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In this application the MAPS Towhee [1] plug-in was used to calculate
the relative adsorption of N2 and CO2 in an LSX-Li zeolite.
This type of simulation is important for the gas separation process,
where companies would like to use zeolites to separate mixtures of gases to produce
pure gas components.
Variation in the type of zeolite, as well as varying cation content or the type of cation
can have a significant impact on the selective adsorption of different gases and hence
on the efficiency of the separation process.
The framework structure of LSX for this study was taken from a zeolite database. Then
the cation locator script within MAPS was employed to replace a number of silicon
atoms by aluminum atoms and to place Li cations at the appropriate places in the
framework.

Finally the accessible free volume was calculated, and areas not accessible by diffusion
were blocked by hard spheres for the following Towhee simulation.
The image below shows the free volume in the zeolite, the non accessible free volume
is characterized by small spherical volume areas.
Atomistic structures of Nitrogen and Carbon Dioxide were also constructed and used for
the following Grand Canonical Monte Carlo simulation with the Towhee Monte Carlo
simulation package integrated into MAPS. Simulation parameters were taken from
literature [2] [3] [4] and simulation setup and analysis were done within MAPS. Both
adsorbent molecules were considered rigid, for N2 a three point charge model was used
in order to appropriately represent the quadruple moment of the N2 molecule.
Simulation
Grand Canonical Monte Carlo (GCMC) with the Towhee plug-in was performed in order
to calculate the absorption isotherms at 293 K. The fugacity and hence the chemical
potential for each N2 and CO2 was calculated at the desired pressures by using PCSAFT
equations of state with the SciTherm plug-in within MAPS.
Results£º
The following graphs represent the results of the GCMC Towhee calculations:


As can be clearly seen, CO2 is adsorbed at lower pressures in the zeolite compared to
N2, likely due to its more polar character. The upper loading limit is also higher for CO2
compared to N2. This is well in agreement with experiment. For absolute numbers, the simulation results rank higher than the experimental loading curves.
It has been shown in a different set of simulations however, that by keeping the cations
flexible
throughout the simulations absolute agreement between experimental and simulated
results can be significantly improved.
Figure 4 shows the final result of the Towhee runs at 6.30 bar.

References:
1. M.G. Martin, J. I. Siepmann, J. Phys. Chem. B, 103, 4908 ¨C 4917, 1999.
2. K. Watanabe, N. Austin and M. R. Stapleton, Molecular Simulation, 15, 197, 1995.3.
3. A.J. Richards, K.Watanabe, N.Austin and M.R.Stapleton, Journal of Porous Materials, 2, 43, 1995.
4. J. G. Harris, K. H. Yung, Journal Chemical Physics, 99(31), 12021, 1995.


[ Last edited by ghcacj on 2010-12-17 at 12:33 ]
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zyj8119

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Originally posted by ghcacj at 2010-12-18 16:56:39:
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zyj8119

ľ³æ (ÖøÃûдÊÖ)

ÒýÓûØÌû:
Originally posted by ghcacj at 2010-12-18 16:56:39:
MAPSÀïÓÐÄ£¿é¾ÓÈ»¿ÉÒÔÖ±½Ó¹ÀËã»¯Ñ§ÊÆºÍÒݶȣ¬Õ⻹ͦ·½±ãµÄ£¬²»È»Ö±½ÓÊäÈë»¯Ñ§ÊÆ¾ÍÌ«Âé·³ÁË¡£

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The fugacity and hence the chemical
potential for each N2 and CO2 was calculated at the desired pressures by using PCSAFT
equations of state with the SciTherm plug-in within MAPS.
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