QRD Batch Reactor for QR

BATCH REACTOR FOR QR - QRD

創新系統

The Batch Reactor for QR, "QRD", designed by EDIBON, enables the study and kinetic analysis of homogeneous liquid-liquid reactions, as well as the demonstration of adiabatic and isothermal reactions.

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一般說明

The Batch Reactor for QR, "QRD", designed by EDIBON, enables the study and kinetic analysis of homogeneous liquid-liquid reactions, as well as the demonstration of adiabatic and isothermal reactions.

This unit offers a wide range of opportunities for investigating reaction kinetics, ranging from sensor calibration to the formulation of velocity equations and the determination of ionic conductivities. Its ability to operate in both batch and continuous modes facilitates detailed analysis of effects such as mixing, variation of kinetic constants with temperature, and comparison of theoretical and experimental data.

Moreover, the discontinuous reactor is ideal for studying various chemical reactions, such as chemical synthesis, precipitation, neutralization, and oxidation-reduction. It also allows for demonstrating the impact of different reaction parameters, such as reactant concentration, temperature, and reaction time. Especially in adiabatic reactions, where there is no heat transfer with the surroundings, the adiabatic discontinuous reactor ensures ideal conditions for studying reactions in detail.

To work with this reactor, the Base and Service Unit, "QUS", is required, which supplies the necessary reagents and thermostatic water for proper operation.

練習和指導練習

手册中包含的指导实践练习

  1. Determination of the ionic conductivities.
  2. Batch operation. Calculation of the order of the reaction referred to the ethyl-acetate. Initial velocity method.
  3. Batch operation. Determination of the order of the reaction referred to the sodium hydroxide. Initial velocity method.
  4. Batch operation. Determination of the speed constant, the initial concentration of the sodium hydroxide is constant.
  5. Batch operation. Determination of the speed constant, the initial concentration of the ethyl acetate is constant.
  6. Formulation of the speed equation.
  7. Batch operation. Variation of the kinetic constant when the temperature is not constant: Arrhenius equation.
  8. Batch operation. Comparison of the theoretical and the experimental conversion: Deviation from the ideality.
  9. Calculation of the heat transference coefficient of the coil.
  10. Calculation of the hydrolysis reaction enthalpy.
  11. Batch operation. Mixture effects.
  12. Conductivity measurement system: conductimeter.

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