SS1701-CS171121
CoppellInterceptorBypass
Coppell,TX
11-21-17
EGR17BPP031
TemporaryBypassCalculations
EGR17BPP031
Temporary BypassCalculations
November 21, 2017
Customer: SJ Louis Construction
Project: Coppell Interceptor Bypass
Location: Coppell, TX
Equipment:
Pump(s): Pioneer Pump PP1212S17
Mody G502T Submersible Pump
AMT Pump 576X-95 C Submersible Pump
AMT Pump 576X-95 D Submersible Pump
Piping: 18”SDR17 HDPE (Suction)
18” SDR26 HDPE (Discharge)
24” SDR26 HDPE (Discharge)
4” Discharge Hose(Discharge)
6” Discharge Hose(Discharge)
By-pass set-up:
Bypass 1
Bypass 1will pull out of MH-3490E as indicated in Bypass 1 Plan View (sheet 2)before being
pumped at most200LF and discharging into MH-3480E. The bypass pipeline is to consist of
approximately 20 LF of 18” SDR17 HDPE suction pipeand no more than 200LF of 24”
SDR26 HDPE discharge pipe.
The maximum flow rate has been predicted to be no more than 25.4MGD (17640 GPM)by
contractor observation. Discharge static head has been assumed to be negligible while
maximum suction lift has been assumed to be no more than 12’.Discharge static head and
suction lift to be verified before work begins.
Primary and backup pumps to be combined into single discharge header via manifold - refer to
Pump Staging Detail A (sheet 18)of drawings.
Primary Pump(s): (4)Pioneer Pump PP1212S17
Bypass 2
Bypass 2 will pull out of MH-3505Eas indicated in Bypass 2 Plan View (sheet 3)before being
pumped at most 725 LFand discharging into MH-3500E. The bypass pipeline is to consist of
approximately 725 LF of 6” discharge hose.
The maximum flow rate has been predicted to be no more than 0.58 MGD (401 GPM)through
contractor observation. Discharge static head has been determined to be 9.5’.
Primary Pump(s): Mody G502T Submersible Pump or Equivalent
Bypass 3
Bypass 3 will pull out of MH-850Eas indicated in Bypass 3 Plan View (sheet 4)before being
pumped at most 50 LFand discharging into MH-3510E. The bypass pipeline is to consist of
approximately 50 LF of 6” discharge hose.
The maximum flow rate has been predicted to be no more than 0.54 MGD (374 GPM)through
contractor observation. Discharge static head has been determined to be 10.8’.
Primary Pump(s): Mody G502T Submersible Pump or Equivalent
Bypass 4
Bypass 4 will pull out of MH-865Eas indicated in Bypass 4 Plan View (sheet 5)before being
pumped at most 100 LFand discharging into MH-3535E. The bypass pipeline is to consist of
approximately 100 LF of 4” discharge hose.
The maximum flow rate has been predicted to be no more than 0.27 MGD (187 GPM)through
contractor observation. Discharge static head has been determined to be 11.1’.
Primary Pump(s): AMT Pump 576X-95C Submersible Pump or Equivalent
Bypass 5
Bypass 5 will pull out of MH-870Eas indicated in Bypass 5 Plan View (sheet 6)before being
pumped at most 75 LFand discharging into MH-3535E. The bypass pipeline is to consist of
approximately 75 LF of 4” discharge hose.
The maximum flow rate has been predicted tobe no more than 0.27 MGD (187 GPM)through
contractor observation. Discharge static head has been determined to be 11.1’.
Primary Pump(s): AMT Pump 576X-95C Submersible Pump or Equivalent
Bypass 6
Bypass 6 will pull out of MH-880Eas indicated in Bypass 6 Plan View (sheet 7)before being
pumped at most 75 LFand discharging into MH-3550E. The bypass pipeline is to consist of
approximately 75 LF of 4” discharge hose.
The maximum flow rate has been predicted to be no more than 0.27 MGD (187 GPM)through
contractor observation. Discharge static head has been determined to be 13.5’.
Primary Pump(s): AMT Pump 576X-95C Submersible Pump or Equivalent
Bypass 7
Bypass 7 will pull out of MH-893Eas indicated in Bypass 7 Plan View (sheet 8)before being
pumped at most 300 LFand discharging into MH-3555E. The bypass pipeline is to consist of
approximately 300 LF of 4” discharge hose.
