Mathematical model of straight run diesel catalytic hydroisomerization

Research output: Chapter in Book/Report/Conference proceedingConference contribution

14 Citations (Scopus)

Abstract

Straight run diesel catalytic hydroisomerization mathematical model has been developed. There are the following steps for sequential accomplishment: assessment of thermodynamic possibility of spontaneous reactions under the existing technological conditions, development and formalization of hydrocarbon reaction network scheme, kinetic parameters evaluation, industrial verification of the model. The temperature impact within 345-405°C, the pressure impact in the range of 5-8 MPa and hydrogen bearing gas consumption impact within 3000-51000 m 3/h on higher molecular n-alkanes conversion and i-alkanes yield as the basic components which determine diesel fuels low-temperature characteristics to the fullest extent, have been investigated using the developed model. It has been revealed that hydroisomerization process ought to be carried out under such temperature and pressure which do not lead to catalyst exploitation properties come-down in order to receive the product with the required low temperature characteristics. They are 355°C and 6,7 MPa. The optimal hydrogen bearing gas consumption has been adopted as 39000 m 3/h when the feed flow rate is 301 m 3/h.

Original languageEnglish
Title of host publicationIOP Conference Series: Earth and Environmental Science
PublisherInstitute of Physics Publishing
Volume21
Edition1
DOIs
Publication statusPublished - 2014
Event18th International Scientific Symposium in Honour of Academician M. A. Usov: Problems of Geology and Subsurface Development, PGON 2014 - Tomsk, Russian Federation
Duration: 7 Apr 201411 Apr 2014

Other

Other18th International Scientific Symposium in Honour of Academician M. A. Usov: Problems of Geology and Subsurface Development, PGON 2014
CountryRussian Federation
CityTomsk
Period7.4.1411.4.14

Fingerprint

diesel
alkane
hydrogen
gas
thermodynamics
temperature
catalyst
hydrocarbon
kinetics
consumption
parameter
evaluation
product
rate
diesel fuel

ASJC Scopus subject areas

  • Earth and Planetary Sciences(all)
  • Environmental Science(all)

Cite this

Belinskaya, N. S., Ivanchina, E., Ivashkina, E., Frantsina, E., & Silko, G. Y. (2014). Mathematical model of straight run diesel catalytic hydroisomerization. In IOP Conference Series: Earth and Environmental Science (1 ed., Vol. 21). [012030] Institute of Physics Publishing. https://doi.org/10.1088/1755-1315/21/1/012030

Mathematical model of straight run diesel catalytic hydroisomerization. / Belinskaya, Nalaliya Sergeevna; Ivanchina, E.; Ivashkina, E.; Frantsina, E.; Silko, Galina Yurievna.

IOP Conference Series: Earth and Environmental Science. Vol. 21 1. ed. Institute of Physics Publishing, 2014. 012030.

Research output: Chapter in Book/Report/Conference proceedingConference contribution

