What Is An API 610 Pump? A Complete Guide To API 610 Centrifugal Pumps For Oil & Gas
Aug 21, 2026
Leave a message
In oil & gas, petrochemical, refining, and other process industries, pumps are often required to handle high temperatures, high pressures, flammable or hazardous liquids, corrosive media, and continuous-duty operation.
Under these conditions, ordinary industrial pumps may not provide the mechanical robustness, sealing arrangements, reliability, and documentation required for critical process services.
This is where API 610 centrifugal pumps become important.
API 610 is a major industry standard developed for centrifugal pumps used in petroleum, petrochemical, and natural gas applications. The standard provides requirements that address pump design, construction, materials, mechanical integrity, testing, and related equipment considerations.
This guide explains what an API 610 pump is, the major API 610 pump configurations, how these pumps are selected, where they are used, and what engineers should consider when specifying an API 610 centrifugal pump.

1. What Does API 610 Mean?
API stands for the American Petroleum Institute.
API 610 is the API standard covering centrifugal pumps for petroleum, petrochemical, and natural gas industries. The American Petroleum Institute currently lists API Standard 610 in its standards catalog, and its standards plan records the 13th edition dated June 29, 2026.
Unlike a general-purpose pump specification, API 610 addresses the requirements associated with demanding process applications where pump reliability, mechanical integrity, maintainability, and controlled manufacturing and testing are especially important.
An API 610 pump is therefore best understood as a centrifugal pump engineered and specified to meet the applicable requirements of API 610 and the project's technical specification.
API 610 should not be confused with a particular hydraulic principle. Most API 610 pumps are still based on conventional centrifugal pump technology. What differentiates them is the engineering, mechanical design, materials, inspection, testing, and application requirements associated with the standard.
2. Why Are API 610 Pumps Important in Oil & Gas Applications?
Oil & gas and petrochemical plants contain many services where pump failure can lead to:
Production losses
Unplanned shutdowns
Product contamination
Hazardous fluid leakage
Fire or environmental risks
Expensive maintenance
Reduced plant availability
For this reason, process pumps used in critical services must be designed with reliability and maintainability in mind.
Typical fluids handled by process pumps may include:
Crude oil
Refined petroleum products
Hydrocarbons
Condensate
Hot process fluids
Chemical solutions
Cooling or process water
Corrosive liquids
Depending on the service, the pump may need to operate at elevated temperature, significant discharge pressure, or demanding suction conditions.
API 610 provides a structured technical basis for specifying and manufacturing these centrifugal pumps.
The goal is not simply to obtain higher pressure. The objective is to achieve reliable hydraulic and mechanical performance over the required operating range and service life.
3. API 610 Pump vs. Standard Industrial Centrifugal Pump
One of the most common misconceptions is that an API 610 pump is simply a "stronger centrifugal pump."
In reality, the difference is broader.
An API 610 project specification may place greater emphasis on:
Mechanical integrity
The shaft, casing, bearings, rotor, coupling, and other components must be designed appropriately for the specified operating conditions.
Rotor dynamics
High-speed or critical-service pumps require careful consideration of shaft stiffness, balance, natural frequencies, and overall rotor behavior.
Sealing
The sealing system must be suitable for the process fluid, operating temperature, pressure, and safety requirements.
Bearing and lubrication systems
Bearing arrangements and lubrication systems need to be appropriate for continuous process operation.
Maintainability
Pump construction should allow inspection, repair, and component replacement with minimum unnecessary downtime.
Inspection and testing
API 610 projects commonly involve detailed inspection, documentation, and performance testing requirements defined by the purchaser and applicable standard.
Therefore, selecting an API 610 pump is not simply a matter of matching flow and head.
4. Main API 610 Pump Configurations
API 610 includes several major centrifugal pump configurations. The appropriate configuration depends on the process conditions, flow rate, pressure, temperature, installation arrangement, and project requirements.
The major categories include:
4.1 OH - Overhung Pumps
In overhung pumps, the impeller is located on the overhung portion of the shaft relative to the bearing arrangement.
Common API 610 overhung configurations include:
OH1
OH2
OH3
OH4
OH5
OH6
OH7
The exact configuration depends on the mounting and drive arrangement.