The maximum flow rate has been predicted to be no more than 0.27 MGD (187 GPM)through
contractor observation. Discharge static head has been determined to be 14.3’.
Primary Pump(s): AMT Pump 576X-95DSubmersible Pump or Equivalent
Bypass 8
Bypass 8 will pull out of MH-A6 as indicated in Bypass 8Plan View (sheet 9)before being
pumped at most 50LFand discharging into MH-B0.The bypass pipeline is to consist of
approximately 20 LF of 18” SDR17 HDPE suction pipeand no more than 50LF of 18”
SDR26 HDPE discharge pipe.
The maximum flow rate has been indicated to be no more than 20.4 MGD (14167 GPM).
Discharge static head has been determined to be negligible whilemaximum suction lift has been
determined to be no more than 10.5’.
Pumps to be utilized in (2) independent systems -refer to Pump Staging Detail B(sheet 19)of
drawings.
Primary Pump(s):(2) PP1212S17
Floats and Alarms
Backup pumpswill be setup on high level floats to ensure flow demands are met in the case that
increased flow is encountered or the primary pump fails.
SpillProtection/Prevention/Response
All the discharge lines will be testedprior to starting, to identify leaks and all leaks corrected
prior toputting the bypass into operation. Upon startup, after running the system for 2 hours all
parts will betightened to ensure tightness. The city will be notified 48 hours prior to testing.
Pumps will be placed on Spill Guards on site to prevent damage in case of spill. In the event of a
majorbreak/spill, the pumps will be turned off immediately. A vacuum truck will be brought on
site to initiate theclean-up process under the direction of the regulatory body having jurisdiction
over this type ofspill.
Periodic disposal of accumulated rainwater in containment berms is responsibility of contractor.
This plan is written byUnited Rentals Pump Solutionsas general guidelines for the selection,
installation andoperation of this bypass pumping system. It is thecontractor'sresponsibility to
ensure adequatepumpingsystem, redundantpumping systems and proper equipment
maintenance is available to divertthe completesewer flow preventing any spills or
overflows.
Fluid Properties
Working Fluid=Water-
Average Fluid Temperature=68°F
Vapor Pressure=0.34psi
3
Density=1.94
slugs/ft
Specific Gravity=1.00-
2
Dynamic Viscosity=2.14
lb-sec/ft
f
2
Kinematic Viscosity=1.11
ft/sec
Btu/lb-°F
Specific Heat=1
m
Thermal Conductivity=0.351Btu/hr-ft-°F
Peak Flow Calculations
Flow Calculations assume pipe 2/3 filled
at flow velocity of 3 ft/s
6" Lateral Tie-In
Pipe Diameter=6in
2
Cross-Sectional Area=0.14
ft
Flow Velocity=3ft/s
3
Peak Flow Rate=0.417
ft/s
=187GPM
2" Lateral Tie-In
Pipe Diameter=2in
2
Cross-Sectional Area=0.02
ft
Flow Velocity=3ft/s
3
Peak Flow Rate=0.060
ft/s
=27GPM
Pipeline Specifications (Bypass 1)
Pipeline RunDiameter (in)SDRMaterial
Suction Piping=1817HDPE
Discharge Piping \[Pump -> Manifold\]=1826HDPE
Discharge Piping \[Manifold -> End\]=2426HDPE
Suction ComponentsAmount
90 Degree Elbow=3
45 Degree Elbow=0
Tee Thru Flow=0
Tee Branch Flow=0
Concentric Reducer=0
Gate Valve, Open=0
Swing Check Valve, Open=0
Angle Valve, Open=0
Globe Valve, Open=0
Discharge Components
90 Degree Elbow=6
45 Degree Elbow=4
Tee Thru Flow=0
Tee Branch Flow=2
Reducer=1
Gate Valve, Open=1
Swing Check Valve, Open=0
Angle Valve, Open=0
Globe Valve, Open=0
TDH Calculations (Bypass 1)
Suction \[MH-3490E -> Pump\]
Static Head=12ft
Flow Rate=4410GPM
Total Length=20ft
Total Equivalent Length=146ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=15.76in
Friction Head Loss=1.37ft
Total Dynamic Suction Head=13.37ft
Flow Velocity=7.25ft/s
Discharge\[Pump -> Manifold Inlet\]
Static Head=0ft
Flow Rate=4410GPM
Total Length=20ft
Total Equivalent Length=146ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=16.533in
Friction Head Loss=1.08ft
Total Dynamic Discharge Head=1.08ft
Flow Velocity=6.59ft/s
Discharge \[Manifold Inlet -> Manifold Outlet\]
Static Head=0ft
Flow Rate=17640GPM
Total Length=10ft
Total Equivalent Length=72ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=16.533in
Friction Head Loss=6.95ft
Total Dynamic Discharge Head=6.95ft
Flow Velocity=26.36ft/s
Discharge \[Manifold Outlet -> MH-3480E\]
Static Head=0ft
Flow Rate=17640GPM
Total Length=200ft
Total Equivalent Length=486ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=22.043in
Friction Head Loss=11.58ft
Total Dynamic Discharge Head=11.58ft
Flow Velocity=14.83ft/s
Total Dynamic Head=32.97ft
PP1212S17 Predicted Flow Rate=4410GPM
PP1212S17 Max Flow Rate=8800GPM
PP1212S17 Max TDH=90ft
Max Allowable Flow > Proposed Flow=
O.K.
