application engineering api 682 - sealmaticindia.com · step iv: completes the sealing system...
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®
Mechanical Seals & Supply Systems for:Refinery & Petrochemical Applications
Selection and application recommendations according to API 682.
APPLICATION ENGINEERING
API 682
AE 3
/ 0
5-20
14
Step I Category
Category 1 Category 2 Category 3
ISO 3069 type C, ASME B73.1 , ASME B73.2 ISO 13709 / API 610 10th edition
-40 °C … 260 °C, 21 bar g (-40 °F … 500 °F, 300 PSI) -40 °C … 400 °C, 41 bar g (-40 °F … 750 °F, 600 PSI)
Minimal data requirements Rigorous data requirements
Step II Arrangement and configuration
Arrangement 1 1CW-FX
Single seal cartridge Contacting Wet - FiXed throttle bushingCategory 1: carbon throttle bushingCategory 2: non-sparking metal throttle bushingCategory 3: not applicable
1CW-FL
Contacting Wet - FLoating throttle bushingCategory 3: carbon throttle bushingCategory 1 and 2: carbon throttle bushing
Arrangement 2 2CW-CW
Dual seal cartridge- pressure between seals
less than seal chamber pressure
- internal reverse balance feature
- fixed carbon throttlebushing
Contacting Wet - Contacting Wet
2CW-CS
Contacting Wet - Containment Seal (non-contacting or contacting CS)
2NC-CS
Non-Contacting - Containment Seal (non-contacting or contacting CS)
Arrangement 3 3CW-FB
Dual seal cartridge- pressure between seals
higher than seal chamber pressure
- internal reverse balance feature
- fixed carbon throttlebushing
Contacting Wet - Face-to-Back
3CW-BB
Contacting Wet - Back-to-Back
3CW-FF
Contacting Wet - Face-to-Face
3NC-BB
Non- Contacting - Back-to-Back
3NC-FF
Non-Contacting - Face-to-Face
3NC-FB
Non-Contacting - Face-to-Back
Step III Type and spring position Flexible element
Type A Rotary springs
Pusher sealTemperature: -40 to 176 °C (-40 to 350 °F)Pressure: 41 bar g (600 PSI)Multiple springs: Alloy C-276Single spring: SS 316O-rings: FKM or FFKM
NBR, HNBR, EPM, EPDM, TFE …
Seal face surface speed < 23 m/s
Stationary springs
Seal face surface speed > 23 m/s
Type B Rotary bellows
Metal bellows seal with O-ringsTemperature: -40 to 176 °C (-40 to 350 °F)Pressure: 21 bar g (300 PSI)Metal bellows: Alloy C-276O-rings: FKM or FFKM
NBR, HNBR, EPM, EPDM, TFE …
Stationary bellows
Type C Rotary bellows
Metal bellows seal with flexible graphiteTemperature: -40 to 400 °C (-40 to 750 °F)Pressure: 21 bar g (300 PSI)Metal bellows: Alloy 718Sealing element: flexible graphite
Stationary bellows
Totally Engineered Sealing system (ES)
For service conditions outside the operating limits of type A, B and CTemperature: < -40 or > 260 °C (< -40 or > 500 °F) category 1
< -40 or > 400 °C (< -40 or > 750 °F) category 2 and 3Pressure: > 21 bar g (300 PSI) category 1
> 41 bar g (600 PSI) category 2 and 3Surface speed: > 23 m/s (75 ft/s)Shaft diameter: below 20 mm (0.75 inch) or above 110 mm (4.3 inch)Medium: highly corrosive fluids for which the specified materials in
API 682/ISO 21049 are not suitable, fluids with absolute vapour pressures > 34 bar a (493 PSI) , unstable liquid properties (e.g. multiphase, non-Newtonian), high viscosity or pour point above or within 20 °C (68 °F) of the mini -mum ambient temperature.
Default Optional
Optional
configurationsconfigurationsdesign feature
Categories, Arrangements and Seal Types
Classification of Sealing SystemsAPI 682 and ISO 21049 specify a range of different sealing systems. Parameters such as category, arrangement, configuration, type and API plans are to be considered.
The chart is a quick overview about the basic features of the different categories, arrangements and seal types. It also shows the links between these parameters and marks default and optional selections.
Step I: The category determines the applicable seal chamber, basic seal design features, maximum operating conditions, testing and data requirements. Each category has special demands regarding the seal arrangement, configuration and type. There are three different categories.
Step II: Determines the arrangement of the mechanical seal cartridges and their possible configurations.
The configuration determines the sealing method, orientation of the mechanical seal components, the use of containment seals and the required API plans. API 682 and ISO 21049 specify six default configurations and five optional configurations. Each of these configurations can be realized with different seal types.
