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Copyright © 2005 The Biophysical Society. All rights reserved.
Biophysical Journal, Volume 89, Issue 6, L58-L60, 1 December 2005

doi:10.1529/biophysj.105.073718

Biophysical Letters

Improvement of Biodesulfurization Rate by Assembling Nanosorbents on the Surfaces of Microbial Cells

S. Guobin^*, †, ,  , Z. Huaiying^*, †, C. Weiquan^*, †, X. Jianmin^* and L. Huizhou^*,  

^* Laboratory of Separation Science and Engineering, State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing, 100080, China
^† Graduate School of the Chinese Academy of Sciences, Beijing, China

Address reprint requests and inquiries to Dr. Shan Guobin, Fax: 86-10-62554264.

Recently, biodesulfurization of petroleum products has received growing attention as the production of ultra-low-sulfur products 1. However, it is still not a commercial technology because of some problems, such as desulfurization rate, bioreactor design, and the volumetric ratio between the oil and aqueous phases. Among these, desulfurization rate represents the main limiting factor for an industrial application of the biotechnological process. Many progresses have been done in improvement of biodesulfurization rate in the last years by increasing the activity of biocatalysts. Despite considerable progress in improving the expression and copies of the key enzymes 2,3, the flux through the system is still too low for widespread commercial applications 1. Setti et al. 4 and Mehrnia et al. 5 reported that transfer of polycyclic aromatic sulfur heterocycle (such as DBT) from the oil to the water (and then from the water to the cells) can limit the rate of its metabolism.

In this study, a novel biodesulfurization technology was developed by assembling γ-Al₂O₃ nanosorbent, which can selectively adsorb DBT (a model polycyclic aromatic sulfur heterocycle) from the organic phase, on the surfaces of microbial cell. The approach to increase the rate of biodesulfurization is based on the improvement of transfer rate of DBT.

Pseudomonas delafieldii R-8 6, was isolated from the sewage pool of Shengli oil field in China, and has the ability to convert DBT to 2-hydroxy-biphenyl (2-HBP) and sulfate.

We synthesized γ-Al₂O₃ nanosorbent by the following method. We dissolved 25g Al(NO₃)₃·9H₂O in 100ml distilled water including 0.1g of cetyltrimethylammonium bromide (CTAB), and then added dropwise a 10% of NH₄HCO₃ aqueous solution including 0.1g of CTAB. The addition was stopped until the sol was formed. The additional amount of NH₄HCO₃ aqueous solution was ∼50ml. To continue to stir for 1h, and then age for 48h, the products were dried in vacuum for 5h at 80°C. Finally, γ-A1₂O₃ nanosorbents were obtained by sintering at 600°C.

Gamma-Al₂O₃ nanosorbents (0.1g) and 0.5g of dry cells were added into 50ml of saline water (8.5% NaCl). The cells assembled with γ-Al₂O₃ nanosorbents were harvested and vacuum-dried at −4°C. Each cell preparation (the aforementioned γ-Al₂O₃-cells or 0.5 of dry cells) was suspended in 15ml phosphate buffer (0.1M, pH=7.0), and the suspension was mixed with 15ml of model oil (5.0mM DBT in n-dodecane). The reaction was carried out in 100-ml flasks at 30°C on a rotary shaker at 180rpm.

FIGURE 1ab, are two transmission electron microscope (TEM) images of γ-Al₂O₃ nanosorbent with different magnifications (×10,000 and ×200,000). It is clearly shown that γ-Al₂O₃ sorbents prepared are very thin long-fiber shape. Its length is ∼100nm, and its width is only a few nanometers. Thus, the size of the sorbent is much smaller than that of microbial cell, which is about a few micrometers.

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FIGURE 1

TEM images of γ-Al₂O₃ nanosorbent (obtained by Hitachi 8100, 200kV). (a) ×10,000; (b) ×200,000.

FIGURE 2ab, are TEM images of free cell and microbial cell assembled with γ-Al₂O₃ nanosorbents, respectively. The γ-Al₂O₃ nanosorbents were efficiently assembled on the surfaces of microbial cell as shown in Fig. 2.

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FIGURE 2

TEM images of free cell and cell assembled with γ-Al₂O₃ nanosorbent. (a) Free cell. (b) γ-Al₂O₃-cell.

