Sulzer ISO 13709 (API 610) Type BB5 Barrel Pumps
Sulzer Pumps
The Heart of Your Process
Long History of Barrel Pumps
Sulzer Pumps
GSG Sales Presentation | slide 2
Barrel Pumps: Diffuser Style
Sulzer Pumps
45 MW SuperCritical Boiler Feed GSG Sales Presentation | slide 3
Types of Horizontal Multistage Pumps Volute Volute - Horizontal Horizontal Split Split
Sulzer Pumps
Diffuser Diffuser - Segmental Segmental Ring
Volute Barrel
BB3 BB5
BB4 – Not used used on H.C. H.C.
Diffuser Barrel Casing BB5
High Speed Diffuser Barrel BB5
GSG Sales Presentation | slide 4
Volute vs. Diffuser Casings Radial loads increase at lower flow, and at flow rates beyond best efficiency point.
Sulzer Pumps
Single Volute Casing
The result is an unbalanced radial load on the rotating element. Small, low flow pumps have relatively small radial loads.
FR
GSG Sales Presentation | slide 5
Volute vs. Diffuser A dual volute casing has an additional passageway 180º from the main throat area which will almost balance the generated radial force. Horizontally split, dual Volute Multistage Pumps have 1 throat are in the top half, 1 in the bottom half - to balance radial forces.
Sulzer Pumps
Dual Volute Casing
F R~ 0
GSG Sales Presentation | slide 6
MultiStage Dual (MSD) Volute
Sulzer Pumps
Volute throat in top half of casing. Volute throat in bottom half is on opposite side for radial force balance.
Top Half Casing
Bottom Half Casing GSG Sales Presentation | slide 7
Volute vs. Diffuser A diffuser has multiple discharge passageways with equal area distributed throughout the circumference resulting in radial load balance.
Sulzer Pumps
Diffuser Casing
F R= 0
GSG Sales Presentation | slide 8
Diffusers
Sulzer Pumps
Diffuser – Discharge Side
Diffuser – Suction Side
Impeller runs in center Return Channels feed next stage
Stage casings GSG Sales Presentation | slide 9
Axial Thrust Development
Sulzer Pumps
Opposed Impeller Design
Fr Total = 0 Fr 1st Pd 1st
X
Fr xst
X
Pd 1st Pd xst
X
X
Pd xst
Unbalanced pressure distribution on impellers results in a thrust in the direction of suction.
Opposed impeller design offsets the unbalanced pressure distribution (thrust) effectively balancing axial thrust. When there are odd number of stages, thrust is handled by adjusting the diameter of the throttle bushing with residual handled by a thrust bearing. GSG Sales Presentation | slide 10
Axial Thrust Development
Sulzer Pumps
Inline Rotor Stack
Fr Total = Fr 1st+Fr xst Fr xst
Fr 1st Pd 1st
X
FDrum ~ 85% Fr Total
X
Pd 1st Pd xst
X
X
FDrum Pd xst Ps
Unbalanced pressure distribution on impellers results in thrust in the direction of suction.
Stacked impeller design results in adding thrust in the direction of suction.
Developed thrust must be compensated by a hydraulic balancing device. Residual thrust is handled by a thrust bearing. GSG Sales Presentation | slide 11
Axial Thrust Compensation Balance Drum
Sulzer Pumps
Balances 85 - 90% of generated thrust. Residual thrust handled by a thrust bearing.
With inline rotor stack, this is most reliable design for transient conditions (start up and run down, temperature changes, daily starts and stops).
Easy and safe axial rotor setting due to radial gap as compared to axial gap (explained on next slide).
Rotor is fixed in the axially position by thrust bearing.
Higher amount of leakage - less efficient.
Close clearance pressure breakdown
PSuction
Balance Drum
PDischarge
Balance Drum Liner
GSG Sales Presentation | slide 12
Axial Thrust Compensation balance disk - Not allowed by ISO 13709 (API 610)
Axial gap will adjust in response to thrust changes
PSuction
Balance Disk
Balances 100% of the generated thrust.
No thrust bearing required.
Rotor floats axially for proper operation.
Least amount of leakage - higher efficiency.
Disc lift off device required for frequent starts and stops
ISO 13709 (API 610) Para. 5.7.1 requires radial running clearance be used for axial thrust balance. That precludes the use of this device.
