Displacement of Oil from Porous Bed by the Oscillating Flow of Polymer Solution

Volodymyr G. Pogrebnyak; Iryna V. Perkun; Andriy V. Pogrebnyak

doi:doi:10.11648/j.ajset.20160102.16

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Displacement of Oil from Porous Bed by the Oscillating Flow of Polymer Solution

Volodymyr G. Pogrebnyak, Iryna V. Perkun, Andriy V. Pogrebnyak

Published in American Journal of Science, Engineering and Technology (Volume 1, Issue 2)

Received: 1 November 2016 Accepted: 9 December 2016 Published: 12 January 2017

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Abstract

The successful and economical design, scale up and operation of a fluidized bed reactor depends upon the true prediction of its bed hydrodynamics. The present research has been carried out to study the hydrodynamics behavior of bed of semolina particles in liquid solid fluidization. The prime objective of this research work is to study the effect of liquid superficial velocity and variation in static bed height on the minimum fluidization velocity and pressure drop. Liquid-solid fluidization is characterized by the uniform expansion of bed particles, therefore it is known as particulate fluidization. In liquid solid fluidization, there is no bubbling phase, that is the main cause of uniform bed expansion. Liquid-solid fluidization has extensive field of applications, i.e. in hydrometallurgy, waste water treatment, biochemical processing and food technology. Minimum fluidization velocity and pressure drop are important hydrodynamic parameters in the design and scale up of fluidized bed reactors. The experimental work was carried out in a column made up of acrylic having 60mm outer diameter and 2mm wall thickness and was 1000mm long. Manometers were used to observe the pressure drop variations across the bed. The minimum fluidization velocity was found to be 0.404mm/sec. It has been found that the minimum fluidization velocity is not affected by the variations in the initial static bed height. Semolina particles being sticky solids offer slightly greater pressure drop. Pressure drop becomes constant when fluidization is achieved.

Published in	American Journal of Science, Engineering and Technology (Volume 1, Issue 2)
DOI	10.11648/j.ajset.20160102.16
Page(s)	53-57
Creative Commons	This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.
Copyright	Copyright © The Author(s), 2017. Published by Science Publishing Group

Keywords

Oscillating Flow, Solution of Polymer, Velocity Gradient, Oil Displacement, Porous Bed, Viscosity, Relaxation Time

References

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[2]	V. S. Boyko, R. M. Kondrat, R. C. Yaremchuk “Handbook of oil and gas science”. L’viv, Svit, 1996, 620 p.
[3]	N. K. Korsakova, V. I. Penkovsky, L. K. Altuninaand, V. A. Kuvshinov “Redistribution of filtration flows by thermo gel at boundary water flooding of oil reservoirs”, 2016, AIP Conf. Proc., Tomsk, pp. 1783–1784.
[4]	A. Y. Malkin, A. Arinstein, V. G. Kulichikhin “Polymer extension flows and instabilities”. Progress in Polymer Science, 2014, vol. 39. No. 5. pp. 959-978.
[5]	V. G. Pogrebnyak, V. S. Voloshin “Ecological Technology of Creating Waterproof Screens”, Donetsk, Knowledge, 2010, 482 p.
[6]	V. G. Pogrebnyak, A. A. Pisarenko “Deformation effects in case of a flow with stretching of polymer solutions”. Turbulence and Shear flow phenomena–1, Santa Barbara, California, Banerjee S., Eaton J. K. editors, New York, 1999, pp. 1345–1350.
[7]	V. G. Pogrebnyak, Yu. F. Ivanyuta and S. Y. Frenkel “The structure of the hydrodynamic field and distortions of the molecular shape of flexible polymers under free-converging flow conditions”, Polymer Sci. USSR, 1992, vol. 34, No. 3, pp. 270–273.
[8]	J. D. Ferry “Viscoelastic properties of polymers”. 1980. John Wiley & Sons, 641 p.
[9]	A. Y. Malkin, "Current Status of Polymer Rheology: achievements and problems" series. Polymer Sci., 2009, ser. А, vol. 51, No. 1, pp. 106–136.
[10]	V. G. Baranov, Yu. V. Brestkin, S. A. Agranova, V. N. Pinkevich "The behavior of macromolecules polystyrene in "viscosities" of a good solvent”. Polymer Sci., 1986, ser. B, vol. 28, No. 11. pp. 841–843.
[11]	A. V. Bazelevich, V. M. Entov, A. V. Karpov [and др.], “The Relaxation Time of Polymer Solutions: Methods of Measurement and Some of Its Applications”. Moscow, Instit. of Appl. Mech. of the Russian Academy of Sciences, 1991, 42p.

