Extraction of light gas oil from catalytic cracking with alkylcarbamate

1971 ◽  
Vol 7 (3) ◽  
pp. 187-191
Author(s):  
T. P. Vishnyakova ◽  
V. V. Zamanov ◽  
G. S. Kaganer ◽  
A. A. Drichko ◽  
A. I. Mezhlumova ◽  
...  
Keyword(s):  
Catalytic Cracking ◽  
Gas Oil ◽  
Light Gas Oil

Extraction of aromatic compounds from catalytic cracking light gas oil with nitromethane

1967 ◽  
Vol 3 (8) ◽  
pp. 568-570
Author(s):  
M. F. Bondarenko ◽  
V. M. Kolychev ◽  
O. N. Rudneva
Keyword(s):  
Aromatic Compounds ◽  
Catalytic Cracking ◽  
Gas Oil ◽  
Light Gas Oil

Catalytic cracking of light gas oil using microwaves as energy source

Fuel ◽  
2013 ◽  
Vol 106 ◽  
pp. 632-638 ◽  
Author(s):  
Alexandro Stonoga V. da Silva ◽  
Regina Weinschutz ◽  
Carlos I. Yamamoto ◽  
Luiz F.L. Luz
Keyword(s):  
Energy Source ◽  
Catalytic Cracking ◽  
Gas Oil ◽  
Light Gas Oil

scholarly journals CATALYTIC CRACKING OF HEAVY OIL OF ALIF FIELD – MARIB- YEMEN

2021 ◽  
Vol 2 (3) ◽  
pp. 103-108
Author(s):  
Rokhsana M. Ismail ◽  
Nadrah M. Husami ◽  
Sahar Alrifaei
Keyword(s):  
Heavy Oil ◽  
Catalytic Cracking ◽  
Chemical Engineering ◽  
Refining Process ◽  
Gas Oil ◽  
Simple Distillation ◽  
Process Pressure ◽  
Light Gas Oil ◽  
Cracking Process ◽  
Cracking Products

The study presents the results of the catalytic cracking process of heavy oil of the Alif – Marib field in Yemen. The best conditions of the process, pressure, temperature, and using zeolite HZSM-5 as catalyst were selected. Based on the characteristics of the heavy oil, the analyses were done using a gas chromatography technique and catalytic cracking unit designed in the laboratory of Chemical Engineering and Petrochemical faculty at Al-Baath University- Syria., refining process was done in Refining Company- Homs. The results of simple distillation of the cracking products at different range of temperature were (Gasoline= 19.5%; Kerosene=15%; Light gas oil= 36%; Distillate residue= 29.5%) and gases (CH4= 67.55 %; C2H4= 14.66 %; C2H6= 7.48 %; H3H8= 9.24%; C4H10=1.06 %). Extraction by sulfuric acid was done. An 84.044% oil-free aromatic has been gotten. In order to remove total paraffins from the oily cut that has a high pour point, different solvents were used. The properties of the oily cut from which the paraffin wax was removed gave encouraging results.

Effect of catalytic cracking conditions on the characteristics of light gas oil

1991 ◽  
Vol 27 (8) ◽  
pp. 439-443
Author(s):  
V. A. Stankevich ◽  
T. Kh. Melik-Akhnazarov ◽  
T. N. Mitusova ◽  
I. Ya. Perezhigina ◽  
A. M. Senekina ◽  
...  
Keyword(s):  
Catalytic Cracking ◽  
Gas Oil ◽  
Light Gas Oil

scholarly journals KAOLINITE MODIFIED BY ALUMINUM IN THE CRACKING OF VACUUM GASOIL AND IT’S MIXTURE WITH FUEL OIL

2020 ◽  
Vol 2 (440) ◽  
pp. 107-114
Author(s):  
L.D. Volkova ◽  
N.N. Zakarina ◽  
O.K. Kim ◽  
A.K. Akurpekova ◽  
D.A. Zhumadullaev ◽  
...  
Keyword(s):  
Aromatic Hydrocarbons ◽  
Catalytic Cracking ◽  
Zeolite Catalyst ◽  
Vacuum Gasoil ◽  
Fuel Oil ◽  
Vacuum Gas Oil ◽  
Gas Oil ◽  
Light Gas Oil ◽  
Oil Fuel ◽  
Zeolite Modification

The data of the cracking of vacuum gas oil (VG) and a mixture of VG with fuel oil (M-100) on HLaY zeolite catalyst based on acid-activated kaolinite of the Pavlodar deposit modified by aluminum are presented. The synthesis of the kaolinite matrix and the HLaY zeolite catalyst with its use, the physicochemical and acid characteristics of the catalyst and its constituent components, and the fractional and hydrocarbon compositions of vacuum gas oil are described. High mesoporosity of the H-form of the used kaolinite (86.2%), modified by aluminum of the H-form (84.1) and the HLaY catalyst (80.1%), which provide the activity of the sample in cracking of the mixture with a yield of 32.6% gasoline and 25.9% light gas oil (LG) at 4500С and in cracking of VG a yield of 38.2% gasoline and 29.4% LG at 5000С. The gasolines of cracking of LG contain an increased content of iso paraffins (up to 20.2%) and a low content of aromatic hydrocarbons (24.1%), which makes the catalyst attractive for cracking a mixture of VG with fuel oil. Key words: catalytic cracking, kaolinite, vacuum gas oil, fuel oil, zeolite, modification.

Effect of the composition on the stability of light gas oil from catalytic cracking

1990 ◽  
Vol 26 (9) ◽  
pp. 471-473
Author(s):  
A. M. Danilov ◽  
N. N. Demina ◽  
V. G. Lebedevskaya ◽  
B. A. �nglin
Keyword(s):  
Catalytic Cracking ◽  
Gas Oil ◽  
Light Gas Oil ◽  
The Stability ◽  
Effect Of The Composition

Synergistic Process for Coker Gas Oil Catalytic Cracking and Gasoline Reformation

2013 ◽  
Vol 27 (2) ◽  
pp. 654-665 ◽  
Author(s):  
Jinhong Zhang ◽  
Honghong Shan ◽  
Wenjing Liu ◽  
Xiaobo Chen ◽  
Chunyi Li ◽  
...  
Keyword(s):  
Catalytic Cracking ◽  
Gas Oil ◽  
Coker Gas Oil

Hydrotreatment of Cracked Light Gas Oil*

2018 ◽  
pp. 145-180
Author(s):  
R. Galiasso ◽  
W. Garcia ◽  
M. M. Ramirez De Agudelo ◽  
P. Andreu
Keyword(s):  
Gas Oil ◽  
Light Gas Oil

scholarly journals Conversion of sulphur compounds into light gas oil: I. Kinetics of the conversion of model compounds

2002 ◽  
Vol 56 (2) ◽  
pp. 68-75
Author(s):  
Jasna Jankovic ◽  
Dejan Skala
Keyword(s):  
Chemical Industry ◽  
Heterocyclic Compounds ◽  
Published Data ◽  
Gas Oil ◽  
Model Compounds ◽  
Sulphur Compounds ◽  
Middle Fraction ◽  
Light Gas Oil ◽  
Reactor Calculation ◽  
Kinetics Of

The problem of sulfur compounds conversion, particularly heterocyclic compounds, from the middle fraction of crude oil (light gas oil) was analyzed and will be published in several articles in the Chemical Industry Journal. Published data in the literature, covering the conversion of tiophene, benzothiophene and dibenzothiophene are presented in the first paper of this series with the goal of comparing and critically analyzing their usage for reactor calculation.

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