Industrial hydrocracker model based on novel continuum lumping approach for optimization in petroleum refinery

Basak, Kaushik; Sau, M.; Manna, Ujjwal; Verma, Ritu

doi:10.1016/j.cattod.2004.07.056

Cited by 43 publications

(27 citation statements)

References 22 publications

Supporting

Mentioning

Contrasting

Order By: Relevance

“…However, these are catalyst dependent. The methodology for estimation has already been published (Basak et al [12]). The model tuning parameters for the present study is given in Table 2.…”

Section: Application Of Model For Prediction Of Vgo Hydrocracking Expmentioning

confidence: 99%

Effects of organic nitrogen compounds on hydrotreating and hydrocracking reactions

Basak

Manna

et al. 2005

Catalysis Today

Self Cite

View full text Add to dashboard Cite

“…However, these are catalyst dependent. The methodology for estimation has already been published (Basak et al [12]). The model tuning parameters for the present study is given in Table 2.…”

Section: Application Of Model For Prediction Of Vgo Hydrocracking Expmentioning

confidence: 99%

Effects of organic nitrogen compounds on hydrotreating and hydrocracking reactions

Basak

Manna

et al. 2005

Catalysis Today

Self Cite

View full text Add to dashboard Cite

“…Different kinetic approaches have been reported in the literature for the hydrocracking of oil fractions (lumping approach, continuous kinetics lumping, single event model) [1][2][3][4][5][6][7][8], but only a few deal with the hydrocracking of heavy oil. Because vacuum gas oil has been mostly used as feed, catalyst deactivation has been neglected.…”

Section: Introductionmentioning

confidence: 99%

Kinetic model for hydrocracking of heavy oil in a CSTR involving short term catalyst deactivation

Martínez

Ancheyta

2012

Fuel

View full text Add to dashboard Cite

“…However, if SR l and SR h have complementary advantage, the corresponding match flow rate can be calculated according to the impurity concentration constraints shown by Equation (4).…”

Section: Maximum Match Flow Rate Matrixmentioning

confidence: 99%

An extended evolutionary design method for the optimization of hydrogen networks with pressure constraint

Jia

Liu

et al. 2015

Can J Chem Eng

View full text Add to dashboard Cite

In this work, the evolutionary method is extended to the work utility consumption and the capital cost of compressors incorporated with fresh hydrogen consumption in the optimization of hydrogen networks. The total cost matrix (TC matrix) is constructed with the cost of each possible match calculated. Further, the minimum total cost rule is proposed to compare different sources that can match the same sink. Based on this, the potential match matrix (P matrix) and the optimal match matrix (O matrix) can be determined sequentially. The fresh hydrogen, work utility consumption, total cost, and corresponding hydrogen distribution network can be obtained from the O matrix. The hydrogen network of a real refinery is studied to demonstrate the application of the extended evolutionary method. The results show that total cost determined by the extended method is 3.32 % less than that identified by the original evolutionary method, and the same as that calculated by the mathematical programming method.

show abstract

Industrial hydrocracker model based on novel continuum lumping approach for optimization in petroleum refinery

Cited by 43 publications

References 22 publications

Effects of organic nitrogen compounds on hydrotreating and hydrocracking reactions

Effects of organic nitrogen compounds on hydrotreating and hydrocracking reactions

Kinetic model for hydrocracking of heavy oil in a CSTR involving short term catalyst deactivation

An extended evolutionary design method for the optimization of hydrogen networks with pressure constraint

Contact Info

Product

Resources

About