Potential for contact causes this design to be considered less forgiving than balancing drum
PDischarge
Counter Disk
Sulzer Pumps
GSG Sales Presentation | slide 13
Inline Impellers vs. Opposed Impellers
Sulzer Pumps
Sulzer GSG: Inline diffuser Barrel Pump
GSG Back-to-Back diffuser Barrel Pump
Sulzer CP: Opposed Impeller Volute Barrel Pump Note: All are ISO 13709 (API 610) type BB5 GSG Sales Presentation | slide 14
Inline vs. Opposed Rotor Stack
Sulzer Pumps
Direct drive, inline diffuser barrel pumps are the least expensive barrel pumps to build. High Speed inline pumps require tilting pad thrust bearings and lube system, high speed seals, VFD or gear speed increaser, etc. which add to the cost.
GSG Sales Presentation | slide 15
Inline vs. Opposed Rotor Stack
Sulzer Pumps
ISO 13709 (API 610) requires stable rotordynamics with 2 times normal ISO 13709 (API 610) specified wear ring clearances. Back to back diffuser stack is often used on smaller pumps or high energy pumps with many stages where rotordynamics require a midspan bearing. The Sulzer Thunderhorse 650 Bar, 13MW injection pumps are designed in this manner.
GSG Sales Presentation | slide 16
The “K” factor – large barrel pumps
Sulzer Pumps
“K factor” 2000
120 K Factor
1800
Shaft Span, in.
1600 1400 1200 1000
Back to Back GSG, HPCP or CP
• Rotor Wt. in lbs. 100
• Shaft Span, in.
80
• Shaft Dia. in.
60
K=(W*L^3/D^4)^0.5
800 40
600 400
20
200 0
0 Inline 3.38
Inline 4.25
B-B 3.38
Some say K factor of = 1200 is good; “Semi-stiff shaft” is another term they use
Type / shaft size, inches Lower “K” factor is generally better. It can be achieved either with fewer stages & large high speed shaft on inline rotor, or back-to-back rotor and direct drive GSG Sales Presentation | slide 17
Rotor Sag
Sulzer Pumps
For small pumps with many stages, the rotor will rest on center bushing. When the pump starts, Lomakin effect lifts rotor for noncontact running.
Non-galling material selection is important. Sulzer uses a stellite coated, or nitrided throttle bushing and center bushing on opposed impeller pumps.
GSG Sales Presentation | slide 18
Inline vs. Opposed Rotor Stack
Sulzer Pumps
Back to Back (Opposed impeller) diffuser or volute design is also used in remote locations where customers prefer not to have a lube system to maintain. Opposed impellers balance axial thrust and may allow use of an antifriction thrust bearing. Back to Back (Opposed impeller) volute multistage barrel pumps are used in abrasive services where 2 large throat diameters are preferred in lieu of many smaller diffuser throats. The inner volute casing is larger in diameter than diffusers so volute style barrel pumps often cost more than diffuser style
GSG Sales Presentation | slide 19
Direct Drive vs. High Speed Flow of a centrifugal pump varies directly with RPM. Head produced by a stage varies as the square of the RPM.
Sulzer Pumps
High Speed, VFD or Gear; fewer stages
In other words, to make the same head, operating a smaller pump 42% faster would make the same head with half the number of stages. However, some customers prefer direct drive 2 pole pumps for reliability and reduced items to maintain. Direct drive pumps often do not require these costly accessories:
Low Speed, Direct Drive; more stages
- lube system & sleeve/pivot shoe bearings - more extensive instrumentation - gear increaser - special mechanical seals
GSG Sales Presentation | slide 20
Cartridge vs Non-cartridge designs
Sulzer Pumps
A “Cartridge” design barrel pump allows the inboard bearing housing and seal chamber to be withdrawn from the barrel with the bundle. On small pump sizes this is impractical because the IB bearing housing is larger than the barrel opening on the IB end. On smaller pumps, a “Non-Cartridge” design barrel pump requires the inboard bearing housing and seal chamber to be removed before withdrawal of the bundle from the outboard end. That adds a little time to disassembly/reassembly but parts are relatively small and can often be handled by hand GSG Sales Presentation | slide 21
High Temperature – Thermal Expansion
To accommodate axial growth due to high temperature operation the suction end of the barrel is equipped with a pin which fixes the Drive End of the pump.
Sulzer Pumps
The discharge end is equipped with a key slot which will allows the barrel to expand in the direction of the NDE end. The barrel to pedestal bolts are torqued to a specific value to accommodate the axial growth.
GSG Sales Presentation | slide 22
Barrel Head Closure Methods
Sulzer Pumps
Studs & Nuts – Most common – requires stretching or torquing Supernuts – more expensive, no stretching; hand tool torquing or Sulzer’s Patented Twist Lock On lower temperature services, to speed overhaul, some customers prefer Sulzer’s patented Twist Lock barrel end cover design – no studs/nuts and no torquing required.
