1. Presented by:
Aditya Kumar, GEA (Mechanical)
Ammonia-II Plant
P. No.- 504661
Presentation on
Mechanical Seal &
Steam Trap
2. What is Shaft Seal ?
The shaft seal is a sealing
element which seals the
rotating shaft of a centrifugal
pump where it passes through the
non-rotating pump casing.
Shaft Seal reduces fluid leakage to
atmosphere or the entry of air from
outside to a certain level.
4. Types of Dynamic Seal
LABYRINTH SEAL:
It is a clearance type seal. There are no rubbing parts and always positive
clearance is maintained between Stationary and rotating part. It is used in
Turbine & Compressor.
CARBON RING SEAL:
Here carbon ring is used, which is in 3-4 parts and held together by means of
spring and provide circulatory form. Generally clearance of 0.03-0.07mm is
maintained between the carbon ring and rotor. This type of seal is used in
Steam Turbine (Governor).
5. Types of Dynamic Seal
GLAND PACKING:
Packing directly touches the rotor and thereby power loss is very high. Here
leakage rate is essential otherwise the packing will burn due to high temperature.
Therefore this type of packing is used where minor leakage is allowed. As packing
needs to be regularly changed ,equipment downtime is high. Generally reciprocating
pumps have this type of seal.
MECHANICAL SEAL:
In this case there is no leakage .Also power loss is very less. Generally Centrifugal
pump have this type of seal.
6. Mechanical Seal
A Mechanical seal is a device which prevent leakage of fluids along
rotating shafts. Primary seal face is at right angle to the axis of rotation
between one stationary ring and one rotating ring.
To minimize leakage.
To prevent leakage of toxic fluid.
O-Ring
7. API Standard
The American Petroleum Institute is the largest U.S. trade association for the oil
and natural gas industry. The American Petroleum Institute was founded on 20
March 1919.
API Standards enhance the safety of industry operations, assure quality, help
keep costs down, reduce waste, and minimize confusion.
ASME is a construction codes (Dimension & Tolerances) that covers Design,
Fabrication and construction issues While API code governs the continued
operation, Inspection & Repairs.
For eg. ASME Section VIII covers fabrication of Pressure Vessel but once the
pressure vessel are put in service, API 510 takes place.
According to a study from the U.S. Department of Commerce, one
petrochemical manufacturer reduced costs by $2.5 million in one year by
implementing an industry-developed risk-based inspection methodology for
process equipment.
8. API 682 about Mechanical Seal
Size of Shaft from 30 MM to 120 MM.
Fluid temperature -30°C to 260°C and Pressure 0 Bar to 34.5 Bar.
Flushing Connection on the gland plate shall be ¾” NPT and Vent & Drain
connection shall be ½” or 3/8” NPT.
The clearance between Shaft OD and shaft Sleeve bore shall be 0.025 to
0.075MM.
Only Solid faces shall be used (Coated face are not allowed).
The seal is to be tested in four different test fluids such as water, Propane,
20%NaOH and Mineral Oil.
Dynamic test is required for minimum 100 hours at 3600 RPM and Static test
shall be for 4 hours.
For Dual Seal ,Each seal to be separately tested and Seal should have Minimum
3 years continuous running life.
9. Parts of Mechanical Seal
A - Stationary face
B - Rotating face
C - Sleeve
D - Gland Plate
E - Stuffing box
1 - O-ring
2 - Dynamic O-ring
3 - Sleeve gasket
4 - Sealing interface
5 - Gland gasket
10. Sealing Points Of Mechanical Seal
• Between the shaft and the sleeve.
• Between the rotating component and the sleeve.
• At the mating surfaces of the primary and mating rings.
• Between the stationary component and the gland plate.
• Between the gland plate and the stuffing box.
IMPELLER
SIDE DRIVE SIDE
11. Balance & Unbalance Seal
The opening area or face area of the balanced seal is same as the unbalanced
seal, but the closing area is maintained in proportion to the face area. As we
reduce the closing area, the closing force also gets reduced. Thus, less heat gets
generated, and we get extended life of the seal.
The balance ratio is Ac/Ao.
Seal Balance Ratio= (Db
2
– Di
2
) / (Do
2
– Di
2
)
where
Do is the seal face outside diameter;
Di is the seal face inside diameter;
Db is the balance diameter of the seal.
12. Balance & Unbalance Seal
UNBALANCE SEAL
In unbalance seal full value of the
pressure sealed is exerted on sealing
faces.
Unbalance seal is used for low
pressure application.
Generally unbalance seal can be
recommended up to 10 kg/sq.cm.
BALANCE SEAL
A step in sleeve is used to relieve
the fluid pressure across seal face.
