Investigation of a Rotordynamic Instability in a High

Transcript Of Investigation of a Rotordynamic Instability in a High
Investigation of a Rotordynamic Instability in a High Pressure Centrifugal Compressor Due to Damper Seal Clearance Divergence
J. Jeffrey Moore, Ph.D. (‘91) Southwest Research Institute
April 11, 2019
Moore, J.J., Camatti, M., Smalley, A.J., Vannini, G.V., Vermin, L.L., 2006, Investigation of a Rotordynamic Instability in a High Pressure Centrifugal Compressor Due to Damper Seal Clearance Divergence, 7th International Conference on Rotor Dynamics, September 25-28, 2006, Vienna, Austria.
SOUTHWEST RESEARCH INSTITUTE®
Benefiting government, industry and the public through innovative science and technology
Divisions
Machinery Department
Applied Physics Chemistry & Chemical Engineering
Fuels & Lubricants
Intelligent Systems
Mechanical Engineering
Machinery Department
Defense & Intelligence Solutions
Space Science & Engineering
Powertrain Engineering
3
Mechanical Engineering Division
Engineering Dynamics
Machinery
Materials Engineering
Fluids Engineering
Structural Engineering
4
Machinery Department
Propulsion & Energy Machinery
Rotating Machinery Dynamics
60 engineers/technicians Design, analysis and testing Turbomachinery Thermodynamic cycle Performance testing Life cycle analysis/design Mechanical systems
(bearings, seals, etc.) Prototype development Computer aided engineering
CFD, FEA, CAD
Rotordynamics Fluid/thermal systems
Fluid Machinery Systems
Machinery Services
Power Cycle Machinery
Machinery Department Test Facilities
Multiphase Machinery Laboratory (B287)
Gas Turbine Laboratory (B129)
Recip Compression Laboratory
(B77)
Turbomachinery Laboratory (B278)
Operating Fluids: Air, CO2, N2 Multiphase with Air/H2O Drive power up to 4 MW Shaft speeds up to 140,000 rpm Machinery: centrifugal pumps &
compressors, reciprocating compressors, and small gas turbine engines
Case Study: Rotordynamic Instability
Two body compression train driven by 10 MW Gas Turbine through a gearbox
Gas gathering application that feeds large LNG plant in Nigeria
LP compressor is a 8 stage back-to-back design and is drivethrough
HP compressor is a 9 stage back-to-back design operating at about 10,000 rpm
Total train pressure ratio is 48:1
Instability experience on HP compressor during field start-up
Low Speed: 7585rpm
GAS TURBINE PGT10B
Gear Box
High Speed: 9198rpm
CE/ COLPCASING 2BCL458
CE/ COHPCASING 2BCL459/ A
Tripped on site
Original Compressor Seal Designs
LP Compressor:
Tooth-on-stator labyrinth seal at both impeller eye and center balance piston locations
Shunt injection on center balance piston No swirl brakes
HP Compressor
Honeycomb damper seal used at center balance piston with No swirl brake or shunt injection on any seal
Design of compressor predated more recent experience with adverse effects of damper seals
Design Pressure P1=22 bar (319 psi) P2=133 bar (1930 psi)
Maximum Discharge Pressure 189 bar (2740 psi) (Maximum Continuous Speed & Near Surge)
Experience Chart
LP and HP compressor plotted on Fulton experience chart Both machines within experience limits
MCS / NC1
4
CRITICAL
3.5
3
LP unit
2.5 API level 1-2
2
GE experience limit
HP unit
1.5
SAFE REGION
WARNING
1
1
10
100
1000
Gas mean density (kg/m3)
Site Description
Site located near the Niger Delta in Nigeria Gas is used to feed large LNG plant Instability not discovered until field start-up since units were not
full load tested at the factory
J. Jeffrey Moore, Ph.D. (‘91) Southwest Research Institute
April 11, 2019
Moore, J.J., Camatti, M., Smalley, A.J., Vannini, G.V., Vermin, L.L., 2006, Investigation of a Rotordynamic Instability in a High Pressure Centrifugal Compressor Due to Damper Seal Clearance Divergence, 7th International Conference on Rotor Dynamics, September 25-28, 2006, Vienna, Austria.
SOUTHWEST RESEARCH INSTITUTE®
Benefiting government, industry and the public through innovative science and technology
Divisions
Machinery Department
Applied Physics Chemistry & Chemical Engineering
Fuels & Lubricants
Intelligent Systems
Mechanical Engineering
Machinery Department
Defense & Intelligence Solutions
Space Science & Engineering
Powertrain Engineering
3
Mechanical Engineering Division
Engineering Dynamics
Machinery
Materials Engineering
Fluids Engineering
Structural Engineering
4
Machinery Department
Propulsion & Energy Machinery
Rotating Machinery Dynamics
60 engineers/technicians Design, analysis and testing Turbomachinery Thermodynamic cycle Performance testing Life cycle analysis/design Mechanical systems
(bearings, seals, etc.) Prototype development Computer aided engineering
CFD, FEA, CAD
Rotordynamics Fluid/thermal systems
Fluid Machinery Systems
Machinery Services
Power Cycle Machinery
Machinery Department Test Facilities
Multiphase Machinery Laboratory (B287)
Gas Turbine Laboratory (B129)
Recip Compression Laboratory
(B77)
Turbomachinery Laboratory (B278)
Operating Fluids: Air, CO2, N2 Multiphase with Air/H2O Drive power up to 4 MW Shaft speeds up to 140,000 rpm Machinery: centrifugal pumps &
compressors, reciprocating compressors, and small gas turbine engines
Case Study: Rotordynamic Instability
Two body compression train driven by 10 MW Gas Turbine through a gearbox
Gas gathering application that feeds large LNG plant in Nigeria
LP compressor is a 8 stage back-to-back design and is drivethrough
HP compressor is a 9 stage back-to-back design operating at about 10,000 rpm
Total train pressure ratio is 48:1
Instability experience on HP compressor during field start-up
Low Speed: 7585rpm
GAS TURBINE PGT10B
Gear Box
High Speed: 9198rpm
CE/ COLPCASING 2BCL458
CE/ COHPCASING 2BCL459/ A
Tripped on site
Original Compressor Seal Designs
LP Compressor:
Tooth-on-stator labyrinth seal at both impeller eye and center balance piston locations
Shunt injection on center balance piston No swirl brakes
HP Compressor
Honeycomb damper seal used at center balance piston with No swirl brake or shunt injection on any seal
Design of compressor predated more recent experience with adverse effects of damper seals
Design Pressure P1=22 bar (319 psi) P2=133 bar (1930 psi)
Maximum Discharge Pressure 189 bar (2740 psi) (Maximum Continuous Speed & Near Surge)
Experience Chart
LP and HP compressor plotted on Fulton experience chart Both machines within experience limits
MCS / NC1
4
CRITICAL
3.5
3
LP unit
2.5 API level 1-2
2
GE experience limit
HP unit
1.5
SAFE REGION
WARNING
1
1
10
100
1000
Gas mean density (kg/m3)
Site Description
Site located near the Niger Delta in Nigeria Gas is used to feed large LNG plant Instability not discovered until field start-up since units were not
full load tested at the factory