Step Ill: Definition of the seal type, the design and material of the spring element and the secondary seals.It defines the appropriate operating limits. API 682 and ISO 21049 specify three basic seal types, a fourth option is a totally engineered sealing system (ES).
Step IV: Completes the sealing system classification by selecting the required API plan.
API 682 and ISO 21049 introduce a seal code which contains information about the category, arrangement, type and API plan.
1
QDF
1CW-FX Contacting Wet - FiXed throttle bushingExample: UFL850N (type B)
Plan 13Recirculation from seal chamber to suction
TI
FI
PI
Option SM ClientPlan 32External flush into the seal chamber
Plan 11Recirculation from discharge to seal chamber
plugged
Plan 61Plugged connections
F D Q
1CW-FL Contacting Wet - FLoating throttle bushing
drain
QuenchPlan 62External quench
LSH
drain
Plan 65Leakage control by float type level switch
Process side Atmospheric side
TI
Plan 23Internal recirculation through a cooler
Plan 31Recirculation from discharge through a cyclone separator to seal chamber
Default Optional
configurationsconfigurations
Each configuration is available for seal types A, B and C
Arrangement 1Single Seal Configurations and API Plans
2
LBO LBI
2CW-CW Contacting Wet – Contacting Wet
PI PSH
LSH
LSL
if specified
filling
flare
LI
Plan 52Unpressurized buffer fluid system
2CW-CS Contacting Wet – Containment Seal
2NC-CS Non-Contacting – Containment Seal
PI
M
PSLFSHFIL
if specified
SM Client
FE
PCV
Plan 72Buffer gas system
PI
LSH
PSH
flare
LI
drainif specified
Plan 75Condensate recovery for condensing leakage
PIPSH
flare
drain
Plan 76Vapour recovery system for non-condensing leakage
Process side Between seals
Plan 13Recirculation from seal chamber to suction
TI
FI
PI
Option SM ClientPlan 32External flush into the seal chamber
Plan 11Recirculation from discharge to seal chamber
Plan 14Recirculation from seal chamber to suction and circulation from discharge to seal chamber
Default Optional
configurationsconfigurations
Each configuration is available for seal types A, B and C
F
F CSV CSD GBI
CSV CSD GBI
Arrangement 2 Dual Seal Configurations and API Plans
Pressure between seals less than seal chamber pressure
3
3CW-FB Contacting Wet – Face-to-Back
3CW-BB Contacting Wet – Back-to-Back
3CW-FF Contacting Wet – Face-to-Face
WS\NNLK
Plan 02Dead end (plugged connections)
PI PSL
LSH
LSL
if specif ied
filling
N2
LI
Plan 53ABarrier fluid reservoir
Plan 54External barrier fluid system
Process side Between seals
PI
TI
PSL
if specif ied
filling
vent
Plan 53BBarrier fluid bladder accumulator system
PI
TI
PSL
LSL
filling
vent
PRV
LI
Plan 53CBarrier fluid piston accumulator system
Plan 13Recirculation from seal chamber to suction
Plan 14Recirculation from seal chamber to suction and circulation from discharge to seal chamber
Plan 11Recirculation from discharge to seal chamber
Default Optional
con�gurationscon�gurations
if specif ied
external source
Arrangement 3 Dual Seal Configurations and API Plans
Barrier fluid pressure higher than seal chamber pressure
4
3NC-FB Non-Contacting – Face-to-Back
PI
MPSL
FSHFIL
if specified
SM Client
FE
PCV
Plan 74Pressurized barrier gas
Process side Between seals
3NC-BB Non-Contacting – Back-to-Back
3NC-FF Non-Contacting – Face-to-Face
plugged
Plan 02Dead end (plugged connections)
Default Optional
configurationsconfigurations
Arrangement 3Dual Seal Configurations and API Plans
Barrier gas pressure higher than seal chamber pressure
5
Sealing systems selection by seal features
Arrangement Default configuration Type Flexible element
1Single seal cartridge
1CW-FX
Contacting Wet sealwith a FiXed throttle bushingapplicable API plans (process side):01 , 02, 11 , 12, 13, 14, 21 , 23, 31 , 32, 41applicable API plans (atmospheric side):51 / 61 , 62, 65
