By Mikhail V. Lurie, Emmanuil Sinaiski
ISBN-10: 3527408339
ISBN-13: 9783527408337
In response to a good tried-and-tested lecture on the Russian nation college of Oil and fuel, this obtainable method of the idea of pipeline transportation offers systematic assurance of assorted varieties of fluids, subsidized through real-world examples. From the contents:* basics of mathematical modeling of one-dimensional flows* types of transported media* constitution of laminar and turbulent fluid flows* Modeling and calculation of steady-state regimes * Closed mathematical versions of one-dimensional fluid and fuel flows * Dimensional concept* actual modeling of phenomena* size and similarity in mathematical modeling of processesEnd-of-chapter difficulties make this useful e-book constant and compatible for self-study.
Read Online or Download Modeling of Oil Product and Gas Pipeline Transportation PDF
Similar petroleum books
Characterization and Properties of Petroleum Fractions
Either petroleum pros and people and not using a technical engineering history will locate this exact new handbook to be a necessary and accomplished reference for the petroleum in either processing and construction. WHAT MAKES THIS guide SO precise? • provides over six hundred predictive tools from theoretical to empirical, together with the main general and such a lot actual ones for quite a lot of stipulations • Covers over a hundred thermodynamic and actual houses, that are appropriate to a variety of natural compounds, combos, petroleum fractions, petroleum items, heavy residues, waxes, asphaltenes, crude oils, usual gases, reservoir fluids, and coal drinks.
The API person Certification courses (ICPs) are good validated all over the world within the oil, gasoline, and petroleum industries. This fast consultant is exclusive in offering uncomplicated, obtainable and well-structured advice for a person learning the API 510 qualified strain Vessel Inspector syllabus through: --Summarizing and assisting them during the syllabus; --Providing a number of instance questions and labored solutions.
Catalyst for Upgrading Heavy Petroleum Feeds
The ebook presents the main updated info on trying out and improvement of hydroprocessing catalysts with the purpose to enhance functionality of the normal and transformed catalysts in addition to to improve novel catalytic formulations. in addition to varied chemical composition, distinctive cognizance is dedicated to pore dimension and pore quantity distribution of the catalysts.
Petroleum Geosciences: Indian Contexts
This publication accommodates unique and assessment articles on a number of elements of petroleum geosciences from Indian terrains, either onshore and offshore, and comprises assorted geological (tectonic, sedimentological, natural geochemical, paleontological, stratigraphic, modelling and diverse others), geophysical equipment and coverage elements.
Additional resources for Modeling of Oil Product and Gas Pipeline Transportation
Example text
It is required to obtain the temperature of oil pumping over the pipeline section of length 150 km in cross-sections x = 50, 100 and 125 km, if the temperature at the beginning of the pipeline T0 = 60 ◦ C, that at the end TL = 30 ◦ C, and that of the environment Tex = 8 ◦ C. The extracted heat of internal friction may be ignored. Solution. Using Eq. 4231)x/150 . 4 C. = 47 C; T(100) ∼ 2. g. 41) takes the form ρvS dJ = πd · qn . , where Cp is the gas specific heat capacity at constant pressure (Cp > Cv ; Cp − Cv = R).
Using Eq. 5 · 109 )] = 757 kg m−3 . The density is increased by 12 kg m−3 . 2). The quantity γ˙ = du/ dy having the sense of velocity gradient with dimension s−1 , is called the shear rate. 3. This dependence states: ‘‘Tangential stresses arising in a medium having been modeled by a Newtonian viscous fluid are proportional to the shear rate of the fluid layers relative to each other. ’’ The dynamic viscosity of fluid µ is represented in this model by the slope of a straight line on the plane (˙γ, τ) : µ = tan ϕ, where ϕ is the angle of inclination of the straight line to the abscissa.
To use Eq. 47) one should go to the limit at κ → 0, therefore it would be better to use Eq. 004 · 150 · 103 /1950 ∼ = 3 K. Exercise 3. It is required to obtain the temperature of oil pumping over the pipeline section of length 150 km in cross-sections x = 50, 100 and 125 km, if the temperature at the beginning of the pipeline T0 = 60 ◦ C, that at the end TL = 30 ◦ C, and that of the environment Tex = 8 ◦ C. The extracted heat of internal friction may be ignored. Solution. Using Eq. 4231)x/150 .
Modeling of Oil Product and Gas Pipeline Transportation by Mikhail V. Lurie, Emmanuil Sinaiski
by Robert
4.1