Comments on the behaviour of a fixed-bed reactor
ثبت نشده
چکیده
Dear Sirs, In a recent series co-workers (see e.g. of papers by Morbidelli and Varma and Morbidelli and Varma 1986a; Morbidelli et al., 1986h Lee and Varma, 1987, 1988; Bauman and Varma 1990), the multiplicity behaviour of a fixed bed reactor is discussed. The basis for this analysis was given by Morbidelli and Varma (1986a) and Morbid& et al. (1986b), where the authors devote many columns to mathematically prove, by means of “a rigorous application of the Implicit Function Theorem”, that the multiplicity of a heterogeneous plug Row packed bed reactor is fully determined by the multiplicity of the inlet particle. Thus, according to Morbidelli et al., this model even in its basic form, does not exhibit an infinite number of steady states, a property referred to as infinite multiplicity (Liu and Amundson, 1962; Eigenberger, 1972). Eigenbcrger (1972) showed quantitatively that infinite multiplicity will not occur if axial dispersion of heat is present. Morbidelli et al. claim that they have proven that, in order to exclude infinite multiplicity, it is not necessary to take into account axial dispersion. We will show that their proof is incorrect and that the modelling equations of the heterogeneous plug flow reactor without thermal axial dispersion do have an infinite number of steady-state solutions. The notation and the equations can be found in Morbidelli and Varma (1986a). The solution of the heterogeneous plug flow model involves the integration of an ordinary differential equation, eq. (7), where at each step in the integration, the non-linear constraint eq. (l’lt_representing the state of the particles needs to be solved to yield OP. As is well known, there can be either one or two stable solutions for this constraint. If the particles operate in the multiplicity region, then there are two possible solutions for the constraint eq. (17). In each step of the integration we must choose between these two solutions. In other words, we must choose the particle to be either in the lower or in the higher state and during the integration we must make this choice for each individual particle over and over again. Now, according to Morbidelli et al. we cannot choose arbitrarily between these two states. They concluded this from the following statement: “from the implicit function theorem it can be seen that the obtained solution of eq. (17) is unique and continuous as long as the following condition is satisfied: (Received 30 August 1990; accepted 23 April 1991)
منابع مشابه
CFD Simulation of Dimethyl Ether Synthesis from Methanol in an Adiabatic Fixed-bed Reactor
A computational fluid dynamic (CFD) study of methanol (MeOH) to dimethyl ether (DME) process in an adiabatic fixed-bed reactor is presented. One of the methods of industrial DME production is the catalytic dehydration of MeOH. Kinetic model was derived based on Bercic rate. The parameters of this equation for a specific catalyst were tuned by solving a one-dimensional homogenous model using MAT...
متن کاملV2O5-MoO3 Catalysts Preparation and Performance Testing on the Oxidation of Benzene to Maleic Anhydride in a Fixed Bed Reactor
In this research, the selective oxidation of benzene to maleic anhydride (MAN) in a fixed-bed reactor was studied. The gas phase catalytic oxidation of benzene was carried outin a laboratory scale fixed bed reactor on the catalysts, which were prepared having two different compositions on silica gel. The effects of temperature, flow rates of benzene and air, and catalyst type on the reactio...
متن کاملModeling and Simulation a Catalytic Fixed Bed Reactor to Produce Ethyl Benzene from Ethanol
Ethyl benzene used increasingly each year is the raw material of producing styrene monomer. This substanceis produced from benzene alkylation with ethylene or ethanol, depending on the availability and cost of rawmaterials. In this study benzene alkylation in the presence of ethanol in a catalytic fixed bed reactor inthree states of isotherm, adiabatic and non-isotherm-non-adiabatic is mathemat...
متن کاملSimulation and Control of a Methanol-To-Olefins (MTO) Laboratory Fixed-Bed Reactor
In this research, modeling, simulation, and control of a methanol-to-olefins laboratory fixed-bed reactor with electrical resistance furnace have been investigated in both steady-state and dynamic conditions. The reactor was modeled as a one-dimensional pseudo-homogeneous system. Then, the reactor was simulated at steady-state conditions and the effect of different parameters including...
متن کاملEffect of the chemical nature of fixed-bed reactor support materials on bioreactor performance and biomass accumulation
This study investigated the effect, on reactor performance and biomass retention inside the bed, of the material used to make the supports of anaerobic fixed-bed reactors. Three inert supports of similar shape but made of three different materials polyvinyl chloride, polypropylene, high-density polyethylene were manufactured and used. All three supports had the same specific surface area but di...
متن کاملMathematical modeling of a fixed bed chromatographic reactor for Fischer Tropsch synthesis
In this research, Fischer Tropsch synthesis (FTS) has been modeled in the fixed bed chromatographic reactor for the first time by applying a rather complex dispersed plug flow model for fluid phase and linear driving force (LDF) model for adsorbent. Model equations are dynamic, multi-component, non-linear and heterogeneous including reaction and adsorption simultaneously Complex kinetics fo...
متن کامل