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Pump Solutions Inc.
Reliable Solutions for Diffucult Applications
985-871-5173
sales@pump-solutions.net
ABOUT
PRODUCTS
CPC Pumps International
Hermetic Pumps
Egger Turo Pumps
Weir Slurry Group
Weir Slurry Group Hazleton
Feluwa Pumps
Phoenix Pump
RESOURCES
CALCULATORS
Friction Loss
isf (Shaft Flexibility Index)
NPSHa (Net Positive Suction Head Available)
Suction Specific Speed (Nss)
Impeller Tip Speed
MCTF (Minimum Continuous Thermal Flow)
REQUEST A QUOTE
Pump Application Data
Spare Parts Inquiry
CONTACT
ABOUT
PRODUCTS
CPC Pumps International
Hermetic Pumps
Egger Turo Pumps
Weir Slurry Group
Weir Slurry Group Hazleton
Feluwa Pumps
Phoenix Pump
RESOURCES
CALCULATORS
Friction Loss
isf (Shaft Flexibility Index)
NPSHa (Net Positive Suction Head Available)
Suction Specific Speed (Nss)
Impeller Tip Speed
MCTF (Minimum Continuous Thermal Flow)
REQUEST A QUOTE
Pump Application Data
Spare Parts Inquiry
CONTACT
Pump Application Data
Step
1
of
3
33%
End User
*
Site Location
*
Engineering Firm/Contractor
Contact Name
First
Last
Contact Phone
Contact Email
*
Unit
Service
Equipment Number
Number of Pumps Required
Type
*
Process Pump
Sump Pump
Is the liquid to be pumped water?
Yes
No
What is the liquid name or type to be pumped?
What is the vapor pressure of the fluid at the operating temperature? (psia)
Please enter a number less than or equal to
9999
.
What is the density of the fluid? (SG)
*
Please enter a number less than or equal to
9.99
.
What is the specific heat of the fluid? (Btu/lbsm-F)
Please enter a number less than or equal to
9.99
.
What is the viscosity of the fluid? (cP)
Please enter a number less than or equal to
9999
.
Is the fluid corrosive in nature?
Yes
No
Please explain corrosive component
Is H2S present in the stream?
Yes
No
Please provide H2S concentration (ppm)
Please enter a number less than or equal to
99999
.
Are chlorides present in the fluid?
Yes
No
Please provide chloride concentration (ppm)
Please enter a number less than or equal to
99999
.
Any other unique characteristics of this fluid that we should know about?
Polymerizes
Shear Sensitive
Supercritical Fluid
Steep Vapor Pressure Curve
Are there any solids present in the fluid?
Yes
No
What is the name or type of solids present?
Are these solids errosive/abrasive?
Yes
No
What is the mean or average particle size?
Please enter a number less than or equal to
9999
.
Please choose units for the mean particle size value
MM
Micron
Mesh
Inch
What is the maximum particle size?
Please enter a number less than or equal to
9999
.
Please choose units for the maximum particle size value
MM
Micron
Mesh
Inch
What is the solids concentration? (% by weight)
Please enter a number less than or equal to
100
.
What is the density of the solids?
Please enter a number less than or equal to
99999
.
Do these solids melt at a certain temperature?
Yes
No
What is the melting temperature of the solids? (°F)
Please enter a number less than or equal to
999999
.
Is there any entrained gas in the fluid?
Yes
No
What is the concentration of the entrained gas? (% by volume)
Please enter a number less than or equal to
100
.
What is the temperature of the fluid to be pumped? (°F)
Please enter a number less than or equal to
850
.
What is the desired minimum capacity of the pump? (gpm)
What is the desired rated capacity of the pump? (gpm)
*
What is the desired maximum capacity of the pump? (gpm)
What is the pressure on the sump? (psig)
If atmospheric, leave blank
What is the suction pressure on the pump? (psig)
*
Please enter a number less than or equal to
9999
.
What is the discharge pressure required of the pump? (psig)
*
Please enter a number less than or equal to
9999
.
Differential head, based on discharge pressure and stated fluid density is:
Differential head, based on discharge pressure and stated fluid density is:
Based on your stated rated suction and discharge pressure, the differential pressure required is (psi):
If differential pressure is different than our calculated value, insert it here (psi)
Differential head, based on differential pressure and stated fluid density is (ft):
What is the NPSH available at the pump impeller centerline? (ft)
*
Visit
our NPSH calculator
if you need to calculate this.