Belinskaya, NS, Ivanchina, E, Ivashkina, E, Frantsina, E & Silko, GY 2014, Mathematical model of straight run diesel catalytic hydroisomerization. in IOP Conference Series: Earth and Environmental Science. 1 edn, vol. 21, 012030, Institute of Physics Publishing, 18th International Scientific Symposium in Honour of Academician M. A. Usov: Problems of Geology and Subsurface Development, PGON 2014, Tomsk, Russian Federation, 7.4.14. https://doi.org/10.1088/1755-1315/21/1/012030
Belinskaya NS, Ivanchina E, Ivashkina E, Frantsina E, Silko GY. Mathematical model of straight run diesel catalytic hydroisomerization. In IOP Conference Series: Earth and Environmental Science. 1 ed. Vol. 21. Institute of Physics Publishing. 2014. 012030 https://doi.org/10.1088/1755-1315/21/1/012030
@inproceedings{385d3d535d5f4a93b1977420263175e1,
title = "Mathematical model of straight run diesel catalytic hydroisomerization",
abstract = "Straight run diesel catalytic hydroisomerization mathematical model has been developed. There are the following steps for sequential accomplishment: assessment of thermodynamic possibility of spontaneous reactions under the existing technological conditions, development and formalization of hydrocarbon reaction network scheme, kinetic parameters evaluation, industrial verification of the model. The temperature impact within 345-405°C, the pressure impact in the range of 5-8 MPa and hydrogen bearing gas consumption impact within 3000-51000 m 3/h on higher molecular n-alkanes conversion and i-alkanes yield as the basic components which determine diesel fuels low-temperature characteristics to the fullest extent, have been investigated using the developed model. It has been revealed that hydroisomerization process ought to be carried out under such temperature and pressure which do not lead to catalyst exploitation properties come-down in order to receive the product with the required low temperature characteristics. They are 355°C and 6,7 MPa. The optimal hydrogen bearing gas consumption has been adopted as 39000 m 3/h when the feed flow rate is 301 m 3/h.",
author = "Belinskaya, {Nalaliya Sergeevna} and E. Ivanchina and E. Ivashkina and E. Frantsina and Silko, {Galina Yurievna}",
year = "2014",
doi = "10.1088/1755-1315/21/1/012030",
language = "English",
volume = "21",
booktitle = "IOP Conference Series: Earth and Environmental Science",
publisher = "Institute of Physics Publishing",
edition = "1",

}

TY - GEN

T1 - Mathematical model of straight run diesel catalytic hydroisomerization

AU - Belinskaya, Nalaliya Sergeevna

AU - Ivanchina, E.

AU - Ivashkina, E.

AU - Frantsina, E.

AU - Silko, Galina Yurievna

PY - 2014

Y1 - 2014

N2 - Straight run diesel catalytic hydroisomerization mathematical model has been developed. There are the following steps for sequential accomplishment: assessment of thermodynamic possibility of spontaneous reactions under the existing technological conditions, development and formalization of hydrocarbon reaction network scheme, kinetic parameters evaluation, industrial verification of the model. The temperature impact within 345-405°C, the pressure impact in the range of 5-8 MPa and hydrogen bearing gas consumption impact within 3000-51000 m 3/h on higher molecular n-alkanes conversion and i-alkanes yield as the basic components which determine diesel fuels low-temperature characteristics to the fullest extent, have been investigated using the developed model. It has been revealed that hydroisomerization process ought to be carried out under such temperature and pressure which do not lead to catalyst exploitation properties come-down in order to receive the product with the required low temperature characteristics. They are 355°C and 6,7 MPa. The optimal hydrogen bearing gas consumption has been adopted as 39000 m 3/h when the feed flow rate is 301 m 3/h.

AB - Straight run diesel catalytic hydroisomerization mathematical model has been developed. There are the following steps for sequential accomplishment: assessment of thermodynamic possibility of spontaneous reactions under the existing technological conditions, development and formalization of hydrocarbon reaction network scheme, kinetic parameters evaluation, industrial verification of the model. The temperature impact within 345-405°C, the pressure impact in the range of 5-8 MPa and hydrogen bearing gas consumption impact within 3000-51000 m 3/h on higher molecular n-alkanes conversion and i-alkanes yield as the basic components which determine diesel fuels low-temperature characteristics to the fullest extent, have been investigated using the developed model. It has been revealed that hydroisomerization process ought to be carried out under such temperature and pressure which do not lead to catalyst exploitation properties come-down in order to receive the product with the required low temperature characteristics. They are 355°C and 6,7 MPa. The optimal hydrogen bearing gas consumption has been adopted as 39000 m 3/h when the feed flow rate is 301 m 3/h.

UR - http://www.scopus.com/inward/record.url?scp=84906956937&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=84906956937&partnerID=8YFLogxK

U2 - 10.1088/1755-1315/21/1/012030

DO - 10.1088/1755-1315/21/1/012030

M3 - Conference contribution

VL - 21

BT - IOP Conference Series: Earth and Environmental Science

PB - Institute of Physics Publishing

ER -