scholarly journals VISCOSITY MATHEMATICAL MODEL OF HEAVY OIL CONTAINING THE METAL OXIDES COLLOID NANOPARTICLES IMPURITY

2019 ◽  
pp. 199 ◽  
Author(s):  
Viktor I. Lesin
2017 ◽  
Vol 22 (1-2) ◽  
pp. 62-68
Author(s):  
V. Sh. Shagapov ◽  
Y. A. Yumagulova ◽  
A. A. Gizzatullina

In radially symmetric formulation is built and investigated mathematical model of the problem of heated heavy oil reservoir by horizontal well and the possibility of further operation of the well for the selection of oil with reduced viscosity. The resulting system of equations reveals the dynamics of the process, to evaluate the characteristics of the distance of penetration of filtration and thermal waves over the period.


2016 ◽  
Vol 693 ◽  
pp. 411-418
Author(s):  
S.Q. Kang ◽  
Y.P. You ◽  
M.Y. Feng

This paper obtains the formula for calculating fuel dynamic viscosity based on the Barus formula and Eying formula from both macroscopic and microscopic perspectives, studies the mathematical model of fuel bulk modulus changing with temperature and pressure based on equation of state for gases and solids, and computes the fitting formula and correlation coefficients of dynamic viscosity and bulk modulus based on IFO 180 test data. The result indicates that the calculation models for fuel dynamic viscosity and bulk modulus are effective.


Author(s):  
M D G M D S Carvalho ◽  
F C Lockwood

A mathematical model for the prediction of the performance of a glass furnace is described. It comprises sub-models for the combustion chamber, feed stock melting (batch), and the glass tank flow. The first sub-model which incorporates physical modelling for the lifted turbulent diffusion flames, soot formation and consumption, and the thermal radiation is given emphasis herein. The whole mathematical model is applied to an end-port regenerative furnace for both gas and heavy oil firing.


Processes ◽  
2021 ◽  
Vol 9 (2) ◽  
pp. 256
Author(s):  
Sergey M. Petrov ◽  
Aliya G. Safiulina ◽  
Natalya Yu. Bashkirtseva ◽  
Alfiya I. Lakhova ◽  
Galiya G. Islamova

Experiments were conducted simulating hydrothermal conversion of heavy oil in the presence of carbonate, kaolin, Al2O3, Ni2+ and Cu2+, NiO mixed with poly-α-olefins, C6H8O7, C2H4O2 at 290–375 °C and 10–135 bar. Al2O3, carbonate at 375 °C and 135 bar, accelerated the resin degradation. Experiments with carbonate at 350 °C and 10 bar showed no significant composition changes. NiSO4, CuSO4, kaolin mineral, at 350 °C and 78 bar, accelerated decomposition of resins (from 35.6% to 32.5%). Al2O3 and carbonate at 290 °C and 14 bar led to the destruction of asphaltenes (from 6.5% to 4.7% by weight), which were adsorbed on the surface of carbonate. Al2O3, NiO, poly-α-olefins at 350 °C and 78 bar accelerated C–C bond cracking of high-boiling asphaltenes. C6H8O7, rock-forming carbonate, at 360 °C and 14 bar, contributed to the polymerization and polycondensation of hydrocarbons with the formation of additional resins. C2H4O2 and kaolin at 360 °C and 12 bar affected the reduction in the resin content from 35.6% to 31.9% wt. C2H4O2 interacted with the active metals with the formation of acetate salts exhibiting catalytic activity.


2021 ◽  
Vol 11 (11) ◽  
pp. 4019-4028
Author(s):  
Xian Zhang ◽  
Hongchang Che ◽  
Yongjian Liu

AbstractIn order to investigate the catalytic effects of transition metal oxides submicro-particles on aquathermolysis of Liaohe extra-heavy crude oil, the catalysts NiO, α·Fe2O3 and Co3O4 are used and evaluated during the experiments. The optimum mass fraction of the catalyst and water was determined to be 5.0 wt% and 30 wt%, respectively. The optimum reaction time for aquathermolysis was 24 h, and the optimum reaction temperature was 240 °C. The analysis results showed the heavy oil was upgraded dramatically by addition of the catalysts based upon viscosity reduction, saturate/aromatics/resins/asphaltenes analyses, elemental analysis, Fourier transform infrared spectroscopy and gas chromatography. All results show the heavy oil is in situ updated dramatically by catalytic aquathermolysis under the optimum operating conditions. A five-lump model is proposed for estimating kinetic parameters of aquathermolysis and agrees well with the experimental data.


2017 ◽  
Vol 53 (2) ◽  
pp. 197-204
Author(s):  
V. P. Zaporin ◽  
S. V. Sukhov ◽  
M. Yu. Dolomatov ◽  
N. A. Zhuravleva ◽  
A. R. Galiakbirov ◽  
...  

Sign in / Sign up

Export Citation Format

Share Document