1984
DOI: 10.1627/jpi1958.27.533
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Resid FCC reaction model.

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Cited by 18 publications
(15 citation statements)
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“…AncheytaJuarez et al [7] followed a different approach in their 5-lump models development, in which they considered the gas oil as one lump, but divided the gas lump into two lumps (liquefied product gas and dry gas). 6-Lump models were developed by Takatsuka et al [8] (including the resid as a separate lump to predict the catalytic cracking of residual oil), and Oliveira and Biscaia [9] (emphasizing in the catalytic cracking of gasoline and paraffinic gas oils). Hagelberg et al [10] expanded the 5-lump model of Ancheyta-Juarez et al [7] to an 8-lump model by dividing the gasoline fraction into paraffins, olefins, naphthenes and aromatics.…”
Section: Introductionmentioning
confidence: 99%
“…AncheytaJuarez et al [7] followed a different approach in their 5-lump models development, in which they considered the gas oil as one lump, but divided the gas lump into two lumps (liquefied product gas and dry gas). 6-Lump models were developed by Takatsuka et al [8] (including the resid as a separate lump to predict the catalytic cracking of residual oil), and Oliveira and Biscaia [9] (emphasizing in the catalytic cracking of gasoline and paraffinic gas oils). Hagelberg et al [10] expanded the 5-lump model of Ancheyta-Juarez et al [7] to an 8-lump model by dividing the gasoline fraction into paraffins, olefins, naphthenes and aromatics.…”
Section: Introductionmentioning
confidence: 99%
“…Chemical kinetic modeling of the main reactions is used to improve and predict the FCC process [4][5][6]. More or less complex kinetic models have been presented by many researchers, such as Weekman [7], Lee et al [8], Yen et al [9], AncheytaJuarez et al [10], Takatsuka et al [11], Soares Cerqueira et al [12] and others. These models are of equal kinetic importance as the simpler ones, but they are mathematically more complex.…”
Section: Introductionmentioning
confidence: 99%
“…Determination of the velocity constants k j o , j=1,...,3 related to reaction velocity are realized by minimization the following objective function (9) where T j exp represents the experimental riser temperature; T j cal (k 1 o ,k 2 o ,k 3 o ) -the temperature calculated with reactor model, for the same values of input data from experimental set j.…”
Section: Weekman Kinetic Modelmentioning
confidence: 99%
“…Hagelberg expanded this model in a 8-lump model by dividing the gasoline fraction into paraffin's, olefins, naphthenes and aromatics [8]. For the heavy feedstock's Chiyoda Chemical Engineering and Construction Co. have developed a 6-lump kinetic model, where the feedstock have been divided in two components: residue and heavy gasoil, and the reaction products obtained are: light gasoline, gasoline, gases and coke [9]. Some authors have developed more complex kinetic models, such as 10-lump model [10,11], 12-lump model [13], 13-lump model [14], 19-lump model [15].…”
mentioning
confidence: 99%