Max Allowable TDH > Predicted TDH=
O.K.
Net Positive Suction Head (Bypass 1)
Site Elevation=500ft
Atmospheric Head=33.34ft
Static Head=12ft
Friction Head=1.37ft
Vapor Head=0.78ft
NPSH Available=19.19ft
NPSH Required=5.3ft
NPSH-A > NPSH-R=
O.K.
Surge Allowance (Bypass 1)
Fluid Bulk Modulus=300000psi
Pipe Effective Modulus=150000psi
Suction
Velocity Delta=7.25ft/s
Wave Celerity=837ft/s
Max Surge Pressure=82psi
Allowable Surge Pressure=250psi
P_max < P_allowable=
O.K.
Discharge
Velocity Delta=14.83ft/s
Wave Celerity=666ft/s
Max Surge Pressure=133psi
Allowable Surge Pressure=160psi
P_max < P_allowable=
O.K.
Pipeline Specifications (Bypass 2)
Pipeline RunDiameter (in)SDRMaterial
Discharge Piping=626HDPE
Discharge Components
90 Degree Elbow=6
45 Degree Elbow=4
Tee Thru Flow=0
Tee Branch Flow=0
Concentric Reducer=0
Gate Valve, Open=0
Swing Check Valve, Open=0
Angle Valve, Open=0
Globe Valve, Open=0
TDH Calculations (Bypass 2)
Discharge \[MH-3505E -> MH-3500E\]
Static Head=9.5ft
Flow Rate=401GPM
Total Length=725ft
Total Equivalent Length=847ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=6in
Friction Head Loss=10.25ft
Total Dynamic Discharge Head=19.75ft
Flow Velocity=4.55ft/s
Total Dynamic Head=19.75ft
Mody G502T Max Flow Rate=455GPM
Mody G502T Max TDH=22ft
Max Allowable Flow > Proposed Flow=
O.K.
Max Allowable TDH > Predicted TDH=
O.K.
Pipeline Specifications (Bypass 3)
Pipeline RunDiameter (in)SDRMaterial
Discharge Piping=6HoseComposite
Discharge Components
90 Degree Elbow=6
45 Degree Elbow=4
Tee Thru Flow=0
Tee Branch Flow=0
Concentric Reducer=0
Gate Valve, Open=0
Swing Check Valve, Open=0
Angle Valve, Open=0
Globe Valve, Open=0
TDH Calculations (Bypass 3)
Discharge \[MH-850E -> MH-3510E\]
Static Head=10.8ft
Flow Rate=374GPM
Total Length=50ft
Total Equivalent Length=172ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=6in
Friction Head Loss=1.83ft
Total Dynamic Discharge Head=12.63ft
Flow Velocity=4.24ft/s
Total Dynamic Head=12.63ft
Mody G502T Max Flow Rate=500GPM
Mody G502T Max TDH=14ft
Max Allowable Flow > Proposed Flow=
O.K.
Max Allowable TDH > Predicted TDH=
O.K.
