Influence of pressure on the deep removal of sulfur and aromatics from cracked diesel fraction over hydrocracking catalyst

Result code in IS VaVaI

<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F62243136%3A_____%2F14%3AMPO16SB" target="_blank" >RIV/62243136:_____/14:MPO16SB - isvavai.cz</a>

Result on the web

<a href="http://www.icct.cz/proceedings/2014/Full_Papers_ICCT_2014.pdf" target="_blank" >http://www.icct.cz/proceedings/2014/Full_Papers_ICCT_2014.pdf</a>

DOI - Digital Object Identifier

—

Result language

čeština

Original language name

Influence of pressure on the deep removal of sulfur and aromatics from cracked diesel fraction over hydrocracking catalyst

Original language description

The consumption of diesel fuel is increasing and the quality requirements (i.e. content of sulfur and aromatics) are becoming stricter. The secondary processes for deeper conversion of crude oil produce wide spectra of middle distillates. These fractionsdo not reach quality of the primary (straight-run) products from crude oil distillation. They contain higher levels of sulfur, nitrogen and aromatic compounds with lower activity in hydrorefining. The possibility of using the secondary distillates in the production of high quality diesel fuel (EN-590) on the existing hydrodesulfurization (HDS) catalysts is limited. The investigation was focused on the possibility of deep removal of sulfur and aromatics from secondary middle distillates using hydrocracking (HCK) process. The process was tested on continuous pilot plant unit with commercial HCK catalyst. The feedstock was a mixture of straight-run distillate having 25 wt. % secondary middle distillates (light cycle oil from FCC (LCO), ga

Czech name

Influence of pressure on the deep removal of sulfur and aromatics from cracked diesel fraction over hydrocracking catalyst

Czech description

The consumption of diesel fuel is increasing and the quality requirements (i.e. content of sulfur and aromatics) are becoming stricter. The secondary processes for deeper conversion of crude oil produce wide spectra of middle distillates. These fractionsdo not reach quality of the primary (straight-run) products from crude oil distillation. They contain higher levels of sulfur, nitrogen and aromatic compounds with lower activity in hydrorefining. The possibility of using the secondary distillates in the production of high quality diesel fuel (EN-590) on the existing hydrodesulfurization (HDS) catalysts is limited. The investigation was focused on the possibility of deep removal of sulfur and aromatics from secondary middle distillates using hydrocracking (HCK) process. The process was tested on continuous pilot plant unit with commercial HCK catalyst. The feedstock was a mixture of straight-run distillate having 25 wt. % secondary middle distillates (light cycle oil from FCC (LCO), ga

Type

D - Article in proceedings

CEP classification

CI - Industrial chemistry and chemical engineering

OECD FORD branch

—

Project

—

Continuities

I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace

Publication year

2014

Confidentiality

S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Article name in the collection

Proceedings of the 2nd international conference on chemical technology

ISBN

978-80-86238-64-7

ISSN

—

e-ISSN

—

Number of pages

5

Pages from-to

124-128

Publisher name

Česká společnost průmyslové chemie a Česká společnost chemická

Place of publication

Praha

Event location

Mikulov

Event date

Jan 1, 2014

Type of event by nationality

EUR - Evropská akce

UT code for WoS article

—