4.6 Article

Modeling the Liquid Fuel Desulfurization Efficiency of Activated Carbons before and after Chemical Treatment: The Competitive Role of Mono- and Diaromatics

Journal

Publisher

AMER CHEMICAL SOC
DOI: 10.1021/acs.iecr.2c02794

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Funding

  1. European Regional Development Fund of the European Union
  2. Greek national funds through the Operational Program Competitiveness, Entrepreneurship and Innovation [?2E?K-01976]
  3. RESEARCH-CREATE-INNOVATE B' CALL (Project: DESULFUR)
  4. [EPAnEK 2014-2020]

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This study focuses on the experimental and modeling investigation of adsorptive deep desulfurization using activated carbons. The effects of oxidative chemical treatment and the presence of aromatic compounds on desulfurization kinetics and performance are examined. The results show that chemical treatment enhances desulfurization performance, while the presence of high concentrations of aromatics reduces efficiency. The study also suggests that surface diffusion is the main mechanism governing the adsorption kinetics.
The scope of this work is the experimental and modeling study of adsorptive deep desulfurization of model fuels utilizing activated carbons. Emphasis is given on how oxidative chemical treatment affects the textural and surface chemistry properties and hence the desulfurization kinetics and performance, while the effect of the copresence of aromatics is also investigated. The derivation of the kinetic model and the understanding of adsorption mechanism(s) are also among the main focuses of the work. Two model solutions, one to mimic gasoline/petrol (DBT in hexane) and another for diesel (4,6-DMDBT in hexadecane), with low initial sulfur concentration (20 ppmwS), as well as a model fuel consisting of 4,6-DMDBT, benzene, and naphthalene in hexadecane mimicking the real diesel fuel, were prepared. Adsorption equilibrium and kinetic experiments were conducted, while the results were fitted by simple empirical models and phenomenological models. Chemical treatment through oxidation enhanced the performance of the carbon, reaching a final concentration of less than 2 ppmwS in the case of DBT in hexane and 7.2 ppmwS for 4,6-DMDBT in hexadecane, thus achieving deep desulfurization. In contrast, the copresence of aromatic compounds in high concentrations decreased the efficiency of the carbons, revealing their competitive character in adsorptive desulfurization. Surface diffusion is considered the main mechanism governing the adsorption kinetics. A strong inhibition in diffusion is observed due to the competitive adsorption/interactions, as well as of the already adsorbed compounds. Interestingly, as regards the DBT/hexane system, the hindrance is so strong that the model has to be replaced by a system of two steps in series having kinetics of quite disparate time scales.

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