Title screen

[References: р. 265-266 (36 tit.)]

Mathematical model of diesel fuel hydroisomerization has been developed on the base of the system analysis strategy, which consists of the sequence of the following stages: thermodynamic analysis of chemical reactions possibility, the hydrocarbons conversion scheme drafting, kinetic model development, kinetic parameters estimation by means of inverse kinetic problem solution and large massive of full-scale experimental data and model verification to the real process. Using the developed model, the hydroisomerization process kinetic regularities have been investigated, the temperature influence in the range of 350–410°С, pressure influence within 4.3-9.3 MPa, hydrogen containing gas flow rate influence in the range of 5000–53000 m{3}/h while the feed flow rate is 301 m{3}/h on the product composition have been studied. An optimal technological regime has been determined.