Pipeline Specifications (Bypass 4)
Pipeline RunDiameter (in)SDRMaterial
Discharge Piping=4HoseComposite
Discharge Components
90 Degree Elbow=6
45 Degree Elbow=4
Tee Thru Flow=0
Tee Branch Flow=0
Concentric Reducer=0
Gate Valve, Open=0
Swing Check Valve, Open=0
Angle Valve, Open=0
Globe Valve, Open=0
TDH Calculations (Bypass 4)
Discharge \[MH-865E -> MH-3535E\]
Static Head=11.1ft
Flow Rate=187GPM
Total Length=100ft
Total Equivalent Length=282ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=4in
Friction Head Loss=5.98ft
Total Dynamic Discharge Head=17.08ft
Flow Velocity=4.77ft/s
Total Dynamic Head=17.08ft
AMT Pump 576X-95C Max Flow Rate=195GPM
AMT Pump 576X-95C Max TDH=17.5ft
Max Allowable Flow > Proposed Flow=
O.K.
Max Allowable TDH > Predicted TDH=
O.K.
Pipeline Specifications (Bypass 5)
Pipeline RunDiameter (in)SDRMaterial
Discharge Piping=4HoseComposite
Discharge Components
90 Degree Elbow=6
45 Degree Elbow=4
Tee Thru Flow=0
Tee Branch Flow=0
Concentric Reducer=0
Gate Valve, Open=0
Swing Check Valve, Open=0
Angle Valve, Open=0
Globe Valve, Open=0
TDH Calculations (Bypass 5)
Discharge \[MH-870E -> MH-3535E\]
Static Head=11.1ft
Flow Rate=187GPM
Total Length=75ft
Total Equivalent Length=257ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=4in
Friction Head Loss=5.45ft
Total Dynamic Discharge Head=16.55ft
Flow Velocity=4.77ft/s
Total Dynamic Head=16.55ft
AMT Pump 576X-95C Max Flow Rate=195GPM
AMT Pump 576X-95C Max TDH=17.5ft
Max Allowable Flow > Proposed Flow=
O.K.
Max Allowable TDH > Predicted TDH=
O.K.
Pipeline Specifications (Bypass 6)
Pipeline RunDiameter (in)SDRMaterial
Discharge Piping=4HoseComposite
Discharge Components
90 Degree Elbow=6
45 Degree Elbow=4
Tee Thru Flow=0
Tee Branch Flow=0
Concentric Reducer=0
Gate Valve, Open=0
Swing Check Valve, Open=0
Angle Valve, Open=0
Globe Valve, Open=0
TDH Calculations (Bypass 6)
Discharge \[MH-880E -> MH-3550E\]
Static Head=13.5ft
Flow Rate=187GPM
Total Length=75ft
Total Equivalent Length=257ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=4in
Friction Head Loss=5.45ft
Total Dynamic Discharge Head=18.95ft
Flow Velocity=4.77ft/s
Total Dynamic Head=18.95ft
AMT Pump 576X-95C Max Flow Rate=190ft
AMT Pump 576X-95C Max TDH=19.2ft
Max Allowable Flow > Proposed Flow=
O.K.
Max Allowable TDH > Predicted TDH=
O.K.
Pipeline Specifications (Bypass 7)
Pipeline RunDiameter (in)SDRMaterial
Discharge Piping=4HoseComposite
Discharge Components
90 Degree Elbow=6
45 Degree Elbow=4
Tee Thru Flow=0
Tee Branch Flow=0
Concentric Reducer=0
Gate Valve, Open=1
Swing Check Valve, Open=0
Angle Valve, Open=0
Globe Valve, Open=0
TDH Calculations (Bypass 7)
Discharge \[MH-893E -> MH-3555E\]
Static Head=14.3ft
Flow Rate=187GPM
Total Length=300ft
Total Equivalent Length=482ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=4in
Friction Head Loss=10.21ft
Total Dynamic Discharge Head=24.51ft
Flow Velocity=4.77ft/s
Total Dynamic Head=24.51ft
AMT Pump 576X-95D Max Flow Rate=230GPM
AMT Pump 576X-95D Max TDH=30ft
Max Allowable Flow > Proposed Flow=
O.K.
Max Allowable TDH > Predicted TDH=
O.K.
