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CN107299909B - A kind of low NPSHr method for designing impeller - Google Patents

A kind of low NPSHr method for designing impeller Download PDF

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Publication number
CN107299909B
CN107299909B CN201610457342.5A CN201610457342A CN107299909B CN 107299909 B CN107299909 B CN 107299909B CN 201610457342 A CN201610457342 A CN 201610457342A CN 107299909 B CN107299909 B CN 107299909B
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China
Prior art keywords
impeller
npshr
rice
pump
inlet
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CN107299909A (en
Inventor
朱荣生
张本营
杨爱玲
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Jiangsu Guoquan Pumps Co Ltd
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Jiangsu Guoquan Pumps Co Ltd
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Priority to CN201610457342.5A priority Critical patent/CN107299909B/en
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00Details, component parts, or accessories
    • F04D29/18Rotors
    • F04D29/22Rotors specially for centrifugal pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00Details, component parts, or accessories
    • F04D29/18Rotors
    • F04D29/22Rotors specially for centrifugal pumps
    • F04D29/24Vanes
    • GPHYSICS
    • G16INFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR SPECIFIC APPLICATION FIELDS
    • G16ZINFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR SPECIFIC APPLICATION FIELDS, NOT OTHERWISE PROVIDED FOR
    • G16Z99/00Subject matter not provided for in other main groups of this subclass

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
  • Hydraulic Turbines (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

The present invention relates to a kind of low NPSHr method for designing impeller, the required cavitation surplus NPSHr relevant parameter mainly for vane pump is provided:The required cavitation surplus NPSHr of vane pump minimum(min), minimum required cavitation surplus COEFFICIENT Kp, vane inlet excretion coefficient ξ that liquid is flowed0, modified impeller inlet diameter Dp, modified impeller inlet equivalent diameter Dp0, by improving impeller parameters, the anti-cavitation performance of vane pump is improved, the stability of vane pump is improved, achievees the purpose that the service life for extending pump and associated components.

Description

A kind of low NPSHr method for designing impeller
Technical field
The present invention relates to a kind of impeller of vane pump design method, in particular to a kind of low NPSHr method for designing impeller.
Background technique
When cavitation phenomenon refers to that the fluid field pressure in liquid stream is reduced under the steam pressure of saturation, liquid will be by liquid It is changed into the gaseous state vacuole full of steam, so that its thermodynamic state is changed.Cavitation is also known as cavitation, cavitation phenomenon pump, Often occur in the fluid machineries such as jet pipe, propeller, the hydraulic turbine, especially in vane pump.
Performance of the cavitation in addition to reducing hydraulic, permanent cavitation also will cause the destruction of material surface, reduce overcurrent The mechanical strength and overcurrent performance of component, and it will cause flow field internal irregularities for instantaneous cavitation, generate vibration and noise, these The structure that unstable pressure and oscillation may cause flow passage components is destroyed.
It is the fundamental equation for describing pump cavitation there are two fundamental equation in blade pump cavitation governing equation:Device cavitation Surplus NPSHa and pump cavitation surplus NPSHr.Device cavitation surplus NPSHa is also known as effective cavitation surplus, is mentioned by suction apparatus Supply, have in the entrance Unit Weight liquid of pump be more than pressure for vaporization head power surplus, i.e. liquid at pump inlet The total head having subtracts the only surplus value of pressure for vaporization head.Pump cavitation surplus NPSHr is related with pump internal flow situation, is It itself is determined by pump.NPSHr characterizes the pressure drop of pump inlet part, cavitation does not just also occur in order to guarantee to pump, it is desirable that pumping Entrance Unit Weight liquid has the power surplus more than pressure for vaporization head, and physical significance indicates liquid in pump inlet portion The degree of partial pressure drop.Since pump cavitation surplus NPSHr is itself to determine that the present invention is mainly to pump cavitation surplus by pump NPSHr is optimized.
Seldom minimum pump cavitation surplus NPSHr is described in design in the design process of the vane pump of the prior art, right The cavitation description inaccuracy of itself is pumped, therefore is easy to appear blade pump cavitation, to cause blade pump speed more than specified turn Cavitation phenomenon occurs when fast.
Application No. is No. 201510679202.8 Chinese invention patents to disclose a kind of high anti-cavitation centrifugal impeller waterpower Design method, this design method are by improving the import laying angle of blade, vane thickness distribution, impeller inlet diameter and leaf Piece entrance width can reduce the bending degree of blade, increase the area of passage of vane inlet, improve the efficiency of centrifugal pump, Cavitation surplus reduces, and cavitation performance is improved.Make impeller channel by different leaves number and specific speed to design subtended angle of blade Interior flowing, which is spread, to be reduced, and flowing is reduced closer to blade shape since the whirlpool of the separation of flow is spread to high-pressure side.But it is above-mentioned special In benefit mention parameter description pump cavitation surplus NPSHR is not described, do not establish yet pump cavitation surplus NPSHR with The relationship of impeller basic parameter.
For above-mentioned defect, the present inventor has invented a kind of low NPSHr method for designing impeller, to pump cavitation surplus NPSHr has carried out accurate description, obtains minimum pump cavitation surplus, to alleviate vane pump in certain degree in the feelings of stall The problem of cavitation occurs under condition, ensure that the anti-cavitation performance of vane pump.
Summary of the invention
To solve the above-mentioned problems, the present invention provides a kind of low NPSHr method for designing impeller.By accurately describing to pump Cavitation surplus NPSHr improves vane pump anti-cavitation performance.
Realizing technical solution used by above-mentioned purpose is:
1, first with common calculation method by initial impeller inlet equivalent diameter D0With impeller outlet diameter D2It is calculated.
2, the excretion coefficient ξ that vane inlet flows liquid0
In formula:
D0- initial impeller inlet equivalent diameter, rice;
ξ0The excretion coefficient that-vane inlet flows liquid;
N-design conditions revolving speed, rev/min;
D2- impeller outlet diameter, rice;
β0 *Shroud blade section blade exit laying angle before-impeller, degree;
3, minimum required cavitation surplus COEFFICIENT Kp
In formula:
KpThe required cavitation surplus coefficient of-minimum;
D0- initial impeller inlet equivalent diameter, rice;
D2- impeller outlet diameter, rice;
ξ0The excretion coefficient that-vane inlet flows liquid;
Q-design conditions flow, rice3/ the second;
N-design conditions revolving speed, rev/min;
4, modified impeller inlet diameter Dp
Dp=Kp·(Q/n)1/3
In formula:
KpThe required cavitation surplus coefficient of-minimum;
Q-design conditions flow, m3/s;
N-design conditions revolving speed, rev/min;
5, modified impeller inlet equivalent diameter Dp0
Dp0=Dp·(1-r2)1/2
In formula:
Dp0- modified impeller inlet equivalent diameter, rice;
Dp- modified impeller inlet diameter, rice;
R-impeller hub radius, rice.
According to above-mentioned steps, a kind of available low NPSHr Paddle Pump Designing method.
Detailed description of the invention
The present invention is further described with reference to the accompanying drawings and detailed description.
Fig. 1 is centrifugal pump impeller axial plane figure.
Specific embodiment
The present invention mainly improves vane pump anti-cavitation performance by accurately describing pump cavitation surplus NPSHr, slows down The cavitation of blade.
This embodiment is to be improved on the basis of giving original vane pump the cavitation surplus NPSHr of vane pump:
Fig. 1 has determined the present embodiment:
1, first with common calculation method by initial impeller inlet equivalent diameter D0With impeller outlet diameter D2It is calculated.
2, the excretion coefficient ξ that vane inlet flows liquid0
3, minimum required cavitation surplus COEFFICIENT Kp
4, modified impeller inlet diameter Dp
Dp=Kp·(Q/n)1/3
5, modified impeller inlet equivalent diameter Dp0
Dp0=Dp·(1-r2)1/2

