Screw Pump Mechanical Seal Options - API 682 Compliance Guide

Complete guide to mechanical seal arrangements for screw pumps including API 682 flush plans, seal types, and material selection for Equipment Engineers.

API 682API 676

Mechanical Seal Basics

How Mechanical Seals Work

┌─────────────────────────────────────────────────────┐
│                                                     │
│     Rotating Face ────────► ◄──────── Stationary   │
│     (on shaft)      Thin film        Face (in      │
│                     of fluid          housing)     │
│                                                     │
│     Spring pressure maintains contact               │
│     Fluid film provides lubrication                 │
│                                                     │
└─────────────────────────────────────────────────────┘

Key Components

ComponentFunction
Rotating faceAttached to shaft, rotates
Stationary faceFixed to housing
Secondary sealsO-rings, gaskets
Spring/bellowsMaintains face contact
Drive mechanismTransmits rotation

Seal Arrangements

Single Seal (Arrangement 1)

Process ─────┤ SEAL ├───── Atmosphere
             ╔═════╗
             ║     ║
         ═══════════════
             Shaft

Applications:

  • Non-hazardous fluids
  • Standard process service
  • Most common arrangement
  • Lower cost

Tandem Seals (Arrangement 2)

Process ─┤ SEAL 1 ├─ Buffer ─┤ SEAL 2 ├─ Atm
         ╔═══════╗           ╔═══════╗
         ║       ║   Fluid   ║       ║
     ════════════════════════════════════
                  Shaft

Applications:

  • Hazardous fluids requiring backup
  • When leak detection needed
  • Extended seal life
  • Not zero-emission

Double Seals (Arrangement 3)

Process ─┤ SEAL 1 ├─ Barrier ─┤ SEAL 2 ├─ Atm
         ╔═══════╗   (Higher  ╔═══════╗
         ║       ║   pressure)║       ║
     ════════════════════════════════════
                  Shaft

Applications:

  • Zero emission required
  • Highly hazardous fluids
  • Carcinogenic fluids
  • Regulatory requirements

API 682 Overview

Standard Scope

API 682 defines standard piping configurations (flush plans) for mechanical seals on:

  • Centrifugal pumps (API 610)
  • Rotary pumps (API 676)
  • Includes screw pumps

Seal Categories

CategoryServiceTypical Applications
1Light hydrocarbonsPropane, butane
2General refineryMost process fluids
3High temperature/criticalHot oil, critical service

API 682 Flush Plans for Screw Pumps

Single Seal Plans

PlanDescriptionBest For
Plan 01Pump discharge to seal chamberSimple, low-cost
Plan 02Circulation through pumping ringSome cooling
Plan 11Discharge through orifice to sealStandard choice
Plan 12Plan 11 + strainerHigh viscosity
Plan 13Reverse circulation to suctionHot fluids
Plan 14Circulation to cooler to sealHigh temperature
Plan 21External clean fluid supplyDirty/abrasive
Plan 23Circulation through heat exchangerHot service
Plan 31Cyclone separator to sealSolids in fluid
Plan 32External buffer with reservoirEnhanced cooling

Tandem/Double Seal Plans

PlanDescriptionApplication
Plan 52External buffer with pressurized reservoirTandem seals
Plan 53APressurized reservoir (accumulator)Double seals, standard
Plan 53BBladder accumulator systemDouble seals, compact
Plan 53CPump-circulated barrierHigh heat load
Plan 54External barrier fluid supplyDouble seals, large

Plan Selection for Screw Pumps

Standard Service: Plan 11

         ┌─────┐
Discharge│ ○   │← Orifice (restricts flow)
    ─────┤     │
         │ SEAL│
         │     │
    ─────┤     │
Seal     └─────┘
Chamber

Flow: Discharge → Orifice → Seal → Drain back to process

When to Use:

  • Clean fluids
  • Viscosity < 200 cSt
  • Temperature < 80°C
  • Most standard applications

Advantages:

  • Simple installation
  • No external piping
  • Low cost
  • Reliable

High Viscosity Service: Plan 12

         ┌─────┐
Discharge│ ▣   │← Y-Strainer (removes particles)
    ─────┤ ○   │← Orifice
         │ SEAL│
         │     │
    ─────┤     │
         └─────┘

Flow: Discharge → Strainer → Orifice → Seal → Drain

When to Use:

  • Viscosity > 200 cSt
  • Fluids with minor particles
  • Extended seal life needed
  • Self-venting required (horizontal pumps)

Advantages:

  • Removes particles before seal
  • Self-venting capability
  • Better seal life in viscous service
  • Standard strainer maintenance