Pipeline Specifications (Bypass 8)
Pipeline RunDiameter (in)SDRMaterial
Suction Piping=1817HDPE
Discharge Piping=1826HDPE
Suction ComponentsAmount
90 Degree Elbow=3
45 Degree Elbow=0
Tee Thru Flow=0
Tee Branch Flow=0
Concentric Reducer=0
Gate Valve, Open=0
Swing Check Valve, Open=0
Angle Valve, Open=0
Globe Valve, Open=0
Discharge Components
90 Degree Elbow=6
45 Degree Elbow=4
Tee Thru Flow=0
Tee Branch Flow=0
Concentric Reducer=0
Gate Valve, Open=0
Swing Check Valve, Open=0
Angle Valve, Open=0
Globe Valve, Open=0
TDH Calculations (Bypass 8)
Suction \[MH-A6 -> Pump\]
Static Head=10.5ft
Flow Rate=7084GPM
Total Length=20ft
Total Equivalent Length=146ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=15.76in
Friction Head Loss=3.28ft
Total Dynamic Suction Head=13.78ft
Flow Velocity=11.65ft/s
Discharge \[Pump -> MH-B0\]
Static Head=0ft
Flow Rate=7084GPM
Total Length=50ft
Total Equivalent Length=394ft
Pipe Roughness Factor=140-
Pipe Inside Diameter=16.53in
Friction Head Loss=7.03ft
Total Dynamic Discharge Head=7.03ft
Flow Velocity=10.59ft/s
Total Dynamic Head=20.81ft
PP1212S17 Predicted Flow Rate=7084GPM
PP1212S17 Max Flow Rate=9000GPM
PP1212S17 Max TDH=27ft
Max Allowable Flow > Proposed Flow=
O.K.
Max Allowable TDH > Predicted TDH=
O.K.
Net Positive Suction Head (Bypass 8)
Site Elevation=500ft
Atmospheric Head=33.34ft
Static Head=10.5ft
Friction Head=3.28ft
Vapor Head=0.78ft
NPSH Available=18.77ft
NPSH Required=14.9ft
NPSH-A > NPSH-R=
O.K.
Surge Allowance (Bypass 6)
Fluid Bulk Modulus=300000psi
Pipe Effective Modulus=150000psi
Suction
Velocity Delta=11.65ft/s
Wave Celerity=837ft/s
Max Surge Pressure=131psi
Allowable Surge Pressure=250psi
P_max < P_allowable=
O.K.
Discharge
Velocity Delta=10.59ft/s
Wave Celerity=666ft/s
Max Surge Pressure=95psi
Allowable Surge Pressure=160psi
P_max < P_allowable=
O.K.
Equation Reference
Friction Loss Calculations
Hazen-Williams Equation:
\[ft of head\]
L
Equivalent Length \[ft\]
=
eq
Hazen-Williams Roughness Coefficient
C=
Flow Rate \[GPM\]
Q=
Inside Pipe Diameter \[in\]
D=
Method of Equivalent Lengths used to determine fitting losses
from Crane Co. Technical Paper No. 409
NPSH Calculations
Atmospheric Pressure:
\[kPa\]
pAtmospheric Pressure at Sea Level \[Pa\]
=
0
2
g=
Earth Surface Gravitational Acceleration \[m/s\]
Molar Mass of Dry Air \[kg/mol\]
M=
Height Above Sea Level \[m\]
h=
R
=
0
T
Standard Temperature at Sea Level \[K\]
=
0
NPSH-Available:
\[ft of head\]
H
Atmospheric Head \[ft\]
=
atm
HStatic Head \[ft\]
=
Z
H
Friction Loss \[ft\]
=
L
HVapor Head \[ft\]
=
vap
Flow Velocity Calculation
\[ft/s\]
Flow Rate \[GPM\]
Q=
2
A=
Pipe Cross Sectional Area \[ft\]
PORTABLE ELECTRIC
Stainless Steel Strainer, Shaft, Impeller, Outlet and
SUBMERSIBLE PUMP FOR
Hardware for maximum corrosion resistance.
