API 610 / ISO 13709 · TYPE OH2

API 610 OH2 Process Pump

Heavy-duty API 610 / ISO 13709 Type OH2 process-pump platform for refinery, petrochemical and severe-service duties. Series coverage extends to 2,600 m³/h, 300 m head, 100 bar and 425 °C; the operating point of the selected size governs the final selection.

For an existing Goulds 3700 installation, use the dedicated 3700 replacement engineering route.
NEW PROJECT · OH2 Neutral API 610 OH2 process pump
API 610 OH2 Process Pump Centerline-mounted end-suction process-pump platform for severe-service duties.
2,600 m³/hSeries maximum capacity
300 mSeries maximum head
100 barSeries maximum pressure
425 °CSeries maximum temperature
API 610 · OH2Centerline-mounted end suction
Start with the duty

New API 610 Project? Start With the Information You Already Have.

You do not need to complete a full API datasheet before the first engineering review. A duty point and process description are enough to begin.

The first selection is preliminary. Final pump size, speed, impeller, material, seal arrangement and project interfaces are confirmed before quotation / release.
01 · DUTY

Flow + Head

Required duty point, operating range, frequency and any existing curve or project design point.

02 · PROCESS

Fluid + Conditions

Liquid, temperature, pressure, SG, viscosity, solids and corrosion considerations.

03 · PROJECT

Specification + Interfaces

Material class, seal / auxiliary requirements, motor, baseplate, nozzles, inspection and documentation.

API 610 OH2 pump architecture visual End Suction Centerline-Mounted Casing Seal / Shaft Region Bearing Housing + Driver Interface
OH2 mechanical architecture

Built Around the API 610 OH2 Arrangement

Centerline-mounted end-suction construction, back-pull-out serviceability and a finned bearing housing with fan cooling define the core mechanical platform for hot and cold process service.

API 610 / ISO 13709 Type OH2Single-stage overhung process-pump platform.
Centerline-Mounted End SuctionHeavy-duty arrangement for hot and cold process service.
Back-Pull-Out ConstructionMaintenance-friendly rotating assembly access.
Modular ConstructionBroad parts commonality across the series.
Finned Bearing HousingDesigned to support demanding process temperature conditions.
Fan CoolingAdditional bearing-housing cooling for hot service.
Hydraulic selection

Performance Coverage Should Be Selected From the Actual Duty Point.

The series envelope reaches 2,600 m³/h capacity, 300 m head, 100 bar pressure and 425 °C temperature. These are series-level limits; the actual operating point, pump size, speed and impeller selection must be confirmed against the reviewed duty point.

Selection note: published figures define the series envelope. The selected pump size and reviewed performance curve govern the quoted operating point.
API 610 OH2 Hydraulic Coverage
to 2,600 m³/hto 300 m
HEAD FLOW
Final performance is confirmed against the selected pump size and reviewed duty curve.
Series operating envelope

API 610 OH2 Series Performance Limits

Use these values as the published series envelope. Final selection is always checked against the operating point and selected pump size.

01 · CAPACITY

Up to 2,600 m³/h

Equivalent to approximately 11,440 US gpm at the series level.

02 · HEAD

Up to 300 m

Equivalent to approximately 1,000 ft at the series level.

03 · PRESSURE

Up to 100 bar

Equivalent to approximately 1,450 psi at the series level.

04 · TEMPERATURE

Up to 425 °C

Equivalent to approximately 800 °F for hot-process service.

Project configuration

Configure the Pump Around the Process — Not the Other Way Around.

The pump is configured around the process conditions, metallurgy, seal requirements and complete project package.

01 · PROCESS CONDITIONS

Pressure, Temperature & Liquid

Review operating and design conditions before selecting hydraulics or metallurgy.

  • Normal / rated / maximum duty
  • Liquid properties and vapor pressure
  • NPSHa / suction condition
  • Continuous / intermittent service
02 · MATERIALS

Metallurgy by Service

Material selection is reviewed against corrosion, erosion, temperature and project requirements.

  • Casing / impeller metallurgy
  • Shaft and wear components
  • Material certification scope
  • Project material class
03 · SEAL / AUXILIARY

Seal Arrangement & Utilities

Seal chamber, mechanical seal and auxiliary requirements are confirmed as part of project review.

