Washout Effects in Pumped Tank Reactors

نویسنده

  • Kenneth Showalter
چکیده

Studies of multiple steady states in continuous-flow stirred tank reactors (CSTR) typically depend on the systematic variation of reactor residence time or some other system constraint such as reactant concentration. The concentration of an intermediate species is usually monitored as a function of time at a particular residence time until a steady state is established; the flow rate is then changed to give a new residence time and the next steady state concentration is determined. At short reactor residence times, the reaction mixture composition approaches the composition of the combined reactant streams; a t long residence times, the composition approaches that corresponding to a batch reaction at thermodynamic equilibrium. For most chemical reactions, the steady-state concentration of a particular species is a continuous, smooth function of residence time between the extremes of zero and infinity. However, in a number of autocatalytic reactions,1-8 the branch of steady states asymptotic to the reactant stream composition and the branch asymptotic to the equilibrium composition do not connect in a continuous fashion, but instead overlap one another. Thus, when a system constraint such as residence time is varied, a hysteresis effect is observed as the system moves from one branch of steady states to the other and back again. The system may exist in either of two steady states in the overlap region, Le., the system is bistable. The familiar pattern of steady-state multiplicity is dramatically altered when a minor modification is made in pumping the CSTR. A simple model system recently proposed by Gray and Scott,9 which combines third-order autocatalysis with a first-order decay of the autocatalytic species, exhibits a second hysteresis region and may even give rise to an isolated branch of steady states. We recognized that a first-order decay of all species in a tank reactor can be provided by supplying a constant flux of solvent to the CSTR in addition to the flux of reagents.lo In addition, the bistable iodate-arsenous acid reaction exhibits third-order autocatalysisll and, therefore, is an ideal chemical system for testing the model predictions. In this communication we report the first experimental characterization of a mushroom (two connected

برای دانلود متن کامل این مقاله و بیش از 32 میلیون مقاله دیگر ابتدا ثبت نام کنید

ثبت نام

اگر عضو سایت هستید لطفا وارد حساب کاربری خود شوید

منابع مشابه

Modeling, simulation, and optimization of bacterial leaching reactors.

Bacterial leaching represents an unusual problem in biochemical engineering, because the substrate for bacterial growth is not supplied directly, but is a product of another reaction, the leaching of mineral particles. In addition, leaching is a heterogeneous reaction dependent on the particle-size distribution in the feed and on the kinetics of particle shrinkage. In this study, these effects ...

متن کامل

CFD Modeling of Gas-Liquid Hydrodynamics in a Stirred Tank Reactor

Multiphase impeller stirred tank reactors enhance mixing of reacting species used in a variety of chemical industries. These reactors have been studied based on Computational Fluid Dynamics (CFD) that can be used in the analysis, design and scale up of these reactors. Most of the researches done in this area are limited to single phase reactors, and a few remaining two phase flow investigat...

متن کامل

The microbiology of biomining: development and optimization of mineral-oxidizing microbial consortia.

Biomining, the use of micro-organisms to recover precious and base metals from mineral ores and concentrates, has developed into a successful and expanding area of biotechnology. While careful considerations are made in the design and engineering of biomining operations, microbiological aspects have been subjected to far less scrutiny and control. Biomining processes employ microbial consortia ...

متن کامل

Chemicals from CO2: Hydrogenotrophic production of acetate with Acetobacterium woodii

The formation of acetate by Acetobacterium woodii was studied systematically in batch-operated stirred-tank reactors at different hydrogen and carbon dioxide partial pressures in the gas phase. 48 parallel stirred-tank reactors on a millilitre-scale as well as stirred-tank reactors on a litre-scale were applied for the detailed reaction engineering analysis of hydrogenotrophic acetate formation...

متن کامل

Optimizing Bioreactors by Extremum Seeking

The optimization of the operation of biological reactors is an interesting non-linear problem whose solution o!ers potential economic bene"t. We apply a peak seeking method to approach the maximum biomass production rate in a continuous stirred tank bioreactor. Two models, Monod and Haldane, are investigated and it is shown by simulation that the peak seeking scheme achieves optimization for bo...

متن کامل

ذخیره در منابع من


  با ذخیره ی این منبع در منابع من، دسترسی به آن را برای استفاده های بعدی آسان تر کنید

برای دانلود متن کامل این مقاله و بیش از 32 میلیون مقاله دیگر ابتدا ثبت نام کنید

ثبت نام

اگر عضو سایت هستید لطفا وارد حساب کاربری خود شوید

عنوان ژورنال:

دوره   شماره 

صفحات  -

تاریخ انتشار 2001