Head Installed
Head partially rotated
Head Rotated & Locked
GSG Sales Presentation | slide 23
Sulzer Pumps
GSG: SMALLER SIZES
50 Hz, 2 pole motor speed
Gray or white are inline rotor
Light blue are only available in back-to-back rotor
GSG Sales Presentation | slide 24
Sulzer Pumps
GSG: LARGER SIZES
50 Hz, 2 pole motor speed
Gray or white are inline rotor
Light blue are only available in back-to-back rotor
GSG Sales Presentation | slide 25
Sulzer Pumps
GSG: SMALLER SIZES
60 Hz, 2 pole motor speed
Gray or white are inline rotor
Light blue are only available in back-to-back rotor
GSG Sales Presentation | slide 26
Sulzer Pumps
GSG: LARGER SIZES
60 Hz, 2 pole motor speed
Gray or white are inline rotor
Light blue are only available in back-to-back rotor
GSG Sales Presentation | slide 27
Hydraulics
Sulzer Pumps
A double suction impeller reduces the NPSHr by about 30%
Double suction first stage available on larger sizes
GSG Sales Presentation | slide 28
Impellers and Diffusers
Sulzer Pumps
Hydraulic layout Multiple hydraulic impeller & diffuser sets per pump size Mixing of impeller / diffuser hydraulics in single pump is possible Double suction first stage is available in larger size pumps
Dynamic balanced impellers & rotor > 3 stages Radial load is balanced
GSG Sales Presentation | slide 29
Mixing of Impeller Hydraulics with Interstage Bleed Off Pumped Medium Density Temperature kinem. Viscosity Head (design) Capacity (design) Total efficiency Pump Power
: : : : : : : :
Boiler Feed Water 909.2 kg/m³ 318 °F 0.19 mm²/s 4,600 ft 900 gpm 75.8 % 1,350 HP
0 0 0 6
Sulzer Pumps
Speed : 3570 rpm Stage Number : 8 nq : 20.0 Impeller Set : B/B/B Basis 4335.11.11/2 & 4335.11.11/2 & 4335.11.11/2 Extraction head : 1,268 ft Extraction capacity : 250 gpm
MD 100-300 / 8
Note the all “B”
Tender : /1 impeller hydraulics Characteristic : TS/1 Impeller diameter : 11.1 inch Impeller dia. (max) : 11.8 inch : 19 ft NPSHR
Note efficiency = 75.8% and power is 1,350 hp
0 0 0 5
0 0 0 4
] t f 0 [ 0 0 H 3 0 0 0 2
RATED Max. ∅
By mixing impeller hydraulics efficiency and power can be optimized 2 Max.
0 0 0 1
∅
RATED
0 0 gpm
200 gpm
400 gpm
600 gpm
800 gpm
1000 gpm
1200 gpm
1400 gpm
1600 gpm
1800 gpm
2000 gpm
GSG Sales Presentation | slide 30
Mixing of Impeller Hydraulics with Interstage Bleed Off Pumped Medium Density Temperature kinem. Viscosity Head (design) Capacity (design) Total efficiency Pump Power
: : : : : : : :
Boiler Feed Water 909.2 kg/m³ 318 °F 0.19 mm²/s 4,600 ft 900 gpm 78.7 % 1,301 HP
0 0 0 6
Sulzer Pumps
Speed : 3570 rpm Stage Number : 9 nq : 20.0 Impeller Set : B/B/S Basis 4335.11.11/2 & 4335.11.11/2 & 4335.11.21/1 Extraction head : 1,268 ft Extraction capacity : 250 gpm
MD 100-300 / 9
Now the “B” hydraulics have Tender : /1 with “S” after been replaced Characteristic : TS/1 thediameter interstage bleed Impeller : 10.9 inch off. Impeller dia. (max) : 11.0 inch : 19 ft NPSHR
Efficiency now = 78.7% and power is 1,301 hp (49 hp reduction)
0 0 0 5
0 0 0 4
] t f 0 [ 0 0 3 H 0 0 0 2
RATED Max. ∅
By mixing impeller hydraulics efficiency and power can be optimized 2 Max. ∅
0 0 0 1
RATED
0 0 gpm
200 gpm
400 gpm
600 gpm
800 gpm
1000 gpm
1200 gpm
1400 gpm