For higher pressure only balanced
seal is used.
In case of balanced seal wear-tear is
low & heat generation is less which
ensures long life of seal.
Generally 70-75% balancing is used.
14. Component & Cartridge Seal
A component seal consist of a separate rotating member and stationary seat
that mount in a gland or housing. Since they are not preset, installation and
maintenance are generally more difficult and require precise measurements
during installation to prevent seal failure.
The cartridge seal is an arrangement of seal components on a shaft sleeve and
in a seal gland constituting a single unit that is usually assembled and pre-set at
the factory i.e. cartridge type seals that are completely encased within secure
housings. . Both bellows and spring-type seals can be cartridge-arranged if the
pump stuffing box is large enough.
cartridge type seals that are completely encased within secure housings.
Further, non-cartridge type seals require precise measurements during
installation to prevent seal failure.
17. Pusher Seal
As the seal springs and other pressures in the stuffing box are exerted on the seal,
closure of the seal faces is achieved.
As the softer carbon face wears down, the rotating face must move to maintain face
closure.
The dynamic ‘O’ ring is designed to move axially (be pushed) along the shaft or sleeve.
Rotating face Stationary Face
Closing forces exerted
on the seal faces
• Used in low temp. services.
• Used in light end services (ethylene, propane, methane,
butane etc.).
• ‘O’ ring secondary seals.
18. Non-Pusher Seal
A non-pusher type seal consists of a bellows assembly.
The bellows is a component that acts as both the load
element (like a spring in a pusher type) and a secondary
sealing element like an ‘O’ ring in a pusher type). Because
the bellows prevents any leakage to the atmospheric side
of the seal, and has a large clearance between itself and
the shaft or sleeve it can move freely in the axial direction
(no dynamic ‘O’ ring), reducing the potential for hang up.
• Closing force supplied by bellows (no dynamic ’O’ ring)
• Metal bellows use ‘grafoil’ secondary seals to handle
high temperature
19. Single Seal & Multiple Seal
Single seals use the pump's fluid as a lubricant, while double seals have a
dedicated buffer or barrier liquid.
A single mechanical seal consists of two very flat surfaces that are pressed
together by a spring and slide against each other. Between these two surfaces is
a fluid film generated by the pumped product. An absence of this fluid film (dry
running of the pump) results in frictional heat and ultimate destruction of the
mechanical seal.
This fluid lubricates the seal faces and absorbs the heat generated from the
associated friction, which crosses the seal faces as a liquid and vaporizes into
the atmosphere. So, it's common practice to use a single mechanical seal if
the pumped product poses little to no risk to the environment.
A double mechanical seal consists of two seals arranged in a series. The inboard,
or “primary seal” keeps the product contained within the pump housing. The
outboard, or “secondary seal” prevents the flush liquid from leaking into the
atmosphere.
20. Double Seal
A double seal is an arrangement in which two mechanical seal are
utilized face to face, back to back or in tandem (facing the same
direction), allowing a barrier/buffer fluid or gas to be introduced between
the two sets of seal faces.
It has 2 Primary and 2 mating ring per seal with a barrier fluid between
two seals.
This type of seal is generally used for:
1. Flammable and toxic or otherwise dangerous fluids
2. Where seal face lubrication is required without diluting the pumped
liquid.
21. Back to Back Double Seal
Here two seals having back to back primary
rings & mating rings are used at extreme
ends.
This arrangement is more suitable for
sealing liquids at high vacuum.
Lubrication of both the seal faces is done by
barrier liquid at a pressure higher than
pump pressure by 1 to 1.5 kg/sq.cm.
In case of inboard seal failure the barrier
fluid will mix with pumped liquid but pumped
liquid will never leak out. So barrier fluid
must be compatible with pumped liquid.
22. Double Tandem Seal
Two seals in same direction facing fluid to be sealed & in series are used.
Outer seal acts as a safety seal in case inner seal fails.
Lubrication of inner seal is by pumping liquid itself & outer seal is lubricated by
barrier fluid.
Here barrier fluid pressure is less than pumping pressure. In case when inner
seal fails, the pumped liquid will mix with barrier fluid but barrier fluid will never
mix with pumped liquid.
This type of seal is mostly used where hazardous fluid to be pumped.
Eg. Tandem seal is used in Ammonia Pump P-3501A/B.
23. The Fluid Film
In most mechanical seals the faces are kept
lubricated by maintaining a thin film of fluid
between the seal faces. This film can either come
from the process fluid being pumped or from an
external source.
This is achieved by maintaining a precise gap
between the faces that is large enough to allow in a
small amounts of clean lubricating liquid but small
enough to prevent contaminants from entering the
gap between the seal faces.