Overhung pumps are widely considered for general process services where their hydraulic range and mechanical configuration are appropriate.
5. BB - Between-Bearings Pumps
Between-bearings pumps support the rotor between two bearings.
Typical API 610 configurations include:
BB1
BB2
BB3
BB4
BB5
These configurations are particularly relevant to demanding process services requiring high reliability, high head, large flow, or multistage hydraulic arrangements.
BB1 Pumps
BB1 pumps are typically associated with axially split, between-bearings, single-stage centrifugal pump designs.
They can be considered for applications requiring relatively high flow and process reliability.
BB2 Pumps
BB2 pumps are generally radially split, between-bearings, single-stage centrifugal pumps.
The radially split casing arrangement can be advantageous for certain high-temperature and high-pressure services.
BB3 Pumps
BB3 pumps are commonly associated with axially split, multistage, between-bearings centrifugal pumps.
They can be selected where several hydraulic stages are required to generate high head.
BB5 Pumps
BB5 pumps are radially split, multistage, between-bearings pumps, typically using a double-casing configuration.
This configuration is particularly relevant to high-pressure process services.
The exact pump configuration should always be selected against the API 610 edition, process data, and project specification rather than solely by pump type name.
6. VS - Vertically Suspended Pumps
VS pumps are designed with the pumping assembly vertically suspended.
Common categories include:
VS1
VS2
VS3
VS4
VS5
VS6
VS7
Vertical configurations may be considered when:
The pump must be installed in a tank or vessel
Available floor space is limited
The suction arrangement requires vertical installation
The process system requires a vertical suspended design
Different VS configurations have different hydraulic, structural, and installation arrangements.
The final selection depends heavily on the actual vessel, suction conditions, liquid properties, and required submergence.
7. Main Components of an API 610 Pump
Although API 610 pumps vary significantly by configuration, their main components generally include the following.
7.1 Pump Casing
The casing contains and guides the process fluid while withstanding the operating pressure and temperature.
Material selection depends on:
Fluid composition
Corrosiveness
Operating temperature
Design pressure
Mechanical requirements
For hazardous process fluids, casing integrity is a fundamental safety consideration.
7.2 Impeller
The impeller converts shaft power into hydraulic energy.
Its design determines major hydraulic performance parameters such as:
Flow rate
Head
Efficiency
NPSH characteristics
Power requirement
Depending on the pump configuration, the impeller may be:
Closed
Open
Single-stage
Multistage
7.3 Shaft
The shaft transmits torque from the driver to the impeller.
For process pumps, shaft design must consider:
Mechanical strength
Shaft deflection
Torsional loading
Critical speed
Corrosion
Fatigue
Seal requirements
A properly designed shaft contributes to stable operation and reduced vibration.
7.4 Bearings
Bearings support the rotating assembly and maintain proper rotor position.
Depending on the pump design, bearings may handle:
Radial loads
Axial loads
Combined loading
Lubrication arrangements must be selected according to operating speed, temperature, and service requirements.
7.5 Mechanical Seal
Mechanical seals are used to reduce leakage along the rotating shaft.
For oil & gas applications, seal selection is particularly important because the pumped medium may be:
Flammable
Toxic
Volatile
Corrosive
High-temperature
Seal arrangement and auxiliary systems should therefore be selected based on the actual process conditions and applicable project requirements.
7.6 Coupling and Baseplate
The coupling transfers power from the driver to the pump.
The baseplate supports the pump-driver assembly and helps maintain alignment.
Poor alignment can lead to:
Excessive vibration
Bearing damage
Coupling wear
Seal problems
Shaft damage
8. How Does an API 610 Centrifugal Pump Work?
The basic hydraulic principle remains the same as other centrifugal pumps.
Step 1: Fluid Enters the Pump
The process fluid enters through the suction nozzle.
The suction system must provide sufficient pressure to prevent undesirable cavitation.
Step 2: The Impeller Rotates
The driver rotates the shaft and impeller.
Mechanical energy is transferred to the process fluid.
Step 3: Fluid Gains Velocity and Energy
The rotating impeller accelerates the liquid and moves it toward the outer diameter.
