QRQC Trainingssystem für Chemiereaktoren, computergesteuert:

11.2.- CHEMISCHE REAKTOREN
COMPUTER CONTROLLED CHEMICAL REACTORS TRAINING SYSTEM - QRQC
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BASE-SERVICE UNIT - QRUBI|
  • QRUBI
Available
11.2.- CHEMISCHE REAKTOREN
QRUBI

Grund- und Dienstgerät. (computergesteuert)

This unit is common for the Chemical Reactors and can work with one or several reactors. Installation and exchange system of the reactors quick and easy to handle. It supplies all the services for the operation of each reactor. Anodized aluminum...
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ÜBUNGEN UND GEFÜHRTE PRAKTIKEN

GEFÜHRTE PRAKTISCHE ÜBUNGEN IM HANDBUCH ENTHALTEN

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.
Mehr sehen

MEHR PRAKTISCHE ÜBUNGEN FÜR DAS GERÄT

  1. Many students view results simultaneously.
    2. 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.
    3. 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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