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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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PP-III-46MATHEMATICAL MODELLING OF A CO-CURRENT REACTORI.S. VerzhbitskayaAl-Farabi Kazakh National University, 71 Al-Farabi st., Almaty 050078, Kazakhstan,fax: +7(727) 247-26-09, e-mail: i_verb@mail.ruThis paper deals with ma<strong>the</strong>matical modeling <strong>of</strong> a cooled catalytic fixed-bed reactorwhere single exo<strong>the</strong>rmic reaction occurs. An important class <strong>of</strong> reactors is that for which <strong>the</strong>wall temperature is not constant but varies along reactor length. Such is <strong>the</strong> case when <strong>the</strong>cooling tubes and reactor tubes form an integral part <strong>of</strong> a composite heat exchanger. In thisstudy co-current flow <strong>of</strong> coolant and reaction mixture is considered. It is assumedinstantaneous heat transfer between <strong>the</strong> solid catalyst and <strong>the</strong> reacting gas mixture, constan<strong>the</strong>at-physical properties and negligible diffusivity inside catalyst pellets. The heat and masstransfer resistance through <strong>the</strong> packing and gas mixture inside <strong>the</strong> bed are described by <strong>the</strong>effective coefficients <strong>of</strong> conductivity and diffusivity. Reaction rate varies with temperature byArrhenius law. With <strong>the</strong>se assumptions a two-dimensional pseudo homogeneous model <strong>of</strong>heat and mass transfer was used. The partial differential equations (PDE) involve threedecision variables (coolant temperature, gas mixture temperature and concentration), whichvary on time and along two space coordinates.Due to high non-linearity and major number <strong>of</strong> system parameters <strong>of</strong> <strong>the</strong>se equations <strong>the</strong>problem can only be solved in this form by numerical techniques. In order to obtain a preview<strong>of</strong> possible dynamics and initial guesses for computations it is necessary to simplify <strong>the</strong>problem and give equations which can be solved analytically. For that <strong>the</strong> set <strong>of</strong> PDE wasconverted to ordinary differential equations (ODE) by discretization <strong>of</strong> <strong>the</strong> spatial derivativeswith finite differences. Then <strong>the</strong> resultant ODE system (<strong>the</strong> dynamical system <strong>of</strong> <strong>the</strong> 3 rd order)was used for finding steady states and periodic solutions, determining <strong>the</strong>ir local stability andbifurcation points. By applying <strong>the</strong> methods <strong>of</strong> bifurcation <strong>the</strong>ory [1] <strong>the</strong> analyticalexpressions for bifurcation diagram and non-unique boundary were obtained. It was foundthat <strong>the</strong> system can possess from 1 to 3 different equilibrium states. One equilibrium staterepresents a meta-stable and <strong>the</strong> remaining two states correspond to high- or low-temperatureregime, depending on initial conditions. The stability <strong>of</strong> steady states was investigated on <strong>the</strong>basis <strong>of</strong> linear approximation <strong>of</strong> simplified model by applying <strong>the</strong> 1 st Lyapunov method andRouth-Hurwitz stability criterion [1]. The parametric equations <strong>of</strong> stability boundaries in <strong>the</strong>plane «inlet gas temperature»(ϑ 0 ) – «reaction heat»(q) were obtained. These boundariesdivide <strong>the</strong> parametric plane ϑ 0 ,q into 6 regions with different type <strong>of</strong> stability and number <strong>of</strong>389

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