Any unique operating parameters that we should know about?
What is the sump depth (l1 in the sketch below)? (ft)
*
Please enter a number less than or equal to
999
.
What is the low liquid level (l2 in the sketch below)? (ft)
Please enter a number less than or equal to
99999
.
What is the sump length if square or rectangular? (ft)
Please enter a number less than or equal to
999
.
What is the sump width if square or rectangular? (ft)
Please enter a number less than or equal to
999
.
What is the sump diameter (if round)? (ft)
Please enter a number less than or equal to
999
.
What is the applicable pump standard we should adhere to?
API 610 - Latest Edition
API 685 - Latest Edition
Non-API Sealless
Sealless - Lethal Service
Non-API - Sealed
Vendor choose based on application
What materials of construction should we use for the process wetted components of the pump?
API 610 - S-4 (CS / CS / CI)
API 610 - S-5 (CS / CS / 12Ch)
API 610 - S-6 (CS / 12Ch / 12Ch)
API 610 - S-8 (CS / SS /SS)
API 610 - S-9 (CS / Monel / Monel)
API 610 - C-6 (12Ch / 12Ch /12Ch)
API 610 - A-8 (SS / SS / SS)
API 610 - D-1 (Duplex /Duplex / Duplex)
API 610 - D-2 (Super Duplex / Super Duplex / Super Duplex)
What materials of construction should we use for the process wetted components of the pump?
API 685 - S-1 (CS / CI / CI)
API 685 - S-3 (CS / Ni-Resist / Ni-Resist)
API 685 - S-4 (CS / CS / CI)
API 685 - S-5 (CS / CS / 12Ch)
API 685 - S-6 (CS /12Ch / 12Ch)
API 685 - S-8 (CS / SS / SS)
API 685 - S-9 (CS / Ni-Cu Alloy/ Ni-Cu Alloy)
API 685 - C-6 (12Ch / 12Ch / 12 Ch)
API 685 - A-7 (AUS / AUS / AUS)
API 685 - A-8 (SS / SS / SS)
API 685 - A-9 (A20 / A20 / A20)
API 685 - D-1 (Duplex / Duplex / Duplex)
API 685 - D-2 (Super Duplex / Super Duplex / Super Duplex)
API 685 - H-1 (Hast B / Hast B / Hast B)
API 685 - H-2 (Hast C / Hast C / Hast C)
API 685 - T-1 (Ti / Ti / Ti)
What materials of construction should we use for the process wetted metallic components of the pump?
Cast Iron
Ductile Iron
Carbon Steel
28% Chrome
316 SS
317 SS
CD4MCU
Duplex
Super Duplex
Hastelloy B
Hastelloy C
Titanium
Zirconium
What materials of construction should we use for the process wetted non-metallic components of the pump?
Natural Rubber
EPDM
Urethane
Neoprene
Nitrile
Viton
Ceramic
What Pump Orientation would best suit your needs?
Horizontal
Inline
No preference
What Lubrication method do you prefer?
Grease
Flood Oil
Pure Oil Mist
Purge Oil Mist
Forced Oil Lubrication Skid
What type of testing would you like performed on the pump?
Certified (non-witnessed)
Witnessed
Not Required
List any additional or special testing
QC / NDE will be applied per applicable standard
What type of seal and seal support system would you prefer?
Packing (N/A for API 610 compliant pumps)
Single Mechanical Seal
Dual Mechanical Seal
Vendor Choose based on application
Seal Flush Plan Preference? (Check all that apply)
Plan 11
Plan 13
Plan 14
Plan 21
Plan 23
Plan 32
Plan 52
Plan 53A
Plan 53B
Plan 53C
Plan 54
Plan 72
Plan 74
Plan 75
Plan 76
Plan 61
Plan 62
Plan 65A
Plan 65B
Plan 66A
Plan 66B
N/A
Is Nitrogen present for use with seal system?
Yes
No
Is cooling water present if needed for pump or seal system cooling?
Yes
No
What voltage is available for the electric motor driver?
480V
2300V
4160V
What Area Classification is required for the motor?
Class I
Class II
What Area Division is required for the motor?
Division I
Division II
What Area Temp Code is required for the motor?
T1
T2
T2A
T2B
T2C
T2D
T3
T3A
T3B
T4
T4A
T5
T6
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