APIRotating Equipment

API 674

Positive Displacement Pumps — Reciprocating

US / International
Rotating Equipment

Reference profile

Designation
API 674
Title
Positive Displacement Pumps — Reciprocating
Issuing body
American Petroleum Institute (API)
Current edition
3rd Edition (Reaffirmed 2021 / ISO 13710 Equivalent)
Status
Active; international benchmark standard for heavy-duty reciprocating displacement pumps.
Category
Reciprocating Positive Displacement Pump Standard
1

Overview

API Standard 674 (ISO 13710) covers the minimum requirements for reciprocating positive displacement pumps and pump units for use in the petroleum, petrochemical, and natural gas process industries.

Both direct-acting pumps and power-driven pumps (simplex, duplex, triplex, quintuplex, multiplex) are covered. These units excel in high-pressure, fixed-volume services where discharge pressure is independent of flow rate.

2

Scope & Applicability

Covers

  • Pump Types: Power pumps (motor/engine-driven via crankshaft and connecting rods: Simplex, Duplex, Triplex, Quintuplex) and Direct-acting pumps (steam/gas-driven).
  • Liquid End (Fluid End) Mechanical Construction: Forged block cylinders, replaceable liners, plungers/pistons, suction/discharge valves (disc, wing, spherical), stuffing box packing, and lubrication/flush systems.
  • Power End Mechanical Construction: Heavy-duty cast iron/steel frames, crankshafts, connecting rods, crossheads, and splash or forced lubrication systems.
  • Pulsation Control: Suction and discharge pulsation suppression devices (dampeners/stabilizers) and acoustic/vibration design analysis.
  • Testing Requirements: Hydrostatic testing (1.5x MAWP), mechanical running performance test, NPSH margin verification, and NDE of forged liquid ends.

Does NOT cover (exclusions)

  • Controlled volume metering pumps—covered by API 675.
  • Rotary positive displacement pumps (screw, gear, vane)—covered by API 676.
  • Centrifugal process pumps—covered by API 610.
  • In-service overhaul procedures and field packing replacement—refer to vendor maintenance manuals.
3

Key Requirements

Pulsation & Vibration Control (Design Approaches 1, 2, 3)

  • Design Approach 1: Basic dampener sizing using standard empirical mathematical relationships.
  • Design Approach 2: Acoustic simulation of the pump and piping system to eliminate acoustic resonance peaks.
  • Design Approach 3: Combined acoustic simulation and mechanical piping dynamic stress analysis for high-energy or multi-pump installations.

Liquid End (Fluid End) High-Pressure Design

  • Forged Block Construction: Forged carbon steel, stainless steel, duplex, or nickel alloy blocks are mandatory for severe high-pressure services to prevent fatigue cracking.
  • Valves & Seats: Replaceable disc, wing-guided, or spherical check valves with hardened seats to resist erosion and high differential pressures.

Overpressure Protection & Safety Provisions

  • Mandatory Safety Relief Valve (PSV): A liquid-certified safety relief valve must be installed on the discharge piping upstream of any isolation valve.

Inspection & Hydrostatic Testing

  • Hydrostatic Test: Liquid end pressure-retaining components must be hydrostatically tested at a minimum of 1.5x MAWP for at least 30 minutes.
  • Mechanical Running Test: Shop performance running test at rated speed, pressure, and capacity for at least 4 hours to verify volumetric efficiency, vibration, and bearing temperatures.
4

Technical Details

Pulsation Peak-to-Peak Limit: Peak-to-peak pressure pulsation in the line piping must be suppressed to less than 1.5% to 3.0% of average operating pressure.

NPSH Margin Requirement: NPSHA must exceed NPSHR by at least 1.0 m to 1.5 m (3 ft to 5 ft) to prevent fluid flashing in the suction stroke.

Volumetric Efficiency Benchmark: Typical API 674 plunger pumps achieve high volumetric efficiency (90% to 98%) depending on fluid compressibility and valve response.

Where to find it in the codeConsult API 674 Section 6 for Basic Design (Liquid End, Power End, Valves, Plungers, Dampeners), Section 7 for Accessories & Relief Valves, Section 8 for Inspection & Testing, and Annex 6C for Pulsation Control Guidelines.
5

Engineering Notes

  • Never install a block valve between a positive displacement pump discharge and its safety relief valve (PSV); positive displacement pumps can generate infinite pressure until structural rupture if blocked.
  • Mount pulsation dampeners as close as possible to the liquid end suction and discharge flanges (within 1 to 2 pipe diameters) for maximum dampening effectiveness.
  • Specify a dedicated packing flush/lubrication system for toxic, corrosive, or abrasive services to extend plunger and stuffing box packing life.
6

Related Standards

  • API 675

    Positive Displacement Pumps—Controlled Volume (Metering Pumps).

  • API 676

    Positive Displacement Pumps—Rotary.

  • API 618

    Companion or referenced standard; verify its exact relationship in the adopted edition.

7

Source, Edition & Status

Publisher
API
Edition Year
N/A
Industries
Refinery, Petrochemical, Oil & Gas
Content Status
reviewed
Last Reviewed
2026-07-01
Last Updated
2026-07-01
Verified By
Engineering Reviewer
Official Link
www.api.org

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