Step 4: Velocity Is Converted Into Pressure
The hydraulic passage in the casing or diffuser converts part of the fluid velocity into pressure.
Step 5: Fluid Leaves the Pump
The pressurized fluid exits through the discharge nozzle and continues into the process system.
For a multistage pump, the process is repeated across multiple hydraulic stages, allowing significantly higher total head to be achieved.
9. Typical Applications of API 610 Pumps
API 610 centrifugal pumps can be applied to numerous services across the petroleum, petrochemical, and natural gas industries.
Typical applications include:
Refinery Processes
- Crude oil transfer
- Product transfer
- Hydrocarbon circulation
- Process feed
- Hot oil services
Petrochemical Plants
- Process liquid transfer
- Chemical circulation
- Intermediate product transfer
- Cooling and utility services
Oil & Gas Transportation
- Pipeline booster systems
- Terminal transfer
- Tank farm transfer
- Loading and unloading systems
LNG and Gas Processing
- Hydrocarbon liquid services
- Condensate handling
- Process circulation
- Utility systems
Offshore Applications
Vertical and horizontal process pump configurations may be used for:
- Produced water
- Process circulation
- Hydrocarbon transfer
- Utility services
The exact applicability depends on the fluid properties, operating conditions, pump configuration, and project specification.
10. Important Parameters for API 610 Pump Selection
Correct API 610 pump selection begins with accurate process data.
The key parameters include:
Flow Rate
Normally specified in:
m³/h
L/s
US gpm
Differential Head
Specified in:
m
ft
Operating Pressure
Both suction and discharge pressure should be evaluated.
Temperature
Temperature affects:
Material selection
Mechanical seal selection
Bearing and lubrication requirements
Vapor pressure
NPSH conditions
Fluid Properties
The pump manufacturer needs to know:
Density
Viscosity
Vapor pressure
Corrosiveness
Solids content
Toxicity or hazardous characteristics
NPSHA
Available NPSH must be carefully evaluated, especially for hot or volatile hydrocarbons.
Speed
Pump speed influences:
Hydraulic performance
NPSH
Power
Vibration
Rotor dynamics
Duty and Operating Range
The pump should not be selected solely according to a single rated point.
Engineers should also consider:
Minimum continuous flow
Normal operating point
Maximum operating point
Start-up conditions
Turndown requirements
Transient conditions
11. Why NPSH Is Critical in API 610 Applications
Cavitation is one of the major risks in centrifugal pump operation.
When the local pressure in the pump falls below the liquid vapor pressure, vapor bubbles may form. Their subsequent collapse can damage hydraulic and mechanical components.
Possible consequences include:
Noise
Vibration
Head loss
Flow instability
Impeller erosion
Bearing damage
Seal failure
The basic relationship to consider is:
NPSHA > NPSHR
However, the required engineering margin depends on the application, pump design, fluid properties, and project requirements.
For hydrocarbon services, NPSH analysis is especially important because many process liquids have relatively high vapor pressure.
12. API 610 Pump Mechanical Design Considerations
One of the reasons API 610 is important is that the standard addresses much more than basic hydraulic performance.
For a demanding project, engineers may need to evaluate:
Rotor Dynamics
The rotating assembly must operate reliably within the required speed range.
Shaft Deflection
Excessive shaft deflection can negatively affect:
Mechanical seals
Bearings
Couplings
Rotor stability
Critical Speed
Operating speed and critical speeds must be properly evaluated for the selected pump.
Bearing Loading
Radial and axial forces must remain within acceptable design limits.
Thermal Expansion
High-temperature process conditions may cause significant dimensional changes.
Casing Design
The casing must be suitable for the specified pressure, temperature, and fluid.
These factors distinguish a properly engineered process pump from a basic general-purpose centrifugal pump.
13. API 610 Pump Sealing and Auxiliary Systems
For hazardous services, the seal system can be as important as the pump itself.
Depending on the process conditions, the system may require appropriate:
Mechanical seal arrangements
Seal flush systems
Cooling systems
Quench systems
Barrier or buffer fluid systems
The proper configuration depends on:
Fluid properties
Temperature
Pressure
Volatility
Toxicity
Leakage requirements
Seal selection should therefore be performed together with the pump selection rather than treated as an afterthought.
