Centrifugal Pump Vibrations: The Causes by Steven J. Hrivnak, P.E. - - PowerPoint PPT Presentation

centrifugal pump vibrations the causes
SMART_READER_LITE
LIVE PREVIEW

Centrifugal Pump Vibrations: The Causes by Steven J. Hrivnak, P.E. - - PowerPoint PPT Presentation

Centrifugal Pump Vibrations: The Causes by Steven J. Hrivnak, P.E. Associate Mechanical Engineer Tennessee Eastman Eastman Chemical Company EASTMAN FAULTS REPORTED OVER 3 YEARS Vibration: a measure of reliability! a measure of reliability!


slide-1
SLIDE 1

Centrifugal Pump Vibrations: The Causes

by Steven J. Hrivnak, P.E.

Associate Mechanical Engineer Tennessee Eastman Eastman Chemical Company

EASTMAN

slide-2
SLIDE 2

FAULTS REPORTED OVER 3 YEARS

slide-3
SLIDE 3

Vibration: Vibration: a measure of reliability! a measure of reliability!

Poorly installed and operated pumps average .178 in/sec overall vibration and have 6 months life. Properly installed pumps average .071 in/sec overall vibration and have 60 months life.

EASTMAN

slide-4
SLIDE 4

Three Basic Causes of Pump Three Basic Causes of Pump Vibrations: Vibrations:

  • Mechanically Induced

Mechanically Induced

  • System Induced

System Induced

  • Operation Induced

Operation Induced

slide-5
SLIDE 5

Mechanically Induced Mechanically Induced

  • Bad bearings

Bad bearings

  • Bent Shaft

Bent Shaft

  • Unbalanced Rotor

Unbalanced Rotor

  • Check Valve Installed Backwards

Check Valve Installed Backwards

  • Mis

Mis-Alignment

  • Alignment
  • Looseness

Looseness

  • Soft Foot

Soft Foot

  • Maximum Size Impeller

Maximum Size Impeller

slide-6
SLIDE 6
slide-7
SLIDE 7
slide-8
SLIDE 8

System Induced System Induced

  • Partially/Plugged Strainer

Partially/Plugged Strainer

  • Clogged Impeller or Suction Line

Clogged Impeller or Suction Line

  • Installation

Installation

slide-9
SLIDE 9

PIPING?

slide-10
SLIDE 10
slide-11
SLIDE 11
slide-12
SLIDE 12
slide-13
SLIDE 13
slide-14
SLIDE 14

Foundations Foundations and and Baseplates Baseplates

slide-15
SLIDE 15

The mass ratio must be 3:1 to The mass ratio must be 3:1 to minimize vibration minimize vibration

slide-16
SLIDE 16
slide-17
SLIDE 17
slide-18
SLIDE 18
slide-19
SLIDE 19
slide-20
SLIDE 20
slide-21
SLIDE 21
slide-22
SLIDE 22
slide-23
SLIDE 23
slide-24
SLIDE 24

Operationally Induced Operationally Induced

  • Cavitation

Cavitation

  • Flow

Flow

  • Speed

Speed

  • Insufficient Immersion of Suction Pipe or

Insufficient Immersion of Suction Pipe or Bell Bell

slide-25
SLIDE 25

Cavitation and Flow Cavitation and Flow

slide-26
SLIDE 26
slide-27
SLIDE 27

Operating Off The B.E.P.

Flow Head

High Temp. Rise Low Flow Cavitation Low Bearing and Seal Life Reduced Impeller Life Suction Recirculation Discharge Recirculation B.E.P. Low Bearing and Seal Life Cavation

slide-28
SLIDE 28
slide-29
SLIDE 29
slide-30
SLIDE 30
slide-31
SLIDE 31
slide-32
SLIDE 32
slide-33
SLIDE 33

You can’t run a pump with suction You can’t run a pump with suction and discharge valves closed! and discharge valves closed!

slide-34
SLIDE 34
slide-35
SLIDE 35

Minimum Flow Minimum Flow

1750 rpm 15-20% BEP Flow 1750 rpm 15-20% BEP Flow 3500 rpm 30-50% BEP Flow 3500 rpm 30-50% BEP Flow

slide-36
SLIDE 36

Maximum Flow Maximum Flow

110-115% BEP Flow 110-115% BEP Flow

slide-37
SLIDE 37
slide-38
SLIDE 38
slide-39
SLIDE 39
slide-40
SLIDE 40
slide-41
SLIDE 41

Speed Speed

slide-42
SLIDE 42
slide-43
SLIDE 43
slide-44
SLIDE 44

Suction Pipe Immersion Suction Pipe Immersion

slide-45
SLIDE 45
slide-46
SLIDE 46
slide-47
SLIDE 47

EASTMAN

Avoid Max Size Impellers Avoid Max Size Impellers

Conclusions Conclusions

slide-48
SLIDE 48

EASTMAN

Avoid Max Size Impellers Avoid Max Size Impellers Keep speed to 1750 max Keep speed to 1750 max

Conclusions Conclusions

slide-49
SLIDE 49

EASTMAN

Avoid Max Size Impellers Avoid Max Size Impellers Keep speed to 1750 max Keep speed to 1750 max Keep flow in design range Keep flow in design range

Conclusions Conclusions

slide-50
SLIDE 50

EASTMAN

Avoid Max Size Impellers Avoid Max Size Impellers Keep speed to 1750 max Keep speed to 1750 max Keep flow in design range Keep flow in design range Grout your baseplates Grout your baseplates

Conclusions Conclusions

slide-51
SLIDE 51

EASTMAN

Avoid Max Size Impellers Avoid Max Size Impellers Keep speed to 1750 max Keep speed to 1750 max Keep flow in design range Keep flow in design range Grout your baseplates Grout your baseplates Use proper piping Use proper piping

Conclusions Conclusions

slide-52
SLIDE 52

EASTMAN

Avoid Max Size Impellers Avoid Max Size Impellers Keep speed to 1750 max Keep speed to 1750 max Keep flow in design range Keep flow in design range Grout your Grout your baseplates baseplates Use proper piping Use proper piping Avoid hydraulically induced problems like Avoid hydraulically induced problems like cavitation, and suction and discharge re-circulation, cavitation, and suction and discharge re-circulation, submergence. submergence.

Conclusions Conclusions

slide-53
SLIDE 53
slide-54
SLIDE 54

5 PUMPS - 6 YR. MTBF 8 PUMPS - 5 YR. MTBF 15 PUMPS - 4 YR. MTBF 5 PUMPS - 6 YR. MTBF 8 PUMPS - 5 YR. MTBF 15 PUMPS - 4 YR. MTBF