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APA Style

Volodymyr G. Pogrebnyak, Iryna V. Perkun, Andriy V. Pogrebnyak. (2017). Displacement of Oil from Porous Bed by the Oscillating Flow of Polymer Solution. American Journal of Science, Engineering and Technology, 1(2), 53-57. https://doi.org/10.11648/j.ajset.20160102.16

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ACS Style

Volodymyr G. Pogrebnyak; Iryna V. Perkun; Andriy V. Pogrebnyak. Displacement of Oil from Porous Bed by the Oscillating Flow of Polymer Solution. Am. J. Sci. Eng. Technol. 2017, 1(2), 53-57. doi: 10.11648/j.ajset.20160102.16

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AMA Style

Volodymyr G. Pogrebnyak, Iryna V. Perkun, Andriy V. Pogrebnyak. Displacement of Oil from Porous Bed by the Oscillating Flow of Polymer Solution. Am J Sci Eng Technol. 2017;1(2):53-57. doi: 10.11648/j.ajset.20160102.16

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@article{10.11648/j.ajset.20160102.16,
  author = {Volodymyr G. Pogrebnyak and Iryna V. Perkun and Andriy V. Pogrebnyak},
  title = {Displacement of Oil from Porous Bed by the Oscillating Flow of Polymer Solution},
  journal = {American Journal of Science, Engineering and Technology},
  volume = {1},
  number = {2},
  pages = {53-57},
  doi = {10.11648/j.ajset.20160102.16},
  url = {https://doi.org/10.11648/j.ajset.20160102.16},
  eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajset.20160102.16},
  abstract = {The successful and economical design, scale up and operation of a fluidized bed reactor depends upon the true prediction of its bed hydrodynamics. The present research has been carried out to study the hydrodynamics behavior of bed of semolina particles in liquid solid fluidization. The prime objective of this research work is to study the effect of liquid superficial velocity and variation in static bed height on the minimum fluidization velocity and pressure drop. Liquid-solid fluidization is characterized by the uniform expansion of bed particles, therefore it is known as particulate fluidization. In liquid solid fluidization, there is no bubbling phase, that is the main cause of uniform bed expansion. Liquid-solid fluidization has extensive field of applications, i.e. in hydrometallurgy, waste water treatment, biochemical processing and food technology. Minimum fluidization velocity and pressure drop are important hydrodynamic parameters in the design and scale up of fluidized bed reactors. The experimental work was carried out in a column made up of acrylic having 60mm outer diameter and 2mm wall thickness and was 1000mm long. Manometers were used to observe the pressure drop variations across the bed. The minimum fluidization velocity was found to be 0.404mm/sec. It has been found that the minimum fluidization velocity is not affected by the variations in the initial static bed height. Semolina particles being sticky solids offer slightly greater pressure drop. Pressure drop becomes constant when fluidization is achieved.},
 year = {2017}
}

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TY - JOUR
T1 - Displacement of Oil from Porous Bed by the Oscillating Flow of Polymer Solution
AU - Volodymyr G. Pogrebnyak
AU - Iryna V. Perkun
AU - Andriy V. Pogrebnyak
Y1 - 2017/01/12
PY - 2017
N1 - https://doi.org/10.11648/j.ajset.20160102.16
DO - 10.11648/j.ajset.20160102.16
T2 - American Journal of Science, Engineering and Technology
JF - American Journal of Science, Engineering and Technology
JO - American Journal of Science, Engineering and Technology
SP - 53
EP - 57
PB - Science Publishing Group
SN - 2578-8353
UR - https://doi.org/10.11648/j.ajset.20160102.16
AB - The successful and economical design, scale up and operation of a fluidized bed reactor depends upon the true prediction of its bed hydrodynamics. The present research has been carried out to study the hydrodynamics behavior of bed of semolina particles in liquid solid fluidization. The prime objective of this research work is to study the effect of liquid superficial velocity and variation in static bed height on the minimum fluidization velocity and pressure drop. Liquid-solid fluidization is characterized by the uniform expansion of bed particles, therefore it is known as particulate fluidization. In liquid solid fluidization, there is no bubbling phase, that is the main cause of uniform bed expansion. Liquid-solid fluidization has extensive field of applications, i.e. in hydrometallurgy, waste water treatment, biochemical processing and food technology. Minimum fluidization velocity and pressure drop are important hydrodynamic parameters in the design and scale up of fluidized bed reactors. The experimental work was carried out in a column made up of acrylic having 60mm outer diameter and 2mm wall thickness and was 1000mm long. Manometers were used to observe the pressure drop variations across the bed. The minimum fluidization velocity was found to be 0.404mm/sec. It has been found that the minimum fluidization velocity is not affected by the variations in the initial static bed height. Semolina particles being sticky solids offer slightly greater pressure drop. Pressure drop becomes constant when fluidization is achieved.
VL - 1
IS - 2
ER -