ARotary springsStationary springs
BRotary bellowsStationary bellows
CRotary bellowsStationary bellows
1CW-FL
Contacting Wet sealwith a FLoating throttle bushingapplicable API plans (process side):01 , 02, 11 , 12, 13, 14, 21 , 23, 31 , 32, 41applicable API plans (atmospheric side):51 / 61 , 62, 65
ARotary springsStationary springs
BRotary bellowsStationary bellows
CRotary bellowsStationary bellows
2
Dual seal cartridge
Operated with unpressurized buffer medium
2CW-CW(tandem)
Contacting Wet sealsapplicable API plans (process side):01 , 02, 11 , 12, 13, 14, 21 , 23, 31 , 32, 41applicable API plans (between seals):51 , 52
ARotary springsStationary springs
BRotary bellowsStationary bellows
CRotary bellowsStationary bellows
2CW-CS(tandem)
Contacting Wet inner sealwith a Containment Sealapplicable API plans (process side):01 , 02, 11 , 12, 13, 14, 21 , 23, 31 , 32, 41applicable API plans (between seals):71 , 72, 75, 76
ARotary springsStationary springs
BRotary bellowsStationary bellows
CRotary bellowsStationary bellows
3
Dual seal cartridge
Operated with pressurized barrier medium
3CW-FB(tandem)
Contacting Wet sealsin Face-to-Back arrangementapplicable API plans (process side):01 , 02, 11 , 12, 13, 14, 32applicable API plans (between seals):53A, 53B, 53C, 54
ARotary springsStationary springs
BRotary bellowsStationary bellows
CRotary bellowsStationary bellows
3NC-BB
Non-Contacting sealsin Back-to-Back arrangementapplicable API plans (process side):01 , 02, 11 , 12, 13, 14, 32applicable API plans (between seals): 74
ARotary springsStationary springs
BRotary bellowsStationary bellows
CRotary bellowsStationary bellows
Arrangement Most common optional configurations Type Flexible element
2 See above 2NC-CS (tandem) Non-Contacting inner seal with a Containment Seal A Rotary springs
3 See above3CW-BB Contacting Wet seals in Back-to-Back arrangement A Rotary springs3NC-FB (tandem) Non-Contacting seals in Face-to-Back arrangement A Stationary springs
Operation mode API plan Description
Primary flush
21/22 Circulation from pump discharge through cooler to seal23 Circulation of liquid from seal chamber through cooler to seal31 (41 ) Circulation from discharge through cyclone separator to seal32 Injection of clean liquid into seal chamber
Quench/buffer systems
51 External reservoir provides static liquid quench52 External reservoir provides circulation buffer liquid62 External source provides flowing quench liquid72 Gas buffer system
Barrier systems
53A Barrier liquid system with reservoir53B Barrier liquid system with bladder accumulator53C Barrier liquid system with fluid piston accumulator54 Barrier liquid system from external source74 Barrier gas system
Leakage collection/alarm
65 Recovery system with level control for liquid leakage75 Recovery system for condensing leakage76 Recovery system for non-condensing leakage
Default Optional
configurationsconfigurations
6
Standard seal type Temperature °C (°F)
Pressure bar g (PSI)
Mechanical seal Supply system
Type Arr.1) API plan2)
Non
-hyd
roca
rbon
sWater
< 80 (180)< 21 (300)
A
1 1121 … 41 (300 … 600)
> 80 (180) < 41 (600) 1 23
Sour water
< 80 (180)
< 21 (300)2 52
21 … 41 (300 … 600)
Caustic, amines, crystallize< 21 (300)
1 6221 … 41 (300 … 600)
H 2SO4 (max. 20% at 25°C)< 21 (300) 3 53A
H 3P04 (max. 20% at 80°C)
All other acids – ES 3 note 3)
Non
-flas
hing
hyd
roca
rbon
s
Absolute vapour pressureless than 1 barat pumping temperature
-40 … -5(-40 … 20)
< 21 (300)
A
3
53A53B or C21 … 41 (300 … 600)
-5 … 176(20 … 350)
< 21 (300) 53A53B or C21 … 41 (300 … 600)
176 … 260(350 … 500)
< 21 (300) C 02+53A21 … 41 (300 … 600) ES 02+53C
260 … 400(500 … 750)
< 21 (300) C 02+53A21 … 41 (300 … 600) ES 02+53C
Flas
hing
hyd
roca
rbon
s
Absolute vapour pressureabove 1 barat pumping temperature
-40 … -5(-40 … 20)
< 21 (300)
A
3
53A53B or C21 … 41 (300 … 600)
