QRQC Système d'Entrainement de Réacteurs Chimiques, Contrôlé par Ordinateur (PC)

COMPUTER CONTROLLED CHEMICAL REACTORS TRAINING SYSTEM - QRQC

SYSTEMES INNOVANTS

The Computer Controlled Chemical Reactors Training System, "QRQC", has been designed by EDIBON for the study and comparison of different types of chemical reactors.

Voir description générale

Description Générale

The Computer Controlled Chemical Reactors Training System, "QRQC", has been designed by EDIBON for the study and comparison of different types of chemical reactors.

The minimum supply consists of two main elements: the Base Service Unit, "QRUBI", and at least one of the required elements described below.

The Base Service Unit, "QRUBI", provides the necessary elements for the operation of the different reactor modules.

It performs the following functions:

  • Reagent supply: consisting of two glass tanks, two dosing pumps and all the necessary connections.
  • Temperature control: consisting of a thermostatic bath and an impulsion pump.
  • Product collection system: allows the products obtained in the reactors to be quickly and easily conveyed to the base module and deposited in the corresponding tank.
  • Reaction monitoring system: this consists of a conductivity cell and a conductivity meter installed on the front panel of the base module.

Accessoires

Des exercices et pratiques guidées

EXERCICES GUIDÉS INCLUS DANS LE MANUEL

Practices to be done with the Isothermal Reactor with Stirrer (QRIA):

  1. Determining the ionic conductivities.
  2. Batch operation. Obtaining the reaction order with respect to the ethyl acetate. Method of initial rates.
  3. Batch operation. Obtaining the reaction order with respect to the sodium hydroxide. Method of initial rates.
  4. Batch operation. Calculation of the rate constant. Constant sodium hydroxide initial concentration.
  5. Batch operation. Calculation of the rate constant. Constant ethyl acetate initial concentration.
  6. Rate equation formulation.
  7. Batch operation. Variation of the kinetic constant with temperature. Arrhenius equation.
  8. Batch operation. Theoretical and experimental conversion comparison. Deviation from ideality.
  9. Batch operation. Mixture effects.
  10. Continuous operation.
  11. Continuous operation. Mixture effects.
  12. Sensors calibration.

Practices to be done with Isothermal Reactor with Distillation (QRIA/D):

  1. Determination of the ionic conductivities.
  2. Batch operation. Obtaining the reaction order with respect to the ethyl acetate. Method of initial rates.
  3. Batch operation. Obtaining the reaction order with respect to the sodium hydroxide. Method of initial rates.
  4. Batch operation. Calculation of the rate constant. Constant sodium hydroxide initial concentration.
  5. Batch operation. Calculation of the rate constant. Constant ethyl acetate initial concentration.
  6. Rate equation formulation.
  7. Batch operation. Variation of the kinetic constant with temperature. Arrhenius equation.
  8. Batch operation. Theoretical and experimental conversion comparison. Deviation from ideality.
  9. Batch operation. Mixture effects.
  10. Continuous operation.
  11. Continuous operation. Mixture effects.
  12. Sensors calibration.

Practices to be done with the Tubular Flow Reactor (QRFT):

  1. Determination of the ionic conductivities.
  2. Theoretical conversion of the tubular reactor.
  3. Experimental determination of the tubular reactor conversion.
  4. Dependence on the residence time.
  5. Determination of the reaction order.
  6. Dependence of the rate constant and the conversion with the temperature.
  7. Sensors calibration.

Practices to be done with the Adiabatic and Isothermal Reactor (QRAD):

  1. Determination of the ionic conductivities.
  2. Batch operation. Obtaining the reaction order with respect to the ethyl acetate. Method of initial rates.
  3. Bach operation. Obtaining the reaction order with respect to the sodium hydroxide. Method of initial rates.
  4. Batch operation. Calculation of the rate constant. Constant sodium hydroxide initial concentration.
  5. Batch operation. Calculation of the rate constant. Constant ethyl acetate initial concentration.
  6. Rate equation formulation.
  7. Batch operation. Variation of the kinetic constant with temperature. Arrhenius equation.
  8. Batch operation. Theoretical and experimental conversion comparison. Deviation from ideality.
  9. Batch operation. Effect of concentration on conversion.
  10. Calculation of the heat transfer coefficient of the coil.
  11. Batch operation. Mixing effects.
  12. Continuous operation.
  13. Sensors calibration.

Practices to be done with the Reactors with Stirrer in Series (QRSA):

  1. Determination of the ionic conductivities.
  2. Continuous operation with only one reactor.
  3. Continuous operation with only one reactor with mixture effects.
  4. Continuous operation with the three reactors.
  5. Sensors calibration.
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PLUS D'EXERCICES PRATIQUES À EFFECTUER AVEC CETTE ÉQUIPEMENT

  1. Many students view results simultaneously. To view all results in real time in the classroom by means of a projector or an electronic whiteboard.
  2. Open Control, Multicontrol and Real Time Control. This unit allows intrinsically and/or extrinsically to change the span, gains, proportional, integral, derivate parameters, etc, in real time.
  3. The Computer Control System with SCADA and PID Control allow a real industrial simulation.
  4. This unit is totally safe as uses mechanical, electrical and electronic, and software safety devices.
  5. This unit can be used for doing applied research.
  6. This unit can be used for giving training courses to Industries even to other Technical Education Institutions.
  7. Control of the unit process through the control interface box without the computer.
  8. Visualization of all the sensors values used in the unit process.
  9. By using PLC-PI additional 19 more exercises can be done.
  10. Several other exercises can be done and designed by the user.

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