CORROSIVE & ABRASIVE
APPLICATIONS
Choice of impeller materials:
…………………………………………………………
1) 316 Stainless Steel for sea water and corrosive
applications and;
G 502T / G 504T / G 506T
2) Nitride Hardened 410 Stainless Steel for abrasive
applications. (Standard)
4"(100mm) / 4"(100mm) / 3"(75/80mm) NPT or Hose
…………………………………………………………
•Tandem Tungsten Carbide/Tungsten Carbide and
Tungsten Carbide/Tungsten Carbide mechanical seals.
G 530T / G 536T
Mechanical Seals in wholly enclosed pressure
4"(100mm) / 3"(75/80mm) NPT or Hose
compensated oil chamber.
…………………………………………………………
Field adjustable Nitrile Rubber-lined Diffuser/Wear Plate
Optimizes efficiency throughout the life of the pump. Optional
Polyurethane Diffusers and Wear Plates are available.
G 554T / G 556T
Automatic ON/OFF/ON Thermal Overloads embedded in Stator
4"(100mm) / 3"(75/80mm) NPT or Hose
Winding Optional - requires 6 core cable and external controls.
…………………………………………………………
Equipped with Sacrificial Zinc Anodes for maximum life
in a saline fluid environment.
Available in complete 316 Stainless Steel Construction with
Silicon Carbide/Silicon Carbide Mechanical Seals and Viton®
Elastomers.
Mody Pumps® Inc.
2166 Zeus Court, Bakersfield, CA 93308. USA
Tel.: (661) 392-7600 • Fax: (661) 392-7601
http://www.modypump.com
E-mail: sales@modypump.com
03.10.Rev.0
MATERIALS OF CONSTRUCTION
AND ENGINEERING DATA
MOTOR
2-pole induction continuous rated motor with squirrel cage rotor.
Stator insulation class 'H' (180ºC)
Speed : 3400 RPM @ 60 Hz, 2800 RPM @ 50 Hz
Power Rating : 5HP/7.5HP/10HP @ 60 Hz, 3.7kW/5.5kW/7.5kW @ 50Hz Full Load
Current FLA: 7.1, 11, 14 Amps @ 460v. 8.1, 12.5, 16 @ 400v.
Max. temperature of the pump liquid: 104°F/40°C
Max. start/stop per hour : 15
POWER SUPPLY
3 phase, 50/60 Hz, AC Supply. Available in any voltage frequency
combination.(208/220/230/380/415/460/575/1000V)
MODEL A
BALL BEARINGS
G-502 25-1/4” (640mm)
The rotor shaft is carried in two single row, deep groove ball bearings.
G-504
The bearings are enclosed with high temperature grease-containing special
G-506
Anti-corrosion additive.
G-530 28-1/2” (725mm)
POWER CABLE
G-536
Waterproof/oil proof, rubber-insulated, neoprene-sheathed copper conductor
flexible cable, 50ft. (15m) length standard. Type SOOW in North America,
G-554 29-1/2” (750mm)
EPR in the Middle East and HO7RN in the EU. 6 Core with thermal overloads
G-556
optional.
SHAFT SEAL
Tandem Tungsten Carbide/Tungsten Carbide and Tungsten Carbide/Tungsten
Carbide Mechanical seals wholly enclosed in a pressure compensated oil chamber.
CORROSION RESISTANT
Epoxy coated Aluminum Outer Casing
Epoxy coated Extruded Aluminum Stator Casing
PERFORMANCE CURVES
Nitrile Rubber– Lined Diffuser/Wear plate. Polyurethane Optional.
Shaft: 431 Stainless Steel
Hardware: 304 Stainless Steel
Impeller: Nitride Hardened 410SS to 56HRC is Standard.
pH Range 5 - 8
STRAINER
304 Stainless Steel with 1” (25mm) X 1/4” (6mm) {G 502/504},
1-3/16” (30mm) X 3/8” (9.5mm) {G530/554},
1/4” (6mm) Round Holes {G 506/536/556}
SUBMERGENCE
Submergence below liquid surface min 5” (127mm) max. 50’ (15m).
WEIGHTS(Approx. without cable)
G 502/504: 110lbs. (50Kg)
G 506: 115lbs. (52Kg)
G 530: 130lbs. (59Kg)
G 536: 135lbs. (61Kg)
G 554: 142lbs. (64Kg)
G 556: 147lbs. (67Kg)
Due to continuous product development, specifications are subject to change without notice.
03.10 Rev.0
Support