14. Materials for API 610 Process Pumps
Material selection should be based on the actual operating environment.
Common engineering considerations include:
Corrosion resistance
Temperature resistance
Mechanical strength
Erosion resistance
Compatibility with the pumped medium
Possible materials may include various grades of:
Carbon steel
Stainless steel
Duplex stainless steel
Alloy steel
Other corrosion-resistant alloys
The correct material cannot be selected solely from the pump model. It should be determined from the fluid composition, temperature, pressure, corrosion characteristics, and project material specification.
15. Common API 610 Pump Operating Problems
Even a properly designed pump can experience problems when system conditions or operating practices are incorrect.
Low Discharge Pressure
Possible causes include:
- Incorrect pump speed
- Wrong rotation direction
- Insufficient suction conditions
- Excessive internal wear
- Damaged impeller
- Operation outside the performance range
Excessive Vibration
Possible causes include:
- Misalignment
- Rotor imbalance
- Bearing problems
- Cavitation
- Pipe strain
- Foundation issues
- Hydraulic instability
Mechanical Seal Leakage
Possible causes include:
- Incorrect seal selection
- Seal damage
- Shaft runout
- Misalignment
- Improper seal auxiliary conditions
- Excessive vibration
High Bearing Temperature
Possible causes include:
- Poor lubrication
- Incorrect lubricant
- Bearing wear
- Misalignment
- Excessive mechanical load
- Abnormal operating conditions
Troubleshooting should focus on identifying the root cause rather than simply replacing individual components.
16. API 610 Pump Maintenance
Preventive maintenance is essential for maintaining process pump reliability.
A typical maintenance program may include:
Daily or Routine Monitoring
Check:
Pressure
Flow
Bearing temperature
Vibration
Seal leakage
Lubrication condition
Motor current
Periodic Inspection
Inspect:
Mechanical seals
Bearings
Coupling
Shaft condition
Impeller
Wear components
Alignment
Performance Monitoring
Compare actual operating data with the original pump performance.
Changes in:
Flow
Head
Power consumption
Vibration
may indicate internal wear or changing system conditions.
Maintenance Records
Maintain records of:
Operating hours
Vibration trends
Seal replacement
Bearing replacement
Overhaul history
Performance data
Trend-based maintenance can identify developing problems before they cause a major shutdown.
17. How to Choose an API 610 Pump Manufacturer
Selecting the right manufacturer is as important as selecting the pump type.
When evaluating a supplier, consider:
Engineering Capability
Does the manufacturer understand:
Process pump design?
Hydraulic selection?
High-temperature services?
High-pressure applications?
NPSH analysis?
Material selection?
Manufacturing Capability
Evaluate:
Casting quality
Machining accuracy
Rotor balancing
Assembly control
Quality inspection
Testing Capability
Ask what testing and inspection documentation can be provided for the project.
Depending on the purchase specification, this may include:
Performance testing
Material documentation
Dimensional inspection
Balancing records
Pressure testing
Non-destructive examination
Inspection and test plans
After-Sales Support
For long-term industrial operation, spare parts, technical support, troubleshooting, and maintenance assistance are also important.
18. API 610 Does Not Mean Every Pump Is Automatically "API Certified"
This point is important for pump buyers.
There is a difference between:
"Designed / manufactured to meet API 610 requirements"
and
"API-certified product or manufacturer."
The actual certification status depends on the manufacturer, product, project, and applicable API certification program.
Therefore, purchasing teams should ask for specific supporting documentation rather than relying only on the phrase "API 610 pump."
Depending on the project, buyers may request:
API documentation
Technical datasheets
Inspection and test plans
Material certificates
Test reports
Quality documentation
Drawings
Performance curves
Manufacturing records
The applicable requirements should always be confirmed against the purchaser's technical specification.
