 57: 3042-3051, 2011
引用
收藏
页码:3042 / 3051
页数:10
相关论文
共 39 条
[1]   Methane storage in activated carbon fibres [J].
AlcanizMonge, J ;
delaCasaLillo, MA ;
CazorlaAmoros, D ;
LinaresSolano, A .
CARBON, 1997, 35 (02) :291-297
[2]   CO2 capture capacities of activated carbon fibre-phenolic resin composites [J].
An, Hui ;
Feng, Bo ;
Su, Shi .
CARBON, 2009, 47 (10) :2396-2405
[3]   Storage and separation of CO2 and CH4 in silicalite, C168 schwarzite, and IRMOF-1:: A comparative study from monte carlo simulation [J].
Babarao, Ravichandar ;
Hu, Zhongqiao ;
Jiang, Jianwen ;
Chempath, Shaji ;
Sandler, Stanley I. .
LANGMUIR, 2007, 23 (02) :659-666
[4]   High-throughput synthesis of zeolitic imidazolate frameworks and application to CO2 capture [J].
Banerjee, Rahul ;
Phan, Anh ;
Wang, Bo ;
Knobler, Carolyn ;
Furukawa, Hiroyasu ;
O'Keeffe, Michael ;
Yaghi, Omar M. .
SCIENCE, 2008, 319 (5865) :939-943
[5]   Modeling the selectivity of activated carbons for efficient separation of hydrogen and carbon dioxide [J].
Cao, DP ;
Wu, JZ .
CARBON, 2005, 43 (07) :1364-1370
[6]   Experiment, molecular simulation and density functional theory for investigation of fluid confined in MCM-41 [J].
Cao, DP ;
Shen, ZG ;
Chen, JF ;
Zhang, XR .
MICROPOROUS AND MESOPOROUS MATERIALS, 2004, 67 (2-3) :159-166
[7]   Determination of pore size distribution and adsorption of methane and CCl4 on activated carbon by molecular simulation [J].
Cao, DP ;
Wang, WC ;
Shen, ZG ;
Chen, JF .
CARBON, 2002, 40 (13) :2359-2365
[8]   Optimization of single-walled carbon nanotube arrays for methane storage at room temperature [J].
Cao, DP ;
Zhang, XR ;
Chen, JF ;
Wang, WC ;
Yun, J .
JOURNAL OF PHYSICAL CHEMISTRY B, 2003, 107 (48) :13286-13292
[9]   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
[10]   Adsorption of natural gas and biogas components on activated carbon [J].
Esteves, Isabel A. A. C. ;
Lopes, Marta S. S. ;
Nunes, Pedro M. C. ;
Mota, Jose P. B. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2008, 62 (02) :281-296