Hot Service: Plan 13 or Plan 23

Plan 13: Reverse circulation (seal → suction)

  • Uses cooler suction as flush source
  • Simple, no heat exchanger

Plan 23: Includes heat exchanger

  • External cooling of flush fluid
  • For very hot service (>150°C)
  • Maintains seal face temperature

Zero Emission: Plan 53A/B/C

         ┌─────────────┐
         │ Accumulator │
         │ ▲           │
         │ │ Barrier   │
    ─────┤ │ Fluid     ├─────
         │             │
    ═════╡ SEAL 1│SEAL 2╞═════
         └─────────────┘

Barrier pressure > Process pressure
Zero process fluid emission

When to Use:

  • Carcinogenic fluids
  • Regulatory requirements
  • Zero emission mandate
  • Highly toxic service

Seal Face Materials

Common Combinations

ApplicationRotating FaceStationary Face
StandardCarbon graphiteSilicon carbide
High pressureTungsten carbideSilicon carbide
AbrasiveSilicon carbideSilicon carbide
ChemicalCarbon graphiteCeramic (Al₂O₃)
High tempSpecial carbonSilicon carbide

Material Selection by Fluid

Fluid TypeRecommended Faces
Clean oilsCarbon vs SiC
WaterCarbon vs SiC
CausticCarbon vs Ceramic
AbrasiveSiC vs SiC
Hot oilCarbon vs SiC (with cooling)
ChemicalConsult manufacturer

Elastomer Selection

Common Elastomers

MaterialCodeTemperatureChemical Resistance
Buna-N (NBR)NBR-30 to +100°COils, fuels
Viton (FKM)FKM-20 to +200°CMost chemicals
EPDMEPDM-50 to +150°CWater, caustic
Kalrez (FFKM)FFKM-20 to +300°CNearly universal
PTFEPTFE-200 to +250°CUniversal

Selection Guide

ApplicationRecommended
HydrocarbonsFKM (Viton)
Water/steamEPDM
Hot oil (>150°C)FFKM or PTFE
Chemical processFFKM
CryogenicPTFE

Specification Format

Seal Specification Template

=== MECHANICAL SEAL SPECIFICATION ===

Service:
Tag number: _______________
Pump model: _______________
Shaft size: ___ mm

Process Conditions:
Fluid: _______________
Temperature: ___ °C (normal), ___ °C (max)
Pressure at seal: ___ barg
Viscosity: ___ cSt

Seal Requirements:
Arrangement: □ Single □ Tandem □ Double
API 682 Category: □ 1 □ 2 □ 3
Flush Plan: Plan ___

Materials:
Rotating face: _______________
Stationary face: _______________
Elastomers: _______________
Metal parts: _______________

Flush System:
Plan: API 682 Plan ___
Flush fluid: _______________
Flush rate: ___ L/min
Inlet temperature: ___ °C

Special Requirements:
□ API 682 compliance required
□ Cartridge seal required
□ Monitoring provisions (pressure, temperature)
□ Other: _______________

Maintenance Considerations

Seal Life Expectations

ServiceTypical Life
Clean, light duty3-5 years
Standard process2-3 years
Harsh/abrasive1-2 years
High temperature1-2 years

Maintenance Activities

ActivityFrequency
Flush pressure checkWeekly
Visual inspectionMonthly
Flush flow verificationQuarterly
Strainer cleaning (Plan 12)Quarterly
Full seal inspectionAnnual

Summary: Plan Selection Guide

ApplicationRecommended Plan
Standard servicePlan 11
High viscosity (>200 cSt)Plan 12
Hot service (>80°C)Plan 13 or 23
Dirty/abrasive fluidPlan 21 or 31
Hazardous (backup needed)Plan 52 (tandem)
Zero emission requiredPlan 53A/B/C (double)
Very high temp (>150°C)Plan 23 + cooling

Frequently Asked Questions

What is the standard seal arrangement for screw pumps?
Single mechanical seal with API 682 Plan 11 or Plan 12 is standard for most applications. Plan 11 provides basic flush from discharge; Plan 12 adds filtration for viscous fluids or those with particles.
When should I specify double or tandem seals?
Specify double seals for zero-emission requirements or extremely hazardous fluids. Use tandem seals when backup protection is needed but zero emission is not required. Both require Plan 52, 53A/B/C, or 54.
What flush plan is best for high viscosity fluids?
Plan 12 (with Y-strainer/filter) is best for high viscosity. The filter removes particles and the plan self-vents air pockets. For very high viscosity (>1000 cSt), Plan 21 with external cooled supply may be needed.

📚References & Sources

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