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Kinetic parameters of five lump model were tuned with industrial data.
Next, a simplified lump model is derived that is suitable for the observer design.
The ability of the model in simulation of complex hydrological processes with GIS interface has created priorities for it in using relevant lump model for hydrological components simulation (Akbari 2010).
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Four and ten lump models were used for simulating cracking reactions.
On the basis of the scaling relations (5)–(17) and the lumping approach, parameters of the lumped model were given as where the sum is taken over all tissues that are grouped together in the lumped compartment 'L'.
A 6-lump model was used for product characterization.
In the sequential approach, the kinetic parameters have been estimated for a 3-lump model, and then the information is used to estimate the 4-lump parameters using a 4-lump model.
Finally, the kinetic constants obtained from 4-lump are used to estimate the kinetic parameters for 5-lump model.
The kinetic constants, related to an eight-lump model, were calculated based on a reactor model which intrinsically includes the effect of molar expansion during cracking.
A new method is proposed to determine the fluid catalytic cracking catalyst deactivation and kinetic parameters of a 6-lump model of catalytic cracking, using few microactivity test (MAT) experiments.
A 5-lump model, derived from 3- and 4-lumps, is used to represent the experimental data and used to estimate the kinetic constants and hence the yields of gasoline, LPG, dry gases, coke and feedstocks.
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