The gap between the faces on a typical seal is as
little as 1 micron – 75 times narrower than a human
hair. Because the gap is so tiny, particles are
unable to enter otherwise damage the seal faces.
24. Seal Materials
Carbon Graphite , Tungsten Carbide , Silicon Carbide , Ceramics , Rubber
elastomers (Viton, PTFE, Neoprene) are the most common materials used in
Mechanical Seals.
Selection of material depends on operating temperature, pressure, corrosion
resistance property & compatibility with pumped fluid .
Carbon:
It is compatible with most of the chemicals.
It also has a good self lubricating properties for start up condition.
Excellent heat transfer properties.
Resin impregnated carbon which is generally used.
Metal impregnated (normally antimony), used for high temp. application.
Tungsten Carbide:
It has outstanding wear resistant characteristics & high modulus of Elasticity.
It is not suitable for high acidic liquids having Ph<4.
Cobalt bonded generally used in many chemicals .
Nickel bonded is generally used for BFW application and in refineries.
25. Seal Materials
SILICON CARBIDE:
It is corrosion resistant to most of the liquid except for highly alkaline liquids at
high temp.
First is resin bonded, used for high speed, high temp. applications due to its
lower coefficient of friction & higher hardness.
Second is alpha sintered and used for all general application. it has excellent
abrasive resistance.
CERAMIC:
This is basically aluminum oxide. It has good abrasion resistance properties.
But it can not take thermal shock, so it is used where temp. variation across the
face is lower than 100o
c .
26. Seal Materials
ELASTOMERS: Here operating temp. is main criteria. The material must retain
their flexibility at operating temp. And at the same time should be corrosion
resistant.
RUBBER ELASTOMERS: Usually viton, neoprene, etc are used. It’s compatibility
with pumped fluid should be checked.
GFT/PTFE ELASTOMERS: If rubber material is not compatible then these can be
used. GFT(glass filled teflon) is capable of handling high temp. than PTFE(poly
tetra flouro ethelene). sleeve wear is more with these materials than rubber.
GRAFOIL PACKING: For higher temp. application where rubber/GFT packing are
not suitable grafoil packing is used. But these can not be used in dynamic
condition, hence can not be used in pusher type seal heads. this is the only
packing used with metal bellows seals.
27. Face Flatness
The mechanical seal faces are obviously the most critical sealing point of a
mechanical seal assembly.
The faces can be manufactured of different materials, one is typically carbon, while
the other is usually a hard material. (i.e. Alox (Aluminum Oxide Ceramic), Tungsten
Carbide, Silicon Carbide, etc.)
In order for a seal to be achieved, the faces must be very flat. This is achieved by
machining the faces, then lapping them to a fine finish.
Flatness is measured in Light Bands. After lapping, the faces are placed on an
Optical Flat, a clear glass surface where a monochromatic light is shined on the
face.
This single wavelength light will produce an image of rings or lines on the face. Each
ring/line is One Light Band. Each light band is equivalent to .000011 or eleven
millionths of an inch(.29μm). This refers to the variations in the surface of the face.
On most face materials, one light band is found.
28. Face Flatness
Surface flatness of the sliding faces
Outer diameter of the sliding faces< 80 mm
2 light bands ( 0.58 μm)
Outer diameter of the sliding faces > 80 mm
1 light band ( 0.29 μm)
Sliding surface
with imperfect
flatness
Perfectly
flat surface
29. Internal recirculation from pump discharge
to seal & use for clean pumpage only
Recirculation from Pump discharge
through a flow control orifice to the seal
Recirculation from Pump discharge
through a strainer & flow control orifice to
the seal
Recirculation from Pump seal
chamber through a flow control
orifice and back to the pump suction
SEAL CHAMBER FOR
PLAN 13
Flush is injected into the seal chamber
from an external source Recirculation from Pump discharge through a
cyclone separator delivering the clean fluid
through seal cooler to seal chamber and fluid
with solids back to pump suction
API Seal Flush Plan
30. API Plan 52 & 62 (Quenching)
LBI- Liquid Buffer Inlet, LBO- Liquid Buffer Outlet
LSL- Level Switch Low LSH- Level Switch High
PI- Pressure Indicator PS- Pressure Switch
6- Reservoir, 7- Make up Buffer Fluid
F- Flush, V- Vent LI- Level Indicator
31. Causes of Seal Failure
Dry running.
Vaporization.
Abrasives in product.
Sludging.
Bad fitments.
Carbon ring erosion.
Face distortion.
O-ring extrusion.
Spring distortion.
32. Steam Trap
A Steam Trap is a device used to discharge condensates and non-condensable
gases with a negligible consumption or loss of live steam.
