Numerical modelling of raw materials atomization and vaporization in a heat carrier gas flow in technical carbon production based on the Euler approach

¹ LTD “TESIS”, of. 705, 18 Unnatov str., Moscow, 127083, Russia
² Kutateladze Institute of Thermophysics of the Siberian Branch of the Russian Academy of Sciences, 1 Akademik Lavrentyev Ave., Novosibirsk, 630090, Russia
³ LTD «Omsk Carbon Group», 17/1 Pushkina str., Omsk, 644024, Russia

^* Corresponding author: cher@ict.nsc.ru

Abstract

Previously, the authors of this article proposed a 3D Euler-Eulerian model of raw materials spraying and evaporation in the heat-carrier gas flow in the carbon production reactor. The raw materials' droplets fragmentation and evaporation are considered as the carrier and dispersed phase interaction. The continuous phase is a heat carrier gas whose motion is described by the Navier-Stokes equations. Dispersed phase (droplets of raw material and products of its evaporation) motion is described using a non-uniform convective-diffusion equation for the particle concentration. The model was tested with water as a raw material. In this work, hydrocarbons are specified as raw materials. It is proposed next to solve the inverse problem with the target functional providing zero contact of the unevaporated raw materials with the reactor wall. Then the number of solid coke particles in the final product will be minimal. An analysis is made of the unevaporated raw material area sensitivity to the inlet velocity of the heat-carrier gas flow. This parameter has the most impact on the distribution area of the unevaporated raw materials and is assumed to be varied in the optimization problem.