Influence of an impeller inlet diameter on operation of a high-speed submersible electric pump at the high flow rate modes

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BACKGROUND: The study object is a high-speed drainage submersible electric pump, aimed to water polluted sea and fresh water bailing out of drowned rooms of shipbuilding industry facilities.

AIMS: To obtain dependencies of pump cavitation properties on relative diameter of an impeller inlet at the high flow rate modes, to determine the kind of head-capacity and energy properties of a pump for various geometrical ratios of an impeller in the flow rate operational range.

METHODS: Main geometrical properties of impellers were determined with use of semi-empirical formulas of various authors’ methods. For the study of dependencies, three options of impellers were chosen and series of fluid dynamic simulations of three-dimensional flow of viscous fluid with use of the ANSYS CFX software were completed.

RESULTS: Head-capacity, energy and cavitation properties of the pumping unit were obtained. The experimental head-capacity curve correlates to the simulated one. The simulation results revealed that using of narrowed impeller inlet leads to generation of wide low-pressure area at the backside of the impeller vane and disruption of operational curves at the high flow rate modes. With the biggest relative diameter of the impeller inlet, the vapor pressure area at the backside of the impeller is absent so there is no disruption of operational curves at the high flow rate modes, however, the pump hydraulic efficiency ratio at the whole range of flow rate is the lowest among all the studied options of impellers.

CONCLUSIONS: The method of defining the value of an impeller inlet diameter, optimal with regard to energy and cavitation properties, to ensure cavitation free operation of a high-speed submersible electric pump at the whole range of flow rate is proposed.

作者简介

Daniil Gorbatov

Peter the Great St. Petersburg Polytechnic University; SULAK

Email: Da.Gorbatov@yandex.ru
ORCID iD: 0000-0002-3172-3346
SPIN 代码: 5727-2661

post graduate

俄罗斯联邦, 29 Politekhnicheskaya street, 195251, Saint Petersburg; Saint Petersburg

Alexander Zharkovsky

Peter the Great St. Petersburg Polytechnic University

Email: azharkovsky@gmail.com
ORCID iD: 0000-0002-3044-8768
SPIN 代码: 3637-7853

Professor, Dr. Sci. (Tech.); Professor

俄罗斯联邦, 29 Politekhnicheskaya street, 195251, Saint Petersburg

Artemy Adrianov

"SULAK"

编辑信件的主要联系方式.
Email: mr_a@inbox.ru
ORCID iD: 0000-0003-4853-0804
SPIN 代码: 8117-4795

General Director

俄罗斯联邦, 29 Politekhnicheskaya street, 195251, Saint Petersburg

参考

  1. Zharkovskiy AA, Kurikov NN, Pugachev PV, et al. Computer research and visualization of flow in centrifugal pumps. Nauchno-tekhnicheskie vedomosti SPbGPU. Informatika. Telekommunikatsii. Upravlenie. 2010;4(103):119–123. (in Russ).
  2. ANSYS CFX Tutorial Guide. Release 17.2. ANSYS Inc.
  3. Garbaruk AV, Strelets MKh, Travin AK, et al. Sovremennye podkhody k modelirovaniyu turbulentnosti: uch. pos. St. Petersburg.: Izd-vo Politekh. un-ta; 2016. (in Russ).
  4. Gorgidzhanyan SA. Gidravlicheskie raschety protochnoy chasti tsentrobezhnykh nasosov: metodicheskie ukazaniya po kursovomu proektirovaniyu. Leningrad: LPI im. MI Kalinina; 1982. (in Russ).
  5. Graueser TE. Abaque pour pompes et pompesturbines reversibl. Lausanne: Institut de machines hydraulignes; 1978.
  6. Gulich JF. Centrifugal Pumps. Berlin, Heidelberg: Springer-Verlag; 2010.
  7. Mikhaylov AK, Malyushenko VV. Lopastnye nasosy. Teoriya, raschet i konstruirovanie. Moscow: Mashinostroenie; 1977. (in Russ).

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2. Fig. 1. The submersible pump design.

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3. Fig. 2. Head-capacity and energy curves of the pump for various impeller inlet diameters: 1 – D0 /D2=0.62; 2 – D0 /D2=0.66; 3 – D0 /D2=0.78; solid lines – the simulation, dashed lines – the experiment.

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4. Fig. 3. The simulated overall cavitation curves for various impeller inlet diameters: 1 – D0 /D2=0.62; 2 – D0 /D2=0.66; 3 – D0 /D2=0.78; Δhexp is the distance between free surface and the pump inlet in the experiment.

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5. Fig. 4. The absolute pressure field of the original impeller (D0 /D2=0.62).

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6. Fig. 5. The absolute pressure field of the new impeller (D0 /D2=0.78).

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版权所有 © Gorbatov D.A., Zharkovsky A.A., Adrianov A.V., 2023

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