4.6 Article

Biodesulfurization of Dibenzothiophene and Its Alkylated Derivatives in a Two-Phase Bubble Column Bioreactor by Resting Cells of Rhodococcus erythropolis IGTS8

期刊

PROCESSES
卷 9, 期 11, 页码 -

出版社

MDPI
DOI: 10.3390/pr9112064

关键词

biodesulfurization kinetics; Rhodococcus erythropolis IGTS8; resting cells; dibenzothiophene; alkylated dibenzothiophene; bubble column bioreactor

资金

  1. European Regional Development Fund of the European Union
  2. Greek national funds through the Operational Program Competitiveness, Entrepreneurship, and Innovation, under the call RESEARCH-CREATE-INNOVATE [T1ED K-02074, MIS 5030227]
  3. European Union
  4. Greek National Funds (European Social Fund) through the Operational Program Human Resources Development, Education, and Lifelong Learning [MIS 5033021]

向作者/读者索取更多资源

BDS using resting cells of Rhodococcus erythropolis IGTS8 was investigated in a bubble column bioreactor with two-phase media, finding that biocatalyst performance was best at an OFP of 50% v/v, and biocatalysts from the exponential growth phase exhibited the highest biodesulfurization efficiency. A new semi-empirical model based on Michaelis-Menten kinetics was developed to describe the biphasic BDS process.
Biodesulfurization (BDS) is considered a complementary technology to the traditional hydrodesulfurization treatment for the removal of recalcitrant sulfur compounds from petroleum products. BDS was investigated in a bubble column bioreactor using two-phase media. The effects of various process parameters, such as biocatalyst age and concentration, organic fraction percentage (OFP), and type of sulfur compound-namely, dibenzothiophene (DBT), 4-methyldibenzothiophene (4-MDBT), 4,6-dimethyldibenzothiophene (4,6-DMDBT), and 4,6-diethyldibenzothiophene (4,6-DEDBT)-were evaluated, using resting cells of Rhodococcus erythropolis IGTS8. Cells derived from the beginning of the exponential growth phase of the bacterium exhibited the highest biodesulfurization efficiency and rate. The biocatalyst performed better in an OFP of 50% v/v. The extent of DBT desulfurization was dependent on cell concentration, with the desulfurization rate reaching its maximum at intermediate cell concentrations. A new semi-empirical model for the biphasic BDS was developed, based on the overall Michaelis-Menten kinetics and taking into consideration the deactivation of the biocatalyst over time, as well as the underlying mass transfer phenomena. The model fitted experimental data on DBT consumption and 2-hydroxibyphenyl (2-HBP) accumulation in the organic phase for various initial DBT concentrations and different organosulfur compounds. For constant OFP and biocatalyst concentration, the most important parameter that affects BDS efficiency seems to be biocatalyst deactivation, while the phenomenon is controlled by the affinities of biodesulfurizing enzymes for the different organosulfur compounds. Thus, desulfurization efficiency decreased with increasing initial DBT concentration, and in inverse proportion to increases in the carbon number of alkyl substituent groups.

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