
Flowserve.com 11SSIOM000743-00 (EN/AQ) November 2022
682R Reservoir API 682 Compliant Reservoirs
Piping Plan 52 is an unpressurized dual seal system
which is used in services where no leakage to atmosphere
is tolerated. The system consists of dual mechanical seals
with a buffer uid between the seals. The buffer uid is
contained in the seal pot which is vented to a are, thus
maintaining the buffer uid pressure close to atmosphere.
Primary (inboard) seal leakage will be product leakage into
the buffer uid. There will always be some leakage.
Plan 52 relies on uid circulating from the reservoir to the
mechanical seal. Circulation can come from a circulation
feature in the mechanical seal and/or a thermosyphon
effect with the buffer uid. When a thermosyphon effect
is used, the circulation of liquid occurs due to natural
convention (as opposed to mechanical pumping). The
temperature difference between seal and reservoir will
cause different density across the loop; hence, thermal
expansion.
Warmer liquid will oat about the cooler, moving the buffer
uid upwards, from the seal towards the reservoir.
In a Piping Plan 52 there is an external reservoir providing
buffer liquid for the outer seal of an arrangement 2 seal.
The buffer liquid shall be maintained at a pressure less
than seal chamber pressure and less than 0.28 MPag
(2.8 barg, 40 psig).
Plan 52 works best with clean, non-polymerizing products
which have a vapor pressure higher than the buffer uid
pressure.
These products will ash in the supply tank and the vapor
can escape to the vent system. If the product has a
vapor pressure lower than the buffer uid or supply tank
pressure, the leakage will remain a liquid and will cause
the buffer uid level to rise.
Should excessive primary (inboard) seal leakage not be
detected early, the heavier process uid will displace the
buffer uid and can result in increased seal wear. Used
with dual unpressurized seals, high vapor pressure uids,
light hydrocarbons, hazardous or toxic uids, and heat
transfer uids. Refer to Figure 5 in the following page.
Piping Plan 53A is a pressurized dual seal system
which is used in services where no process leakage to
atmosphere is tolerated. The system consists of dual
mechanical seals with a barrier uid between them. The
barrier uid in the supply tank is pressurized to a higher
pressure than the seal chamber, normally 15 to 25 psig
(1 to 1.7 barg). Primary (inboard) seal leakage will be
barrier uid into the product. A small amount of leakage is
customary.
A Plan 53A is usually chosen over a Plan 52 for dirty,
abrasive or polymerizing products which would either
damage the seal faces or cause problems with the
barrier uid system if a Plan 52 is used. There are two
disadvantages to a Plan 53A which must be considered.
First, there will always be some leakage of barrier uid into
the product. Normally, this leakage will be minute, and
the leakage rate can be monitored via the level gauges
or other instrumentation; however, the product must be
able to accommodate a small amount of contamination
from the barrier uid. Secondly, a Plan 53A system is
dependent on having the supply tank pressure maintained
at the proper level. If the supply tank pressure drops, seal
leakage direction will be reversed (the seal system will
begin to operate like a Piping Plan 52) and the barrier uid
will be contaminated with the process uid.
Used with high vapor pressure uids, light hydrocarbons,
hazardous or toxic uids, heat transfer uids, dirty/
abrasive or polymerizing uids, and mixer or agitators and
vacuum services, refer to Figure 6.