Claims (1)

1. a kind of low NPSHr method for designing impeller provides the required cavitation surplus NPSHr correlation ginseng mainly for vane pump Number:The required cavitation surplus NPSHr of vane pump minimum(min), minimum required cavitation surplus COEFFICIENT Kp, vane inlet flows liquid Excretion coefficient ξ0, modified impeller inlet diameter Dp, modified impeller inlet equivalent diameter Dp0, it is characterised in that:Impeller It is suitble to following relationship between geometric parameter and pump operating point for design performance parameter:
Dp=Kp·(Q/n)1/3 (4)
Dp0=Dp·(1-r2)1/2 (5)
In formula:
NPSHr(min)The required cavitation surplus of-minimum, rice;
Dp0- modified impeller inlet equivalent diameter, rice;
D0- initial impeller inlet equivalent diameter, rice;
KpThe required cavitation surplus coefficient of-minimum;
ξ0The excretion coefficient that-vane inlet flows liquid;
Q-design conditions flow, rice3/ the second;
N-design conditions revolving speed, rev/min;
D2- impeller outlet diameter, rice;
β0 *Shroud blade section blade exit laying angle before-impeller, degree;
Dp- modified impeller inlet diameter, rice;
R-impeller hub radius, rice.
CN201610457342.5A 2016-06-22 2016-06-22 A kind of low NPSHr method for designing impeller Active CN107299909B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610457342.5A CN107299909B (en) 2016-06-22 2016-06-22 A kind of low NPSHr method for designing impeller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610457342.5A CN107299909B (en) 2016-06-22 2016-06-22 A kind of low NPSHr method for designing impeller

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Publication Number Publication Date
CN107299909A CN107299909A (en) 2017-10-27
CN107299909B true CN107299909B (en) 2018-11-30

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103016396A (en) * 2012-12-11 2013-04-03 江苏大学 Centrifugal pump hydraulic design method controlling maximum flow by cavitation
EP2589811A2 (en) * 2011-11-03 2013-05-08 Assoma Inc. Magnetic drive pump
CN103994105A (en) * 2014-04-29 2014-08-20 江苏大学 Impeller hydraulic power design method for low-cavitation non-load centrifugal pump
CN105298908A (en) * 2015-10-16 2016-02-03 江苏大学 High-cavitation-resistance centrifugal impeller hydraulic design method

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2589811A2 (en) * 2011-11-03 2013-05-08 Assoma Inc. Magnetic drive pump
CN103016396A (en) * 2012-12-11 2013-04-03 江苏大学 Centrifugal pump hydraulic design method controlling maximum flow by cavitation
CN103994105A (en) * 2014-04-29 2014-08-20 江苏大学 Impeller hydraulic power design method for low-cavitation non-load centrifugal pump
CN105298908A (en) * 2015-10-16 2016-02-03 江苏大学 High-cavitation-resistance centrifugal impeller hydraulic design method

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