Modeling of crystallization processes of aviation fuel with different content of aromatic hydrocarbons

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The influence of additives of some organic substances on the crystallization onset temperatures of kerosene fractions (KF) obtained from crude oil (straight-run or SRKF) and in the process of catalytic cracking of heavy oil residues (HKF) is studied by the method of thermodynamic modeling. Normal paraffins CnH2n+2 (n = 9, 11, 16) are used as additives to the KFs, and m-ethylbutylbenzene is used as an aromatic hydrocarbon. It is shown that using the UNIFAC and UNIQUAC models, one can reproduce the experimental data presented in publications and indicating that the addition of normal paraffins to HKF noticeably increases the freezing point when n is 11 and greater. For SRKF, a similar increase occurs starting from n = 16. According to the calculation results, the addition of m-ethylbutylbenzene practically does not affect the crystallization onset temperature.

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作者简介

M. Mamontov

M. V. Lomonosov Moscow State University

编辑信件的主要联系方式.
Email: mmn@td.chem.msu.ru

Department of Chemistry

俄罗斯联邦, Moscow

A. Oshchenko

The 25th State Research Institute of Chemmotology of the Ministry of Defense of Russia

Email: mmn@td.chem.msu.ru
俄罗斯联邦, Moscow

参考

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2. Fig. 1. Freezing temperature of PCF with different amounts of dopants (w – wt. %). Points – experiment [7], lines – calculation (this work). Numbers indicate mixtures with different dopants: (1, ×) – cetane C₁₆H₃₄; (2, ○) – undecane C₁₁H₂₄; (3, ▲) – nonane C₉H₂₀; (4, ■) – m-ethylbutylbenzene C₁₂H₂₈. Line (3) practically merges with line (4) at w < 5 wt. %.

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3. Fig. 2. Freezing temperature of GCF with different amounts of dopants (w – wt. %). Points – experiment [7], lines – calculation (this work). Numbers indicate mixtures with different dopants: (1, ×) – cetane C₁₆H₃₄; (2, ○) – undecane C₁₁H₂₄; (3, ▲) – nonane C₉H₂₀; (4, ■) – m-ethylbutylbenzene C₁₂H₂₈. Line (3) practically merges with line (4) at w < 5 wt. %.

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