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Consecutive reactions in batch reactor
  Solves numerically and plots the kinetics of given consecutive reactions in a batch reactor
2024.Jul.03 18:18:40
tf, h h (both)† Final reaction time and step size (T). •
T kelvin Reaction temperature. •
ΔT1, ΔT2 kelvin Temperature variations to double the rates. •
y0 (mol/m3) Initial (at time zero) concentrations.
Show values ? Shows the graph coordinates.
  Solves a model of the kinetic behaviour of a system of consecutive reactions, R1, R2, in a batch reactor at constant volume, numerically, via a 4.th order Runge-Kutta method, and plots the four concentrations vs. time.
  From the base data, the rate constants (k1 = 0.01, k2 = 0.02) were made to double when T rises by ΔT1 and ΔT2, respectively. (The system is, thus, quite sensitive to T.)
Suggestions Vary: T by about ± 5 K; reaction time (to get steady state); initial concentrations (eg., 30, 0, 10, 8).
References: Plate: Nauman22T

• Nauman, E. B., 1987, "Chemical reactor design", John Wiley & Sons, Inc., New York, NY (ISBN 0-471-84580-9, Exa. 2.2, p 28).

• "The NIST Reference on constants, units, and uncertainty". (†Units outside the SI: hour, h; minute, min).

• 1795-10-16: Rodrigues, Benjamin Olinde (16-Oct .pdf) (1851-12-17).

 
 
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Created: 2011-10-16 — Last modified: 2017-06-03