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TMMC: Reference Adsorption Isotherms for N2/CO2 Mixtures in Metal-organic Frameworks

Transition-Matrix Monte Carlo (TMMC) simulations of  binary mixtures of N2 and CO2 [1-10] were performed at T = 300 K and 350 K in the ZIF-8 metal-organic framework (MOF). The main result of a GC-TMMC simulation is the particle number probability distribution (PNPD), which is constructed by stitching together the particle number distributions from each window. The adsorption isotherm may be determined from the PNPD [10].

Simulations used different combinations of Monte Carlo moves depending on the number of particles, as described below. Low density windows used a conventional set of moves (i.e., no configurational bias) whereas high density windows used a configurational bias strategy known as Dual-cut configurational bias (DCCB) Monte Carlo [13]. Additionally, low-density windows started in Wang-Landau biasing mode to quickly generate a guess of the PNPD, later switching to TMMC mode; data from the TMMC phase of the simulation was saved and reported here.

Other key simulation details common to all simulations are given below:

Fluid ModelTraPPE N2 and CO2[11]
Lennard-Jones cutoff12A (cut potential, no tail correction)
Ewald ParametersSet according to DL_POLY recipe [15], with relative tolerance 10-5
Trial Move TypesALL: Translation, Pivot rotation
Grand-Canonical:
    N < Nmax/2: Standard Insertion and Deletion
    N > Nmax/2: Dual-cut Configurational Bias (DCCB) [13] Growth
Isochoric Semigrand Canonical: Identity-change
 
DCCB DetailsNumber of trials per atom: 4
Reference Potential: Lennard-Jones + Ewald Realspace
Cutoff Radius for Reference Potential: 4.5A
Bias update freq1.0e5
Simulation Length200 sweeps [FEASST]
Physical ParametersCODATA 2018 [12]

Simulations were performed using the open-source FEASST Monte Carlo engine [11], using version 0.21.1 or 0.24.1.

The adsorbent MOF was reconstructed from publicly-available crystal structures and replicated to ensure that the simulation cell was at least twice the cutoff radius in all dimensions. Forcefields for each MOF were taken from published literature. The MOF structure and forcefield are provided in FEASST particle files in the data repository associated with this page (see "Data Availability" below). Coulombic interactions were handled using the Ewald summation method [2,3] (parameters listed in the metadata files). Lorentz-Berthelot combining rules were used to set the unlike-atom Lennard-Jones parameters.

Simulation details specific to each MOF 

 ZIF-8
NmaxN2:350; CO2: 300
Unit Cell Replication (Nx, Ny, Nz)(2,2,2)
Cubic Box Dimensions (A)34.023240
Simulation MOF Mass (amu)21846.91
MOF Forcefield,
Reference
Snurr [16]
FEASST MOF Particledata.ZIF8_Snurr_rep222

The result of each simulation is the PNPD and average potential energy (for each N state). The PNPD may be used to compute the adsorption isotherm by the histogram-reweighting procedure described by Shen and Errington [8]. All systems were single phase and, hence, no phase decomposition of the PNPD was necessary.

The pressure for a particular chemical potential pair was determined from TMMC simulations of the bulk N2/CO2 fluid at the same cutoff.

Results: ZIF-8

Temperature = 300K

Binary Adsorption Isotherm of N2/CO2 Mixture in ZIF-8 at 300K
Credit: NIST
Selectivity of CO2 versus N2 in ZIF-8 at 300K
Credit: NIST

 

Temperature = 350 K

Binary Adsorption Isotherm of N2/CO2 Mixture in ZIF-8 at 350K
Credit: NIST
Selectivity of CO2 versus N2 in ZIF-8 at 350K
Credit: NIST

 

Data Availability

Various data files used to generate the reference isotherms are available in a Git Repository: https://github.com/dwsideriusNIST/NIST_SRSW_Data/tree/master/N2_CO2_REF_ISOTHERMS

Files in the repository include:
FEASST particle file for the MOF material [includes atomic coordinates and the forcefield parameters]
FEASST particle files for TraPPE N2 and CO
Particle number probability distributions for the adsorbed fluid mixture
Isotherm data files, including the individual species adsorption isotherms and selectivity and estimated uncertainties, formatted as AIF files [17]

References

  1. J. R. Errington, J. Chem. Phys. 118, 9915 (2003).
  2. M. P. Allen and D. J. Tildesley, Computer Simulation of Liquids (Oxford University Press, New York, 1989).
  3. D. Frenkel and B. Smit, Understanding Molecular Simulation, 2nd ed. (Academic, San Diego, 2002)., pp.37-38.
  4. J. R. Errington and A. Z. Panagiotopoulos, J. Chem. Phys., 109, 1093 (1998).
  5. J. R. Errington and V. K. Shen, J. Chem. Phys., 123, 164103 (2005).
  6. V. K. Shen and D. W. Siderius, J. Chem. Phys., 140, 244106, 2014.
  7. V. K. Shen and J. R. Errington, JPC B 108, 19595, 2004.
  8. V. K. Shen and J. R. Errington, JCP 122, 064508, 2005.
  9. V. K. Shen, R. D. Mountain, and J. R. Errington, JPC B 111, 6198, 2007.
  10. D. W. Siderius and V. K. Shen, JPC C 117, 5681, 2013.
  11. J. A. Potoff and J. I. Siepmann, AIChE J., 47, 1676–1682, 2001.
  12. CODATA Internationally recommended 2018 values of the Fundamental Physical Constants
  13. T. J. H. Vlugt, M. G. Martin, B. Smit, J. I. Siepmann, and R. Krishna, Mol Phys, 94, 727, 1998.
  14. H. W. Hatch, N. A. Mahynski, and V. K. Shen J Res Natl Inst Stan, 123, 123004, 2018.
  15. E. I. Todorov and W. Smith, The DL\_POLY User Manual (version 4.03).
  16. H. Zhang and R. Q. Snurr, JPC C, 121, 24000, 2017.
  17. J. D. Evans, V. Bon, I. Senkovska, S. Kaskel, Langmuir, 37, 4222, 2021.
Created September 17, 2024, Updated September 18, 2024