19. API 610 Pump Selection Checklist
Before requesting a quotation, prepare the following information:
| Parameter | Recommended Information |
|---|---|
| Pump Service | Process description |
| Fluid | Fluid name and composition |
| Flow Rate | Normal / Rated / Maximum |
| Differential Head | Normal / Rated |
| Suction Pressure | Operating value |
| Discharge Pressure | Operating value |
| Temperature | Normal / Maximum |
| Density | kg/m³ |
| Viscosity | cP |
| Vapor Pressure | At operating temperature |
| NPSHA | Available NPSH |
| Pump Speed | rpm |
| Driver | Motor / Turbine |
| Power Supply | Voltage / Frequency |
| Installation | Horizontal / Vertical |
| Pump Configuration | OH / BB / VS |
| Seal Arrangement | Project requirement |
| Materials | Process-specific |
| Standards | API 610 edition / project specification |
| Duty | Continuous / intermittent |
| Area Classification | Hazardous area requirements |
Providing complete information allows the pump manufacturer to recommend the correct hydraulic and mechanical configuration.
20. HNYB PUMPS: Industrial Centrifugal Pump Solutions for Process Applications
HNYB PUMPS is a professional Chinese manufacturer of industrial centrifugal pumps, serving water supply, petrochemical, oil & gas, chemical, mining, power, and other industrial applications.
Our product portfolio includes various centrifugal pump configurations, including:
Petrochemical process pumps
Horizontal centrifugal pumps
Horizontal multistage centrifugal pumps
High-pressure multistage pumps
Split case centrifugal pumps
Chemical centrifugal pumps
Vertical centrifugal pumps
Customized industrial pump systems
For demanding oil & gas and petrochemical applications, pump selection can be customized according to:
Flow
Head
Temperature
Pressure
Fluid properties
Materials
Sealing requirements
Installation configuration
Driver requirements
Project specifications
HNYB PUMPS focuses on combining hydraulic performance, mechanical reliability, material compatibility, and application-specific engineering to provide dependable pumping solutions for industrial projects.
For projects that specify API 610, customers should provide the applicable API 610 edition and project technical specification so that the pump design, inspection, testing, materials, and documentation can be evaluated against the actual purchasing requirements.
API 610 centrifugal pumps are designed for demanding process applications where reliability, mechanical integrity, maintainability, and controlled testing are important.
For oil & gas, refining, petrochemical, LNG, and other process industries, choosing the correct pump requires much more than selecting a pump based only on flow and head.
Engineers should evaluate:
Flow + Head + Temperature + Pressure + Fluid Properties + NPSH + Pump Configuration + Materials + Sealing + Driver + Project Specification
The correct combination of these factors helps ensure stable operation, reduced maintenance requirements, and improved plant availability.
HNYB PUMPS provides a range of industrial centrifugal pump solutions for demanding process applications. For API 610-related projects, we recommend evaluating the pump against the specific API 610 edition and purchaser's technical specification before finalizing the design or procurement.
Contact HNYB PUMPS with your process data and project requirements for a customized centrifugal pump recommendation.
FAQ About API 610 Pumps
Q: What is an API 610 pump?
A: An API 610 pump is a centrifugal pump designed and specified for petroleum, petrochemical, and natural gas industry services in accordance with the applicable requirements of API Standard 610.
Q: Is API 610 only for oil pumps?
A: No. API 610 covers centrifugal pumps used in petroleum, petrochemical, and natural gas industries. The pumped liquid may be crude oil, refined products, hydrocarbons, chemicals, water, or other process fluids depending on the application.
Q: What are the main API 610 pump types?
A: The main structural groups include:
OH - Overhung pumps
BB - Between-bearings pumps
VS - Vertically suspended pumps
Q: What is the difference between BB and OH pumps?
A: OH pumps use an overhung rotor arrangement, while BB pumps support the rotor between bearings.
BB configurations are often selected for applications requiring higher hydraulic performance, multistage designs, or additional mechanical robustness.
Q: Why is NPSH important for API 610 pumps?
A: Insufficient NPSH margin can result in cavitation, which may cause vibration, noise, hydraulic instability, and component damage.
Q: Are all API 610 pumps high-pressure pumps?
A: No. API 610 is primarily an equipment standard for centrifugal pumps used in petroleum, petrochemical, and natural gas services. Required pressure and head depend on the individual process application and pump configuration.
Q: Can a standard centrifugal pump replace an API 610 pump?
A: Not automatically. For a project specifically requiring API 610 compliance, the pump should be evaluated against the applicable API 610 requirements rather than substituted solely based on similar flow and head.
