2015
DOI: 10.1016/j.cej.2015.02.036
|View full text |Cite
|
Sign up to set email alerts
|

Decreasing the hydrogen-rich gas circulation ratio and service life extension of the C9–C14 alkanes dehydrogenation catalyst

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1

Citation Types

0
8
0

Year Published

2015
2015
2021
2021

Publication Types

Select...
8

Relationship

3
5

Authors

Journals

citations
Cited by 14 publications
(8 citation statements)
references
References 25 publications
0
8
0
Order By: Relevance
“…Mathematical model for calculation and optimization of catalytic cracking is based on the multistage and hierarchical approach to the mathematical models construction [34][35][36][37]. The essence of the hierarchical approach of the mathematical description synthesis means that the mathematical description of each subsequent structural level should be included as a main part in the mathematical description of the last level ( Fig.…”
Section: The Mathematical Modelmentioning
confidence: 99%
“…Mathematical model for calculation and optimization of catalytic cracking is based on the multistage and hierarchical approach to the mathematical models construction [34][35][36][37]. The essence of the hierarchical approach of the mathematical description synthesis means that the mathematical description of each subsequent structural level should be included as a main part in the mathematical description of the last level ( Fig.…”
Section: The Mathematical Modelmentioning
confidence: 99%
“…The method of mathematical modelling is widely used to study, improve, optimize and forecast the processes of petroleum refining industry [4][5][6][7][8][9][10][11][12][13][14].…”
Section: Methodsmentioning
confidence: 99%
“…The task of controlling the activity of the catalyst of higher n-alkanes dehydrogenation process, with the purpose of increasing target product yield at the hydrogen/feedstock molar ratio of 6/1 and increasing the catalyst service life was solved in the following way: using the developed mathematical model of dehydrogenation process [26], considering coke generating from aromatic and diene hydrocarbons, and oxidizing of coke compounds by water vapour, the rate of coke generating on the catalyst coating is found:…”
Section: Methodsmentioning
confidence: 99%
“…Taking into account the specific character of the dehydrogenation reaction, the process is better to be kept at lower pressure, which is formed exactly by ratio hydrogen/feedstock. After decreasing molar ratio, the increase in the target product -alkenes -is observed; however, along with that, the decreasing rate of hydrogenation by-products by hydrogen and, as a result, the increasing rate of catalyst dehydrogenation by coke is observed [21][22][23][24][25][26].…”
Section: Introductionmentioning
confidence: 93%