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C HEMISTRY - Research: Dr. Kyle A. Beran


Thermodynamics of the hydrodesulfurization (HDS) process

A new method of performing the hydrodesulfurization (HDS) process utilizes a homogeneous catalyst, contrary to the current use of heterogeneous varieties, to extract the sulfur-containing molecules from petroleum feedstocks. The prototype catalyst, shown to the right, is a RuII(NH3)5OH2 complex that is soluble in water.

catalyst

Overview

Environmental concerns regarding the amount of pollution contributed to the atmosphere by combustion engines requires the more efficient removal of organosulfur compounds from petroleum feedstocks. Currently, the desulfurization process utilizes heterogeneous catalyst systems, such as Co-Mo/Al2O3 or Ni-Mo/Al2O3, to remove the sulfur-containing compounds. Although these catalysts have been successful in removing thiols, thioesters, thiophenes, and benzothiophenes, in a process called hydrodesulfurization (HDS), the catalyst-based processes have been unsuccessful in performing HDS on hindered dibenzothiophenes (4,6-R2DBT, see Figure 1). The presence of alkyl groups substituted at the 4 and/or 6 positions greatly impedes the interaction between the catalyst and the sulfur. To adhere to the EPA's sulfur-content guidelines4, the "deep hydrodesulfurization" of DBTs from fuels is imperative.

thiophene benzothiphene dibenzothiophene
Figure 1. Schematics (left to right) of thiophene, benzothiophene (BT), and 4,6-dibenzothiophene (4,6-R2DBT). R = -H, -CH3, -CH2CH3, etc.

An alternative method utilizes a ruthenium complex, in the absence of catalytic support, in a homogeneous aqueous solution to selectively bind and extract the DBT molecules from petroleum feedstocks.

Research

The simplistic description of the experimental process is to mix the aqueous phase (extracting complex) with the organic phase (sulfur species). This procedure would establish an equilibrium (shown below) that can be used to quantify the affinity that

Ru(NH3)52+ + L ↔ Ru(NH3)5L2+


certain ligands have for the metal-based extracting complex. This phase of the project seeks to theoretically calculate the bond-dissociation energy (BDE) between the metal complex and the sulfur ligands and then correlate BDE values to the experimentally obtained ligand affinity. The difficulty experienced by the near-planar heterogeneous catalysts to perform deep-HDS can be visualized in Figure 2, where the optimized geometries of the RuII complexes for DBT, 2,8-Me2DBT, and 4,6-Me2DBT compared.
figure 2.1 figure 2.2 figure 2.3
Figure 2. Equilibrium geometry for DBT, 2,8-Me2DBT, and 4,6-Me2DBT.

As can be clearly seen, the DBT and the 2,8 complex are very similar in Ru-S bond length and the angle with which the ligand makes with the plane of the NH3 groups. However, the 4,6 complex clearly exhibits a much sharper angle (approaching 90o) as well as a slightly longer Ru-S bond length. It is the steric hindrance introduced by substitution at the 4 and 6 positions that causes the heterogeneous catalysts to become ineffective, whereas the homogeneous RuII complexes further reduce (deep-HDS) the sulfur content in petroleum feedstocks by about 50%.

The computational methodology that we employ determines the equilibrium geometry using density functional theory (DFT), followed by the vibrational analysis of each specie to insure that it occupies a stationary point. The raw data obtained from theory is then used to calculate the BDE between the metal complex and the ligand, as shown in the steps below.

H298 = Et + ZPE + Htr + Hvib + Hrot + RT

The bond dissociation energy, in kcal/mole, for the molecular complex is then calculated using Equation (3).
ΔHRxn = BDE = H298(products) – H298(reactants)

The focus of this project is to correlate experimentally determined equilibrium ligand affinities to theoretical bond dissociation energies, followed by the extrapolation of our theoretical technique to other metal-centered complexes. An initial study of the DBT derivatives in Figure 2 show that the theoretical BDE values follow the same trend (2,8-Me2DBT > DBT > 4,6-Me2DBT) as that of the experimental ligand affinities. Also, owing to the stabilization of the M(II)-S σ bond by the presence of the –CH3 groups, the BDE of 2,8-DBT is larger than that of the unsubstituted DBT ligand. These trends are consistent when other sulfur-containing organics (thiophene, benzothiophene, etc.) are added to the series. We have seen similar general trends when the identity of the metal has been changed to Fe or Cr, for example. However, when we try to incorporate the BDE values of nitrogen-based organics, the trend begins to fail (i.e. the magnitude of the N-based theoretical BDE within the series is not consistent with its position within the ligand affinity series). This discrepancy will be addressed in our future considerations.

What's Next
  1. Complete vibrational analysis of Co, Rh, Ir, Mo, W, and Os metal complexes.
  2. Subsequent BDE comparison of these three complexes to Ru, Fe, Cr.
  3. Incorporate solvent effects into theoretical computations.
  4. Calculate ΔGrxn values for evaluation/comparison.
  5. Perform BDE calculations for these porphyrinic complexes.
  6. Compare to M(II)(NH3)5(H2O)2+ results.
  7. Seek out structural and substitution modifications to further expose/improve predicted binding strength.

 

 

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