1600 gpm
1800 gpm
GSG Sales Presentation | slide 31
Bearing Type Selection
Sulzer Pumps
) m 5000 p r 0 0 4000 6 3 ( P 3000 H P E 2000 B @1000 r e w o 0 P
% 0 2
Pivot Shoe Thrust & Sleeve Radial – Lube System required
Anti-Friction Thrust & Sleeve Radial – Ring Oil Lube
Anti-Friction Thrust & Radial – Ring Oil Lubrication
% 0 3
% 0 4
% 0 5
% % % % % 0 0 0 0 0 0 1 2 3 9 1 1 1 1 Pump Flow - % of BEP
% 0 6
% 0 7
% 0 8
Exact bearing system will depend upon application
GSG Sales Presentation | slide 32
Anti-Friction with Ring Oil Lubrication
Sulzer Pumps
Radial Bearing
Thrust Bearing
Cooling Fan
Oil Rings
Oil Reservoir
Ring Oil Lubrication – Oil rings rotate with shaft, dip down into an oil reservoir and “throw” oil onto bearings. Grooves or channels are located in the bearing housing to distribute oil throughout the bearing(s). Shaft mounted cooling fans provide cooling up to a liquid temperature of 177 o C (350 F). °
GSG Sales Presentation | slide 33
Anti-Friction Thrust & Sleeve Radial Bearings with Ring Oil Lubrication (GSG Back-to-Back only) Thrust Bearing
Sulzer Pumps
Radial Bearings
Cooling Fan Oil Rings Oil Reservoir
Ring Oil Lubrication – Oil rings rotate with shaft, dip down into an oil reservoir and “throw” oil onto bearings. Grooves or channels are located in the bearing housing to distribute oil throughout the bearing(s). Shaft mounted cooling fans provide cooling up to a liquid temperature of 177o C (350 F). Optional water cooled finned tubing is available. °
GSG Sales Presentation | slide 34
Double Acting Tilting Pad Thrust & Sleeve Radial Bearings with Force Feed Oil Lubrication Double Acting, Tilting Pad Thrust Bearing
Sulzer Pumps
Sleeve Radial Bearings
Shaft Driven Oil Pump
Forced Feed Lubrication – Bearing lubrication is provided by an external lube oil system. Depending on specification requirements lube oil systems can be very basic or very elaborate. Standard lube system could cost < 20,000 Euro/USD. ISO 13709 (API 610) Lube system is typically 40,000 Euro/USD. ISO 10438 (API 614) could be 3 to 4 times that cost. If customers specify lube systems, they often specify bearing RTD’s and vibration measurement instrumentation which adds further cost. GSG Sales Presentation | slide 35
Journal and Thrust Bearing Arrangement
Sulzer Pumps
Sleeve Bearings
GSG Sales Presentation | slide 36
Tilting Pad Thrust Bearing Arrangement
Sulzer Pumps
Thrust Bearing Lubrication An “oil wedge” builds up between each stationary thrust pad and the rotating collar, and no metal-to-metal contact occurs during normal operation.
The babbit lining of the pads is designed to be tolerant of any minute particles of grit that may get through.
GSG Sales Presentation | slide 37
Journal and Thrust Bearing Arrangement
Sulzer Pumps
Double Acting “Pivot Shoe” or “Tilting Pad” Thrust Bearing
GSG Sales Presentation | slide 38
Forced Feed Lube Oil Systems
Sulzer Pumps
GSG Sales Presentation | slide 39
Seal Chambers & Jackets
Sulzer Pumps
Seal Chambers are designed to ISO 13709 (API 610) Table 6 dimensions and features. ISO 21049 (API 682) single, double or tandem seals are available
Seal Chamber cooling or heating jackets are available on this model pump.