To investigate the adsorptive ability of γ-Al₂O₃ nanosorbents, an adsorptive process was performed in normal pressure, which 0.1g sorbents were added into 5mL model oil containing 5.0mM of DBT and 5.0mM of 2-HBP. Fig. 3 shows the adsorptive curve of γ-Al₂O₃ nanosorbents at 30°C. During the first 0.5h, DBT and 2-HBP concentrations were, respectively, reduced to 2.69 and 2.85mM from 5.00mM. According to Fig. 3, the sorbents have been saturated with DBT and 2-HBP for <0.5h. So, the adsorptive rate of γ-Al₂O₃ nanosorbents was >446mmolkg⁻¹h⁻¹.

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FIGURE 3

Adsorption of DBT and 2-HBP using γ-Al₂O₃ nanosorbents.

With the purpose of understanding the desulfurizing activity of the γ-Al₂O₃-cells, we tested the desulfurization rates of free cells and the γ-Al₂O₃-cells in model oil containing 5.0mM of DBT, respectively. Fig. 4 shows that the consumption of DBT and the production of 2-HBP using free cells and γ-Al₂O₃-cells in the model oil. During the first 0.5h, the rate of DBT consumption by the γ-Al₂O₃-cells is ∼4.93-fold higher than that by free cells. However, during the same time, the rate of 2-HBP produced by the γ-Al₂O₃-cells is only 1.02-fold higher than that by free cells. The rate of DBT consumption is not consistent with that of 2-HBP produced in model oil. However, during the subsequent 1.0h, both the rates of DBT consumption and 2-HBP produced by the γ-Al₂O₃-cells are the same, which are ∼1.73-fold higher than those by free cells. It is because that the γ-Al₂O₃ nanosorbents can adsorb DBT from model oil, and the rate of adsorption is far higher than that of BDS (Fig. 2). The adsorption process can increase the rate of DBT transfer. During the first 0.5h, a part amount of DBT molecules, ∼0.117mmol (DBT consumed+2-HBP produced)/g(sorbent), was adsorbed into the pores of γ-Al₂O₃ nanosorbent, which resulted in the reduction of DBT and 2-HBP concentrations in oil phase. However, DBT molecules of these cannot be reacted and converted to 2-HBP by microbial cells. Besides, 2-HBP molecules of these produced were adsorbed into the γ-Al₂O₃ nanosorbents and could not be detected in oil phase. Therefore, the rate of DBT consumption in oil phase was higher than that of 2-HBP produced, detected in oil phase, during the first time. On the other hand, once the pores of γ-Al₂O₃ nanosorbents were saturated with DBT and 2-HBP molecules, the consumption of DBT in oil phase can completely be used to convert to 2-HBP, which also was completely transferred to oil phase. Thus, the increase of DBT consumption rate was equivalent to that of 2-HBP production rate after the saturation of sorbents with DBT. The final concentration of 2-HBP produced by γ-Al₂O₃-cells was ∼3.83mM, less than the initial concentration of DBT. It may deduce that ∼0.012mmol of DBT and 2-HBP were adsorbed into the pores of γ-Al₂O₃ nanosorbent.

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FIGURE 4

Time course of desulfurization of DBT by free cells and γ-Al₂O₃-cells. Residual DBT concentration after being consumed by free cells (△); 2-HBP concentration produced by free cells (▴); residual DBT concentration after being consumed by γ-Al₂O₃-cells (□); 2-HBP concentration produced by γ-Al₂O₃-cells (■).

The biodesulfurization rate of R-8 cells has been improved by γ-Al₂O₃-cell (Fig. 4). It is because that the desulfurization rate was mainly limited by the following two factors, i.e., catalytic activity of dsz enzymes in cells and the rate of mass transfer from oil phase to the cell body through aqueous phase. The adsorption of γ-Al₂O₃ nanosorbents to DBT can accelerate the DBT transfer from aqueous phase to the cell surfaces, which results in the increase of desulfurization rate. According to Fig. 3, the adsorptive rate of the γ-Al₂O₃ nanosorbent is >446mmolkg⁻¹h⁻¹, which is far higher than the desulfurization rate of microbial cells. Thus, DBT molecules can be quickly congregated on the cell surface, where nanosorbents were located. Consequently, the DBT molecules can be transported into cell for biodesulfurization reaction. Thus, transfer limitation of the DBT molecules can be eliminated to some extent, which results in the improvement of biodesulfurization rate.