The operation of a steam trap depends on the difference in properties between
steam and condensate.
It is an automatic valve capable of discharging condensate and trapping the steam.
THE STEAM TRAPS CAN SENSED BETWEEN CONDENSATE AND STEAM IN
FOLLOWING WAY.
DIFFERENCE IN DENSITY (MECANICAL STEAM TRAP)
DIFFERENCE IN TEMPRATURE (THERMOSTATIC STEAM TRAP)
DIFFERENCE IN FLOW CHARACTERISTICS (THERMODYNAMIC STEAM TRAP)
33. Why Steam Trap is Necessary ?
All the latent heat associated with steam is used.
Condensate removal for pipe
Capable of discharging air and other non-condensable gases.
Water Hammering
Corrosion
Non-effective Heat Transfer
34. Mechanical Steam Trap & types
Inverted Bucket Trap
In Inverted Bucket steam traps, the bucket within the
trap is attached to a lever that opens and closes the
trap valve in response to the bucket’s motion.
Ball Float trap:
In ball float trap, as condensate enters the trap, the
float attached to a lever becomes buoyant and moves
the lever, causing the trap valve to open.
The float responds to condensate flow, opening and
closing the valve to compensate accordingly.
Mechanical traps are steam traps that operate on the principle of specific gravity (specifically the difference in
the specific gravities of water and steam).
They will continuously pass massive volumes of condensate and are suitable for a large range of process
applications.
35. Thermostatic Steam Trap
Thermostatic trap remove condensate through the temperature difference of
steam & Liquid phase (Condensate) i.e. it works on the difference in Enthalpy of
Steam and Condensate.
Balanced Pressure Trap:
The Flexible sealed element expands and contracts lengthwise under the influence
of internal & external Pressure.
Liquid Expansion Trap:
An oil filled element expands when heated to close the valve against the seat. The
adjustment allows the temperature of the trap discharge to be altered between 60°C
and 100°C.
Bimetallic Expansion trap:
Two metal having different coefficient of expansion are bonded together and heated
the composite piece will take up a curved shape. This movement with changing
temperature can be made to operate the valve of a steam trap.
36. Bimetallic Steam Trap
The Bimetallic Steam Trap uses the Thermostatic principle of the unequal
expansion of two metals (Bimetallic) at high temperatures to open and close the
Condensate drain valve.
When high-temperature Steam comes in, the Bimetal disk will heat and bend.
Causes the stem to move upwards to close the valve, but if condensate water gets
trapped in a steam trap, the condensate temperature will gradually decrease until
the Bimetal disk comes back straight and causes the stem to slide down to
open Valve.
37. Thermodynamic Steam Trap
The thermodynamic trap is an extremely robust steam trap with a simple mode of operation. The
trap operates by means of the dynamic effect of flash steam as it passes through the trap. The
only moving part is the disc above the flat face inside the control chamber or cap.
On start-up, incoming pressure raises the disc, and cool condensate plus air is immediately
discharged from the inner ring, under the disc, and out through peripheral outlets.
• Hot condensate flowing through
the inlet passage into the chamber
under the disc drops in pressure
and releases flash steam moving
at high velocity. This high velocity
creates a low pressure area under
the disc, drawing it towards its
seat.
38. Selection of Steam Traps
OPERATING CHARACTERISTICS
PRESSURE AND TEMPERATURE LIMITS
STEAM TRAP CAPACITY
MATERIALS
ADVERSE CONDITIONS
39. Steam Trap used in AMM-II
Ball Float Steam Trap
Make: M/s Spirax
Thermodynamic Steam Trap
Make: M/s Spirax Marshall
Bimetallic Steam Trap
Make: M/s Armstrong
40. Benefits of Effective Steam Trapping
A healthy steam trap population allows condensate to be removed from the steam
system effectively which means it can be re-used. We call this ‘condensate recovery’
and it saves energy and cost in a number of different ways:
Reduced fuel costs: Normally, condensate will contain around 25% of the usable
energy of the steam from which it came. Returning this to the boiler feed tank can save
thousands of pounds per year in energy alone.
Energy saving: Condensate returned to the feed tank reduces the need for boiler
blowdown, which is used to reduce the concentration of dissolved solids in the boiler.
This therefore reduces the energy lost from the boiler during the blowdown process.
Reduced water charges: Returning and re-using condensate reduces the
requirement for fresh replacement water.
Reduced chemical treatment costs: Re-using as much condensate as possible
minimises the need for costly chemicals to treat raw water.
Reduced effluent costs: In many countries there are restrictions on releasing effluent
at elevated temperatures so it must be cooled if discharged which incurs extra costs.