Kinetic parameters of the formation of oxygen-containing compounds in the vacuum gas oil oxycracking process

被引:4
作者
Guseinova, E. A. [1 ]
Adzhamov, K. Yu. [1 ]
Safarova, S. R. [1 ]
机构
[1] Azerbaijan State Oil & Ind Univ, 16-21 Azadliq Ave, Baku, Azerbaijan
关键词
Kinetics; Oxygen-containing compounds; Oxycracking; Vacuum gas oil; FLUID CATALYTIC CRACKING; MODEL; MECHANISMS;
D O I
10.1007/s11144-020-01725-8
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The kinetics of the formation of oxygen-containing compounds during oxycracking of vacuum gas oil was experimentally studied. The kinetic parameters of the process of formation of oxygen-containing compounds in five target fractions under oxycracking conditions are established: reaction rates, rate constants, reaction orders, activation energies. The average reaction rate of the formation of oxygen-containing compounds in oxycracking products in the first 600 s is limited by the rate of oxidation of the C-10-C-12 fraction, further from 600 up to 900 s by the oxidation of the C-5-C-9 fraction (during this period, the direction/mechanism of the formation of OCC in this fraction changes), and after 900 s-the fractions C-1-C-4. The presence of the induction period indicates that the formation of oxygen-containing compounds in the C-1-C-4 fraction occurs according to the unbranched chain mechanism, and C-5-C-9 and C-22-C-30-through the chain with degenerate branching. The combination of experimental and calculated data indicates a joint homogeneous heterogeneous oxycracking mechanism of vacuum gas oil, which excludes the single-valued contribution of only the volume or only the surface of the catalyst. It is shown that under oxycracking conditions the process proceeds both in the kinetic and in the internal transition region, depending on the temperature.
引用
收藏
页码:925 / 939
页数:15
相关论文
共 26 条
[1]  
Boreskov G.K, 1986, Heterogeneous Catalysis, P304
[2]   A ONE-PARAMETER MODEL OF CATALYST DEACTIVATION FOR FCC MODELING [J].
DAS, AK ;
WOJCIECHOWSKI, BW .
CHEMICAL ENGINEERING SCIENCE, 1993, 48 (06) :1041-1049
[3]   Nine-lumped kinetic model for VGO catalytic cracking; using catalyst deactivation [J].
Ebrahimi, Ali Afshar ;
Mousavi, Hadis ;
Bayesteh, Hamid ;
Towfighi, Jafar .
FUEL, 2018, 231 :118-125
[4]  
Engel TH, 2013, THERMODYNAMICS STAT, P648
[5]   Influence of acidity on the H-Y zeolite performance in n-decane catalytic cracking: evidence of a series/parallel mechanism [J].
Fonseca, N. ;
Lemos, F. ;
Laforge, S. ;
Magnoux, P. ;
Ribeiro, F. Ramoa .
REACTION KINETICS MECHANISMS AND CATALYSIS, 2010, 100 (02) :249-263
[6]   Computational Determination of Conditions for the Vacuum Gas Oil Oxycracking Process [J].
Guseinova, E. A. ;
Mursalova, L. A. ;
Bagirova, N. N. ;
Adzhamov, K. Yu. .
PETROLEUM CHEMISTRY, 2019, 59 (02) :180-185
[7]  
Hadzhieva SN, 1982, KREKING NEFTYANYIH F
[8]   Optimal design and operation of an industrial fluidized catalytic cracking reactor [J].
Jarullah, Aysar T. ;
Awad, Noor A. ;
Mujtaba, Iqbal M. .
FUEL, 2017, 206 :657-674
[9]   Parameter estimation of a six-lump kinetic model of an industrial fluid catalytic cracking unit [J].
John, Yakubu M. ;
Mustafa, Mustafa A. ;
Patel, Raj ;
Mujtaba, Iqbal M. .
FUEL, 2019, 235 :1436-1454
[10]   KINETIC-MODELS OF HETEROGENEOUS CATALYTIC REACTIONS (REVIEW) [J].
KIPERMAN, SL .
BULLETIN OF THE ACADEMY OF SCIENCES OF THE USSR DIVISION OF CHEMICAL SCIENCE, 1991, 40 (12) :2350-2365