Standards explainer

API 682 mechanical seals: what to check in a pump tender

A plain-English overview of API 682 seal categories, arrangements, types and piping plans for bid engineers at pump and seal makers, with the seal items that most often become deviations.

By Ademola Afolabi, Founder, New Odyssey Ltd · Last reviewed:

The short answer

API 682 is the API standard for shaft sealing systems on centrifugal and rotary pumps. It covers the mechanical seal and its support system. In a pump tender, check the seal category, arrangement, type and piping plan against the pump datasheet and owner specification, and record every gap as a deviation.

Key Takeaways

  • API 682 covers shaft sealing systems for centrifugal and rotary pumps: the seal and its support system.
  • Seals are described by category (1, 2, 3), arrangement (1, 2, 3) and type (A, B, C), plus a piping plan.
  • The pump datasheet or owner specification usually sets these; the seal maker answers on a seal datasheet.
  • Piping plan, arrangement and support-system scope are the most common sources of seal deviations.

What API 682 covers

API 682, "Pumps: Shaft Sealing Systems for Centrifugal and Rotary Pumps", sets requirements for mechanical seals and their support systems in petroleum, natural gas and chemical service. Pump tenders usually call it up from the pump specification or from API 610, which refers to API 682 for seals. The seal is normally bought by the pump maker from a seal maker, so the bid engineer has to pass the seal requirements on and check the answer that comes back.

Categories, arrangements, types and piping plans

How API 682 describes a seal (own summary, not API text)
TermWhat it describesIn outline
CategoryThe seal's intended duty and the testing and documentation behind itCategory 1 for pumps not built to API 610, Category 2 for API 610 pumps, Category 3 the most demanding
ArrangementHow many seals there are and how the space between them works1: one seal per cartridge. 2: two seals with an unpressurised buffer fluid. 3: two seals with a pressurised barrier fluid
TypeThe seal designA: pusher seal with elastomer O-rings. B: metal bellows with elastomers. C: metal bellows with flexible graphite, for higher temperatures
Piping planThe fluid, piping and instruments that support the sealFor example Plan 11 (flush from pump discharge), Plan 52 (unpressurised buffer), Plans 53A, 53B, 53C (pressurised barrier) and Plan 54 (external barrier system)

Where seal deviations come from

Seal items to check against the pump datasheet and owner specification
ItemWhat to checkTypical deviation or clarification
Category, arrangement, typeAgainst the datasheet and owner seal rulesSingle seal offered where a dual seal is asked for; different type
Piping planPlan number and its componentsPlan 53A offered where 53B is specified
Support system scopeWho supplies reservoirs, accumulators, coolers, instruments and pipingSeal system by others; scope split unclear
InstrumentsOwner instrument rules, hazardous-area ratings, approved makersSeal maker's standard instruments differ from owner rules
MaterialsFace and secondary seal materials for the fluidDifferent face pair or elastomer offered
Qualification and testsQualification test evidence and any extra tests or witness pointsTest report covers a similar seal, not the one offered
DocumentsSeal datasheet, drawings, plan schematic, certificatesDocument not offered or late

Record each gap as one row in your technical deviation list, with the clause, what you offer, a justification and a cost of withdrawal. The pump manufacturers page has a worked example of a Plan 53A against 53B deviation.

How OdysseyGPT helps

OdysseyGPT reads the whole tender package, including the pump and seal specifications, datasheets, requisition and ITP. It checks each requirement against your own seal and pump datasheets, standard specifications and test procedures, and gives each one a status with a quote and page reference. It exports an editable compliance matrix and a deviations & clarifications list. It does not select seals or piping plans, read P&IDs or certify compliance; your engineers decide every open item. See OdysseyGPT for manufacturing.

Buyer questions

20 questions bid engineers, proposal engineers and buyers ask. Last reviewed:

What does API 682 cover?

API 682 covers shaft sealing systems for centrifugal and rotary pumps. That means the mechanical seal itself and the support system around it, such as piping plans, reservoirs and instruments. It is used mainly in petroleum, natural gas and chemical service. Pump tenders usually call it up from the pump specification or from API 610.

How does API 682 relate to API 610?

API 610 covers the centrifugal pump and refers to API 682 for the seal. In practice, the pump datasheet or owner specification names the seal arrangement and piping plan, and the seal maker fills in an API 682 seal datasheet. A pump offer needs both to agree. Check them side by side. See API 610 datasheet review.

What are the seal categories in API 682?

API 682 has three seal categories: 1, 2 and 3. Category 1 is aimed at pumps that are not built to API 610, such as chemical process pumps. Category 2 is for API 610 pumps. Category 3 is the most demanding, with the widest testing and documentation. Check the category the tender asks for before you price the seal.

What are seal arrangements 1, 2 and 3 in API 682?

The arrangement says how many seals there are and how the space between them works. Arrangement 1 has one seal per cartridge. Arrangement 2 has two seals with a buffer fluid at a lower pressure than the seal chamber. Arrangement 3 has two seals with a barrier fluid at a higher pressure than the seal chamber.

What are seal types A, B and C in API 682?

The type describes the seal design. Type A is a pusher seal with elastomer O-rings. Type B is a metal bellows seal with elastomer secondary seals. Type C is a metal bellows seal with flexible graphite secondary seals, used at higher temperatures. If a tender names a type, an offer of a different type is a deviation.

