About Complex Oil Flow Curve Form in Anomaly Viscosity Low Temperatures and Shear Rates Conditions

Article Preview

Abstract:

This paper presents results of studies of the problem to describe the nature of oil flow at low temperatures and shear velocities for prediction of flow fluidity and determination of the parameters of a cold start of an oil pipeline after an extended downtime. Analytical and experimental studies have been carried out, which include a review of rheological test data from earlier studies available in the literature and an analysis of empirical relation obtained with the rotational viscometry method. More specifically, the existence of a zone of viscosity anomaly for low-paraffin and heavy oils has been proved on the basis of laboratory test data of model mixtures of commercial crude oils and their weighted samples. The necessity has been substantiated to create more adaptive rheological models which fit the total curve of oil flow, including the zone of viscosity anomaly in the transient state of cold start, this zone manifesting itself when reaching a certain temperature, even for low-paraffin oils. Based on the results of this work, the most advance multi-factor rheological models have been identified for description of the total shape of the rheological curve in a wide range of temperatures and velocities.

You might also be interested in these eBooks

Info:

Periodical:

Materials Science Forum (Volume 1086)

Pages:

131-139

Citation:

Online since:

April 2023

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2023 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

* - Corresponding Author

[1] R.M. Karimov, B.N. Mastobaev, Change in the technology of pumping oil on the "Uzen - Atyrau - Samara", oil pipeline with the development of the oil transportation system of Western Kazakhstan Transport and storage of oil products and hydrocarbons. 2 (2010) 9-14.

Google Scholar

[2] R.M. Karimov, B.N. Mastobaev, Rheological features of the West Kazakhstan oil mixture, Transport and storage of oil products and hydrocarbon raw materials. 2 (2011) 3–7.

Google Scholar

[3] R.M. Karimov, B.N. Mastobaev, Joint transport of high-viscosity and highly solidifying oils of Western Kazakhstan via the "Uzen - Atyrau - Samara" oil pipeline, Transport and storage of oil products and hydrocarbons, 1, 3–6.

Google Scholar

[4] P.A. Revel-Muroz, R.N. Bakhtizin, R.M. Karimov, B.N. Mastobaev, Joint pumping of heavy and highly paraffinic oils in a mixture, Socar Proceedings, Scientific works. 2 (2018).

Google Scholar

[5] R.N. Bakhtizin, R.M. Karimov, B.N. Mastobaev, Influence of high-molecular components on rheological properties depending on the structural-group and fractional composition of oil, Socar Proceedings, Scientific works. 1 (2016).

DOI: 10.5510/ogp20160100269

Google Scholar

[6] P.A. Revel-Muroz, R.N. Bakhtizin, R.M. Karimov, B.N. Mastobaev, Joint use of thermal and chemical methods of exposure during the transportation of high-viscosity and solidifying oils, Socar Proceedings, Scientific works, 2 (2017).

DOI: 10.5510/ogp20170200314

Google Scholar

[7] R.M. Karimov, A.V. Zaplatin, R.R. Tashbulatov, Use of twisted heat exchangers made of small-radius coils for heating and heat treatment of oil, Publishing house of Information Agency Neftegaz.RU International. 12 (2018) 45-49.

Google Scholar

[8] R.M. Karimov, R.R. Tashbulatov, A.V. Zaplatin, Coiled Heat Exchanger with Small Radius Bent Tubes for Controlled Heat Treatment of High Viscosity Waxy Oil, IOP Conf. Series: Earth and Environmental Science. 272 (2019) 022193, doi: 10.1088 / 1755-1315 / 272/2/022193

DOI: 10.1088/1755-1315/272/2/022193

Google Scholar

[9] RD 39-30-139-79, Method of thermal hydraulic calculation of main pipelines under stationary and non-stationary modes of pumping, Newtonian and non-Newtonian oils in various climatic conditions.

Google Scholar

[10] RD 39-30-648-81, Method for determining starting pressure for oil pipelines transporting paraffinic oils.

Google Scholar

[11] RD-39-0147103-329-86, Methods for determining the rheological parameters of highly solidifying oils.

Google Scholar

[12] R.M. Karimov, B.N. Mastobaev, Features of pipeline transport of multicomponent systems, Azerbaijan Oil Industry. 1 (2012) 60-63.

Google Scholar

[13] A.Sh. Akzhigitov, On the rheological curve of non-Newtonian oil, Oil and gas. 3 (2007) 53-56.

Google Scholar

[14] R.N. Bakhtizin, R.M. Karimov, B.N. Mastobaev, Generalized flow curve and universal rheological model of oil, Socar Proceedings, Scientific works. 2 (2016).

DOI: 10.5510/ogp20160200277

Google Scholar

[15] R.R. Tashbulatov, R.M. Karimov, B.N. Mastobaev, A.R. Valeev, Approximation of the rheological curve in low-temperature zones of anomalous flow of non-Newtonian oils using an asymptotic model, Pipeline transport, Theory and practice. 4 (2017) 62.

Google Scholar

[16] R.R. Tashbulatov, R.M. Karimov, B.N. Mastobaev, A.R. Valeev, Asymptotic model for describing the rheological curve of non-Newtonian flow of oil mixtures, Transport and storage of oil products and hydrocarbons. 5 (2017) 14 – 23.

Google Scholar

[17] R.R. Tashbulatov, R.M. Karimov, A.R. Valeev, A.V. Kolchin, B.N. Mastobaev, The Asymptotic Rheological Model of Anomalously Viscous Oil Journal of Engineering and Applied Sciences. 7 (2018) 5502-5506.

Google Scholar

[18] R.R. Tashbulatov, R.M. Karimov, A.R. Valeev, B.N. Mastobaev, Modeling the rheological properties of thixotropic oils in the direct course of measurements on rotary viscometers to assess the starting modes of the main oil pipeline, Oil industry. 4 (2020) 80-85.

DOI: 10.24887/0028-2448-2020-4-80-84

Google Scholar