  • Seal arrangement
  • Seal plan / utilities
  • Cooling / flushing requirements
  • Instrumentation interfaces
04 · PACKAGE

Driver, Baseplate & Documentation

Complete package interfaces are reviewed before manufacturing and release.

  • Motor / driver
  • Coupling / guard
  • Baseplate / nozzle interfaces
  • Inspection / test / documentation scope
Process services

API 610 OH2 Duties Across Refinery & Process Applications

Use application examples as selection context. Final suitability depends on the actual duty, liquid, operating range and project specification.

Refinery ProcessHot and cold process duties.
Petrochemical ProcessTransfer and circulation service.
Chemical ProcessConfigured after materials review.
BoostingHigh-duty pressure boosting applications.
DesalinationProject-specific desalination service.
Boiler Feedwater BoosterBoiler-system boosting duties.
Condensate ExtractionProcess and utility condensate service.
HTF Oil CirculationHigh-temperature heat-transfer-fluid circulation.
Hot Process ServiceUp to the verified series temperature envelope.
Other API 610 DutySend the project datasheet for engineering review.
Engineering verification

What We Verify Before an OH2 Pump Is Released

Hydraulics, process conditions, package interfaces and quality requirements are reviewed before release.

01 · HYDRAULICS

Duty & Operating Range

Flow, head, speed, operating window, NPSH and hydraulic selection.

02 · PROCESS

Conditions & Metallurgy

Pressure, temperature, liquid properties, corrosion and material requirements.

03 · MECHANICAL

Package Interfaces

Nozzles, baseplate, shaft centerline, coupling, motor and project interfaces.

04 · SEAL / QA

Auxiliary & Release Scope

Seal plan, cooling / lubrication, inspection, testing and documentation.

01Application Review
02Hydraulic Selection
03Material / Seal Review
04Drawing Confirmation
05Manufacturing
06Inspection / Testing
Existing pump? · API 610 Replacement Hub

Use a Dedicated Replacement Route When the Installed Pump Is Known.

This keeps the generic OH2 page focused on new API 610 selection while preserving high-intent replacement pages.

Flagship replacement route

Existing Goulds 3700

Use the dedicated 3700 page for model-specific hydraulic, dimensional, material, seal and installation-interface review.

Review Goulds 3700 Replacement →
Sulzer family

Existing Sulzer Pump

Keep ZA / ZE / ZF and other Sulzer replacement paths inside the existing Sulzer engineering hub.

View Sulzer Replacement Hub →
Other API 610 model

Other Installed Pump

Send the model, datasheet, curve or GA drawing for a project-specific replacement review.

Send Existing Pump Data →
Buyer questions

API 610 OH2 Product FAQ

Answers focus on the information needed to begin an OH2 engineering review.

What is the published series operating envelope?

The series-level envelope extends to 2,600 m³/h capacity, 300 m head, 100 bar pressure and 425 °C temperature. These are maximum series figures; the selected pump size and reviewed duty curve govern the actual operating point.

What information do I need to select an API 610 OH2 pump?

Start with the required flow, head, process liquid, operating temperature and pressure. If available, include the project specification, NPSHa, material requirements and seal / auxiliary requirements.

Is this page intended for a new pump or an existing pump replacement?

This page is primarily for new API 610 OH2 duties. Existing Goulds 3700 and Sulzer installations should follow the dedicated replacement engineering routes shown above.

Can you review an existing performance curve?

Yes. An existing curve or duty point can be used as an engineering input. Final pump selection is confirmed against the complete operating and process requirements.

Can materials and seal arrangements be configured for the application?

Material and seal requirements are reviewed against the process fluid, temperature, pressure and project specification. Final available options must follow the selected product configuration and verified factory data.

Do I need to complete a full API datasheet before requesting a quote?

No. A duty point, process description or purchasing specification is enough to begin an engineering review. Additional details can be confirmed after the first review.

Can you review API 610 requirements for the current project edition?

Project compliance should be reviewed against the edition and purchaser specification stated in the inquiry. Do not assume every project uses the same edition or optional requirements.

FAST RFQ

Request an API 610 OH2 Pump Quote

Paste the purchasing specification or enter only the duty and project details you already know. Engineering can confirm any additional information after review.

Tell us about your API 610 OH2 requirement

Paste the buyer specification as received, or complete only the fields you already know.

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