ČUDINA, Mirko . Noise as an Indicator of Cavitation and Instability in Centrifugal Pumps. Strojniški vestnik - Journal of Mechanical Engineering, [S.l.], v. 45, n.4, p. 134-146, july 2017. ISSN 0039-2480. Available at: <https://www.sv-jme.eu/sl/article/noise-as-an-indicator-of-cavitation-and-instability-in-centrifugal-pumps/>. Date accessed: 19 nov. 2024. doi:http://dx.doi.org/.
Čudina, M. (1999). Noise as an Indicator of Cavitation and Instability in Centrifugal Pumps. Strojniški vestnik - Journal of Mechanical Engineering, 45(4), 134-146. doi:http://dx.doi.org/
@article{.,
author = {Mirko Čudina},
title = {Noise as an Indicator of Cavitation and Instability in Centrifugal Pumps},
journal = {Strojniški vestnik - Journal of Mechanical Engineering},
volume = {45},
number = {4},
year = {1999},
keywords = {centrifugal pumps; noise; cavitation; operating stability; },
abstract = {Instabilities of a pumping system can be caused by the onset of stall and surge, and/or by cavitation within the pump. Stall and surge occur at flow rates below the design flow rate whereas cavitation can occur within the entire range of operating conditions. Cavitation of a centrifugal pump is the result of insufficient net positive suction head (NPSH) during pump operation,and may cause three different, undesirable, effects: drop in head-capacity curves, damage of the impeller by pitting and erosion, and vibration and noise. The noise that is emitted can be used to detect the pump operating conditions and type of instability. The noise measured at the critical NPSH value can be used to determine the upper limit of permissible pump operation flow rates without cavitation of the pump.},
issn = {0039-2480}, pages = {134-146}, doi = {},
url = {https://www.sv-jme.eu/sl/article/noise-as-an-indicator-of-cavitation-and-instability-in-centrifugal-pumps/}
}
Čudina, M. 1999 July 45. Noise as an Indicator of Cavitation and Instability in Centrifugal Pumps. Strojniški vestnik - Journal of Mechanical Engineering. [Online] 45:4
%A Čudina, Mirko %D 1999 %T Noise as an Indicator of Cavitation and Instability in Centrifugal Pumps %B 1999 %9 centrifugal pumps; noise; cavitation; operating stability; %! Noise as an Indicator of Cavitation and Instability in Centrifugal Pumps %K centrifugal pumps; noise; cavitation; operating stability; %X Instabilities of a pumping system can be caused by the onset of stall and surge, and/or by cavitation within the pump. Stall and surge occur at flow rates below the design flow rate whereas cavitation can occur within the entire range of operating conditions. Cavitation of a centrifugal pump is the result of insufficient net positive suction head (NPSH) during pump operation,and may cause three different, undesirable, effects: drop in head-capacity curves, damage of the impeller by pitting and erosion, and vibration and noise. The noise that is emitted can be used to detect the pump operating conditions and type of instability. The noise measured at the critical NPSH value can be used to determine the upper limit of permissible pump operation flow rates without cavitation of the pump. %U https://www.sv-jme.eu/sl/article/noise-as-an-indicator-of-cavitation-and-instability-in-centrifugal-pumps/ %0 Journal Article %R %& 134 %P 13 %J Strojniški vestnik - Journal of Mechanical Engineering %V 45 %N 4 %@ 0039-2480 %8 2017-07-07 %7 2017-07-07
Čudina, Mirko. "Noise as an Indicator of Cavitation and Instability in Centrifugal Pumps." Strojniški vestnik - Journal of Mechanical Engineering [Online], 45.4 (1999): 134-146. Web. 19 Nov. 2024
TY - JOUR AU - Čudina, Mirko PY - 1999 TI - Noise as an Indicator of Cavitation and Instability in Centrifugal Pumps JF - Strojniški vestnik - Journal of Mechanical Engineering DO - KW - centrifugal pumps; noise; cavitation; operating stability; N2 - Instabilities of a pumping system can be caused by the onset of stall and surge, and/or by cavitation within the pump. Stall and surge occur at flow rates below the design flow rate whereas cavitation can occur within the entire range of operating conditions. Cavitation of a centrifugal pump is the result of insufficient net positive suction head (NPSH) during pump operation,and may cause three different, undesirable, effects: drop in head-capacity curves, damage of the impeller by pitting and erosion, and vibration and noise. The noise that is emitted can be used to detect the pump operating conditions and type of instability. The noise measured at the critical NPSH value can be used to determine the upper limit of permissible pump operation flow rates without cavitation of the pump. UR - https://www.sv-jme.eu/sl/article/noise-as-an-indicator-of-cavitation-and-instability-in-centrifugal-pumps/
@article{{}{.},
author = {Čudina, M.},
title = {Noise as an Indicator of Cavitation and Instability in Centrifugal Pumps},
journal = {Strojniški vestnik - Journal of Mechanical Engineering},
volume = {45},
number = {4},
year = {1999},
doi = {},
url = {https://www.sv-jme.eu/sl/article/noise-as-an-indicator-of-cavitation-and-instability-in-centrifugal-pumps/}
}
TY - JOUR AU - Čudina, Mirko PY - 2017/07/07 TI - Noise as an Indicator of Cavitation and Instability in Centrifugal Pumps JF - Strojniški vestnik - Journal of Mechanical Engineering; Vol 45, No 4 (1999): Strojniški vestnik - Journal of Mechanical Engineering DO - KW - centrifugal pumps, noise, cavitation, operating stability, N2 - Instabilities of a pumping system can be caused by the onset of stall and surge, and/or by cavitation within the pump. Stall and surge occur at flow rates below the design flow rate whereas cavitation can occur within the entire range of operating conditions. Cavitation of a centrifugal pump is the result of insufficient net positive suction head (NPSH) during pump operation,and may cause three different, undesirable, effects: drop in head-capacity curves, damage of the impeller by pitting and erosion, and vibration and noise. The noise that is emitted can be used to detect the pump operating conditions and type of instability. The noise measured at the critical NPSH value can be used to determine the upper limit of permissible pump operation flow rates without cavitation of the pump. UR - https://www.sv-jme.eu/sl/article/noise-as-an-indicator-of-cavitation-and-instability-in-centrifugal-pumps/
Čudina, Mirko"Noise as an Indicator of Cavitation and Instability in Centrifugal Pumps" Strojniški vestnik - Journal of Mechanical Engineering [Online], Volume 45 Number 4 (07 July 2017)
Strojniški vestnik - Journal of Mechanical Engineering 45(1999)4, 134-146
© The Authors, CC-BY 4.0 Int. Change in copyright policy from 2022, Jan 1st.
Instabilities of a pumping system can be caused by the onset of stall and surge, and/or by cavitation within the pump. Stall and surge occur at flow rates below the design flow rate whereas cavitation can occur within the entire range of operating conditions. Cavitation of a centrifugal pump is the result of insufficient net positive suction head (NPSH) during pump operation,and may cause three different, undesirable, effects: drop in head-capacity curves, damage of the impeller by pitting and erosion, and vibration and noise. The noise that is emitted can be used to detect the pump operating conditions and type of instability. The noise measured at the critical NPSH value can be used to determine the upper limit of permissible pump operation flow rates without cavitation of the pump.