GSG Sales Presentation | slide 40
Seal Flush Plans
Sulzer Pumps
TI
FO
FI
Q/D
A variety of seal flush plans are available
GSG Sales Presentation | slide 41
Instrumentation - options NDE X-Y Shaft vibration
Balance Leakoff flow
NDE Bearing temperature
In lieu of more expensive X-Y probes & proximitors, normally bearing bracket velocity is adequate for direct drive pumps
Sulzer Pumps
DE Shaft vibration
DE Bearing temperature
Barrel Temperature, Bottom & Top (for hot standby) GSG Sales Presentation | slide 42
Vibration Instrumentation
Sulzer Pumps
Firm contact from shaft to bearing frame
Velomitors
With anti-friction bearings the shaft is firmly connected to the bearing frame via the bearings. Any vibration of the rotating element will be transferred from the shaft to the bearings to the bearing housings and there will not be any relative movement of the shaft to the bearing housings. Vibration is measured by the relative RMS velocity or acceleration of the bearing frame - by either velomitors or accelerometers. GSG Sales Presentation | slide 43
Vibration Instrumentation
Sulzer Pumps
Film contact from shaft to bearing frame
Probes and Proximitors
With sleeve bearings, the shaft “floats” on a film of oil and is free to move within the clearance of the sleeve bearings. This allows the rotating element to vibrate within the sleeve bearings while the actual bearing frame may not vibrate at all. Vibration is the relative movement of the shaft within the bearing frame. Probes are mounted with very close proximity to the shaft (Bently Nevada type systems) to detect displacement movement. GSG Sales Presentation | slide 44
API Material Classes
Sulzer Pumps
Material classes and abbreviations Part
S-1
S-5
S-6
C-6
CS/Cast Iron
CS/CS
CS/12% Chrome
12% Chrome/ 12% Chrome
Pressure Casing
Carbon Steel
Carbon Steel
Carbon Steel
12% Chrome
Inner Case
Cast Iron
Carbon Steel
12% Chrome
12% Chrome
Impeller
Cast Iron
Carbon Steel
12% Chrome
12% Chrome
Case Wear Rings
Cast Iron
12% Chrome Hardened
12% Chrome Hardened
12% Chrome Hardened
Impeller Wear Rings
Cast Iron
12% Chrome Hardened
12% Chrome Hardened
12% Chrome Hardened
Shaft
Carbon Steel
AISI 4140
AISI 4140
12% Chrome
Throat Bushings
Cast Iron
12% Chrome Hardened
12% Chrome Hardened
12% Chrome Hardened
Interstage Sleeves
Cast Iron
12% Chrome Hardened
12% Chrome Hardened
12% Chrome Hardened
Interstage Bushings
Cast Iron
12% Chrome Hardened
12% Chrome Hardened
12% Chrome Hardened
Case and Gland Studs
AISI 4140
AISI 4140
AISI 4140
AISI 4140
GSG Sales Presentation | slide 45
API Material Classes
Sulzer Pumps
Material classes – cont’d. A-8
D-1
D-2
316SS/316SS
Duplex SS
Super Duplex
Part
Pressure Casing
316L SS
Duplex
S.D.
Inner Case
316L SS
Duplex
S.D.
Impeller
316L SS
Duplex
S.D.
Case Wear Rings
Duplex SS
Duplex
S.D.
Impeller Wear Rings
316l SS HF
Duplex
S.D.
Shaft
Duplex SS
Duplex
S.D.
Throat Bushings
316L SS HF
Duplex
S.D.
Interstage Sleeves
316L SS
Duplex
S.D.
Interstage Bushings
316L SS HF
Duplex
S.D.
Case and Gland Studs
AISI 4140
AISI 4140
AISI 4140 GSG Sales Presentation | slide 46
Pre-Warming
Sulzer Pumps
On Horizontally split multistage pumps, the casing is not uniformly thick. It has very heavy cross sections that take time to reach operating temperature. The rotor & lower half casing gets hot and expands quickly.
Pre-warming of this style pump is required. Maximum ramp-up temperature is 10º C (20ºF) per minute and 110ºC (200 ºF) instantaneous thermal shock
GSG Sales Presentation | slide 47
Pre-Warming
Sulzer Pumps
The Sulzer GSG Pumps are designed with uniform thicknesses and clearances on the inner case components to minimize distortion. Warmup is not required on many applications < 260 oC (500oF). Above that temperature, the barrel drains can be used to uniformly warm the pump, or maintain hot standby. Barrel RTD’s can provide indication of uniform temperatures.
GSG Sales Presentation | slide 48
GSG Cross Section and Features Radial split identical stage casings, diffusers and impellers
Sulzer Pumps
Interstage bleed connections available
Low NPSH 1st stage impeller. Double suction available.
Thrust bearing - antifriction or double acting tilting pad. Radial bearing - sleeve or anti-friction.
Studs & Nuts, Super-nuts or Twist Lock barrel closure on Back-to-Back only
Bearings protected by Labyrinth type oil seals
Hydraulic balance device is Drum type
Stacked rotor design with staggered keyways to provide positive torque to impellers
Radial Split barrel casing with confined gasket. Either casting or forging available.
GSG Sales Presentation | slide 49
Pictures
Sulzer Pumps
GSG Boiler Feed pump with speed increasing gearbox, lube system, suction strainer and automatic recirculation control valve GSG Sales Presentation | slide 50
Pictures
Sulzer Pumps
GSG portion of hydrotreater train (GSG pump, clutch, MSD-T power recovery turbine) with full instrumentation and insulation. Sleeve bearing RTD, Active Thrust RTD, Inactive thrust RTD, X-Y vibration probes, Key phasor.
GSG Sales Presentation | slide 51