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Author Information

Volodymyr G. Pogrebnyak

Department of Environmental Engineering, National Technical University of Oil and Gas, Ivano-Frankivsk, Ukraine
Iryna V. Perkun

Department of Environmental Engineering, National Technical University of Oil and Gas, Ivano-Frankivsk, Ukraine
Andriy V. Pogrebnyak

Faculty of Equipment and Technical Service, Kharkiv State University of Food Technology, Kharkiv, Ukraine

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APA Style

Volodymyr G. Pogrebnyak, Iryna V. Perkun, Andriy V. Pogrebnyak. (2017). Displacement of Oil from Porous Bed by the Oscillating Flow of Polymer Solution. American Journal of Science, Engineering and Technology, 1(2), 53-57. https://doi.org/10.11648/j.ajset.20160102.16

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ACS Style

Volodymyr G. Pogrebnyak; Iryna V. Perkun; Andriy V. Pogrebnyak. Displacement of Oil from Porous Bed by the Oscillating Flow of Polymer Solution. Am. J. Sci. Eng. Technol. 2017, 1(2), 53-57. doi: 10.11648/j.ajset.20160102.16

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AMA Style

Volodymyr G. Pogrebnyak, Iryna V. Perkun, Andriy V. Pogrebnyak. Displacement of Oil from Porous Bed by the Oscillating Flow of Polymer Solution. Am J Sci Eng Technol. 2017;1(2):53-57. doi: 10.11648/j.ajset.20160102.16

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@article{10.11648/j.ajset.20160102.16,
  author = {Volodymyr G. Pogrebnyak and Iryna V. Perkun and Andriy V. Pogrebnyak},
  title = {Displacement of Oil from Porous Bed by the Oscillating Flow of Polymer Solution},
  journal = {American Journal of Science, Engineering and Technology},
  volume = {1},
  number = {2},
  pages = {53-57},
  doi = {10.11648/j.ajset.20160102.16},
  url = {https://doi.org/10.11648/j.ajset.20160102.16},
  eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajset.20160102.16},
  abstract = {The successful and economical design, scale up and operation of a fluidized bed reactor depends upon the true prediction of its bed hydrodynamics. The present research has been carried out to study the hydrodynamics behavior of bed of semolina particles in liquid solid fluidization. The prime objective of this research work is to study the effect of liquid superficial velocity and variation in static bed height on the minimum fluidization velocity and pressure drop. Liquid-solid fluidization is characterized by the uniform expansion of bed particles, therefore it is known as particulate fluidization. In liquid solid fluidization, there is no bubbling phase, that is the main cause of uniform bed expansion. Liquid-solid fluidization has extensive field of applications, i.e. in hydrometallurgy, waste water treatment, biochemical processing and food technology. Minimum fluidization velocity and pressure drop are important hydrodynamic parameters in the design and scale up of fluidized bed reactors. The experimental work was carried out in a column made up of acrylic having 60mm outer diameter and 2mm wall thickness and was 1000mm long. Manometers were used to observe the pressure drop variations across the bed. The minimum fluidization velocity was found to be 0.404mm/sec. It has been found that the minimum fluidization velocity is not affected by the variations in the initial static bed height. Semolina particles being sticky solids offer slightly greater pressure drop. Pressure drop becomes constant when fluidization is achieved.},
 year = {2017}
}

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