Biological and Chemical Reactor Control Opportunities

نویسنده

  • Greg McMillan
چکیده

Biological and chemical process performance is largely determined by reactor performance. The stage for product quality and process efficiency and capacity is set by reaction yield and selectivity. The burden and difficulty for downstream separation and purification processes is minimized by better reactor control. In this tutorial the factors affecting reactor performance are described with examples. For chemical reactors, the general effect on reaction rate of temperature and the concentration of reactant and recycle is described. For biological reactions the effect of pH, temperature, dissolved oxygen, byproduct, substrate, and inhibitor concentration on cell growth rate and product formation rate is discussed. Basic control strategies are discussed for chemical reactions based on liquid and gas phases and for biological reactions based on cell type. Considerations for polymerization reactions are briefly outlined. The relative advantages of cooling and heating control system designs are summarized. Simple translations of variables or additions to the basic control strategies are offered for optimizing production rate. Fed-batch profile opportunities are outlined for chemical and biological reactors for faster and more repeatable batches. The dynamics of reactor response are categorized into three general types. The effect of application dynamics such as process response, controller tuning, noise, and automation system response on the ability of reactor control systems to reach setpoint quickly and reject disturbances is explored. An enhanced PID algorithm developed for wireless measurement and control is explained and the algorithm’s ability to eliminate oscillations from backlash-stiction, large update or sample times, split range discontinuities, and valve position control interactions is discussed. The use of dynamic reset limiting and directional velocity limits for preventing oscillations and safety instrumentation system activation is noted.

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

Poultry Slaughterhouse Wastewater Treatment Using Anaerobic Fluid Bed Reactor and Aerobic Mobile-Bed Biological Reactor

This research evaluated the efficiency of combined anaerobic-aerobic processes for the treatment of slaughterhouse wastewater. The anaerobic reactor consists of a 3.95 L Plexiglas column with 60 mm diameter and 140 cm height. The cylindrical particles of polyvinyl chloride with 2 mm diameter and 1250 kg m-3 density packed to 60 cm of column were used as biomass saving material. The d...

متن کامل

Control of a Chemical Reactor with Chaotic Dynamics

In this paper, control of a non-isothermal continuous stirred tank reactor in which two parallel autocatalytic reactions take place has been addressed. The reactor shows chaotic behavior for a certain set of reactor parameters. In order to control the product concentration, an optimal state feedback controller has been designed. Since concentrations of reactor species are ...

متن کامل

Performance of Biological hydrogen Production Process from Synthesis Gas, Mass Transfer in Batch and Continuous Bioreactors

Biological hydrogen production by anaerobic bacterium, Rhodospirillum rubrum was studied in batch and continuous bioreactors using synthesis gas (CO) as substrate. The systems were operated at ambient temperature and pressure. Correlations available in the literature were used to estimate the gas-liquid mass transfer coefficients (KLa) in batch reactor. Based on experimental results for the con...

متن کامل

Control of a Fluidized Bed Polyethylene Reactor

In present paper, dynamic behavior and control of a fluidized bed reactor for polyethylene production has been considered. A double active sites model for Ziegler-Natta catalysts is used for simulation of polymerization reaction. Hydrodynamic behavior of the bed is modeled using a two phase model including bubble and emulsion phases in which bubble phase has plug flow pattern with different...

متن کامل

Chaos Control in a Non-Isothermal Autocatalytic Chemical Reactor

In this paper, a reaction system consisting of two parallel, non-isothermal autocatalytic reactions in a Continuous Stirred Tank Reactor (CSTR) has been considered. Reactor chaotic behavior is possible for certain values of system parameters. Two types of controllers are designed and compared in order to control both the reactor temperature and the product concentration. T...

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 2011