What is a seal piping plan?

A piping plan is a numbered layout for the fluid, piping and instruments that support the seal. For example, Plan 11 sends pumped fluid from the discharge to the seal chamber. Plan 52 uses an unpressurised buffer fluid. Plans 53A, 53B and 53C pressurise a barrier fluid between dual seals. The plan drives cost, so check it carefully.

What is the difference between Plan 53A and Plan 53B?

Both pressurise a barrier fluid between two seals. Plan 53A uses a reservoir pressurised by an outside gas source, often nitrogen. Plan 53B uses a bladder accumulator and usually a cooler, so the barrier fluid sits in a closed loop. Plan 53B costs more. Offering 53A where 53B is specified is a common deviation in pump tenders.

What is Plan 54 in API 682?

Plan 54 supplies a pressurised barrier fluid from an external system, rather than a seal pot or accumulator next to the pump. It is often used where many pumps share one barrier system. In a tender, check who supplies the external system and where your scope ends. Unclear scope splits are a frequent source of clarifications.

What is API 682 seal qualification testing?

API 682 asks seal makers to qualification test representative seal designs under set conditions. The test shows the design works before it goes into service. Tenders often ask for proof that the offered seal is covered by a qualification test. Make sure the test report covers the seal you offer, not just a similar one.

Which edition of API 682 should a pump tender name?

The tender should name one edition, and your offer should state the edition your seal is built and tested to. Owner specifications are sometimes written to an older edition, and arrangement or category rules can differ between editions. If the tender says latest edition, confirm which one you mean in your offer as a clarification.

What are the most common API 682 deviations in pump tenders?

Typical ones are a different piping plan, a single seal offered where a dual seal is asked for, a different seal type or category, and seal support systems supplied by others. Other common gaps are instrument types, reservoir size, cooler design and face materials. Each needs its own row with a justification and a price.

How do I check a seal datasheet against API 682 and the pump spec?

Check the category, arrangement, type and piping plan first. Then check face and secondary seal materials, the seal chamber conditions, buffer or barrier fluid, instruments and alarms, and the support system scope. Compare each line with the pump datasheet and owner specification. Any mismatch goes into your technical deviation list.

Why do seal support instruments cause clarifications?

Owners often set their own rules for transmitters, gauges, level devices and switches on seal pots and accumulators. Those rules can differ from the seal maker's standard kit. Hazardous-area ratings and approved vendor lists add more. Check each instrument against the owner's instrument specification and list any you supply differently.

Does API 682 cover gas seals on pumps?

Yes. API 682 includes non-contacting seal designs and gas-supported piping plans for pumps, such as dual seals that run on a gas barrier. Gas seals for compressors are a separate topic, covered by other standards. In a pump tender, check that the seal and gas supply plan match what the datasheet asks for.

What seal documents do EPCs ask for?

Usually a completed seal datasheet, a cross-section drawing, a piping plan schematic, a bill of materials, qualification test evidence, test reports and material certificates. The vendor data requirements list says which ones and when. Check that the pump maker and seal maker agree who supplies each item. See the VDRL guide.

Who answers the API 682 part of a pump tender?

Usually the pump maker answers the tender, with seal data from a seal maker. That makes coordination the hard part. The pump bid engineer must pass the right seal requirements to the seal supplier and check the reply before it goes into the offer. Missed handovers lead to late clarifications and repricing.

What do owner specifications usually add to API 682?

Owners often add preferred piping plans for certain services, limits on single seals for hazardous or toxic fluids, approved seal makers, instrument rules and extra tests or witness points. Some also add rules on the seal support system layout. Read the owner pump and seal specifications together, as requirements are often split across both.

When does a pump tender usually ask for a dual seal?

Dual seals are often asked for in hazardous, toxic, flammable or volatile services, or where leaks to the air must be kept very low. The exact rule comes from the owner specification and the seal selection logic it follows. Do not assume. Check the datasheet and the owner rules for each tag before choosing an arrangement.

How does OdysseyGPT check API 682 seal requirements in a tender?

It reads the whole tender package, including the pump and seal specifications, datasheets and requisition. It checks each seal requirement against your own seal datasheets, standard specifications and test procedures. Each requirement gets a status with a quote and page reference. You export an editable compliance matrix and a deviations and clarifications list.

What can OdysseyGPT not do for API 682 seal selection?

It does not select seals or piping plans, size reservoirs or coolers, or do any seal design calculation. It does not read piping plan drawings or P&IDs. It cannot check what API 682 says unless that text is in the documents you upload. It does not certify compliance. Your engineers decide every seal choice and every open item.

Frequently asked questions

Is API 682 only for API 610 pumps?

No. Its title covers centrifugal and rotary pumps, and its Category 1 seals are aimed at pumps not built to API 610. Check which category the tender asks for.

Who fills in the API 682 seal datasheet?

The buyer or pump maker sets the duty and selections, and the seal maker fills in what it offers. The pump maker should check the seal maker's answer against the tender.

References

API Standard 682: Pumps: Shaft Sealing Systems for Centrifugal and Rotary Pumps

American Petroleum Institute

Buy the current edition from API or a standards reseller.

Visit source

What API 682 says on mechanical seal selection

Turbomachinery Magazine

Visit source

API 682 Plan 53B

Swagelok

Visit source

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