-5 … 176(20 … 350)
< 21 (300) 53A53B or C21 … 41 (300 … 600)
176 … 260(350 … 500)
< 21 (300) C 02+53A21 … 41 (300 … 600) ES 02+53C
260 … 400(500 … 750)
< 21 (300) C 02+53A21 … 41 (300 … 600) ES 02+53C
Optional seal typewhen specified
Temperature °C (°F)
Pressure bar g (PSI)
Mechanical seal Supply system
Type Arr.1) API plan2)
Non
-hyd
roca
rbon
s
Water< 80 (180)
< 21 (300) B or C 11121 … 41 (300 … 600)
ES 1> 80 (180) < 41 (600)
Sour water
< 80 (180)
< 21 (300) B or C 132
21 … 41 (300 … 600) ES 1
Caustic, amines, crystallize< 21 (300) B or C 1
6221 … 41 (300 … 600) ES 1
H 2SO4 (max. 20% at 25 °C)< 21 (300) B or C 3 53A
H 3P04 (max. 20% at 80 °C)
All other acids – ES 3 note 3)
Non
-flas
hing
hyd
roca
rbon
s
Absolute vapour pressureless than 1 barat pumping temperature
-40 … -5(-40 … 20)
< 21 (300)B or C 3 53A
21 … 41 (300 … 600) ES 3 53B
-5 … 176(20 … 350)
< 21 (300)B or C 3 02+53A
21 … 41 (300 … 600) ES 3 53B176 … 260(350 … 500)
< 21 (300) ES 3
note 3)21 … 41 (300 … 600) – –
260 … 400(500 … 750)
< 21 (300) ES 321 … 41 (300 … 600) – –
Flas
hing
hyd
roca
rbon
s
Absolute vapour pressureabove 1 barat pumping temperature
-40 … -5(-40 … 20)
< 21 (300)
ES3
53A21 … 41 (300 … 600) 53C
-5 … 176(20 … 350)
< 21 (300) 02+53A21 … 41 (300 … 600) 02+53C
176 … 260(350 … 500)
< 21 (300) 02+53A21 … 41 (300 … 600) 02+53C
260 … 400(500 … 750)
< 21 (300) 02+53A21 … 41 (300 … 600) 02+53C
1) A specific application may allow another seal arrangement. Please contact Sealmatic for further information.2) A specific application may allow additional or different API plans. Please contact Sealmatic for further information.3) The Sealmatic seal type and the API plan(s) are dependant on the specific operation conditions.
Seal Selection by Media Groups
7
Operating limitsp 1(max) = 41 bar g (600 PSI)t1 = -40…176 °C (-40 … 350 °F)v g(max) = 23 m/s (75 ft/s)
Materials*)Face: Carbon (A), SiC (Q1 , Q2)Seat: SiC (Q1 , Q2)O-rings: FKM, FFKM, EPDM, NBR, HNBR …Springs: Alloy C-276 **)
Other parts: SS316 (1 .4571)
B750VN
B750VP
B750VK
SBV
With pumping ring.
Operating limits and materials*)see B750VN
With reverse pressure feature.
Operating limits and materials*)see B750VN
With reverse pressure feature, stationary springs.
Operating limitsp1 (max) = 41…150 bar g (600…2,115 PSI)t1 = -40…176 °C (-40 …350 °F)v g(max) = 50…60 m/s (164…229 ft/s)
Materials*)Face: Carbon (A), SiC (Q1 , Q2), Seat: SiC (Q1 , Q2)O-rings: FKM, FFKM, EPDM, NBR, HNBR …Springs: Alloy C-276**)Other parts: SS316 (1 .4571)
Operating limits refer to default seal face combination Carbon/SIC
*) Default and optional materials available.**) in C-4 available, Sealmatic recommendation.
Pusher SealsType A
8
Metal Bellows SealsType B and C
UFL850N for arrangement 1 and 2 (external pressurization)UFL900N for arrangement 3 (internal pressurization)
Operating limitsp1 (max) = 25 bar g / 23 bar g (363 PSI / 334 PSI)t1 = -40…176 °C (-40…350 °F)v g(max) = 23 m/s (75 ft/s )
Materials*)Face: Carbon (A), SiC (Q1 , Q2), Seat: SiC (Q1 , Q2) O-rings: FKM, FFKM, EPDM, NBR, HNBR…, Other parts: SS316 (1 .4571) Bellows: Alloy C-276 (in Alloy 718 available, Sealmatic recommendation)
With pumping ring.
Operating limits and materials*)see UFL850/900N
With stationary bellows.
Operating limitsp1 (max) = 25 bar g (363 PSI)t1 = -40…400 °C (-40…750 °F)v g(max) = 50 m/s (164 ft/s)
Materials*)Face: Carbon (A), SiC (Q1 , Q2), Seat: SiC (Q1 , Q2)O-rings: Flexible graphiteBellows: Alloy 718Other parts: SS316 (1 .4571), Ni42 (1 .3917)
With rotary bellows. UFLWT800 for arr. 1 and 2 (ext. press.), UFLWT900 for arr. 3 (internal pressurization).
Operating limitsp 1(max) = 25 bar g / 23 bar g (363 PSI / 334 PSI)t1 = -20…400 °C (-4…750 °F)For temperatures below -20 °C (-4 °F) UFLCT 800/920v g(max) = 23 m/s (75 ft/s)
Materials*)Face: Carbon (A), SiC (Q1 , Q2), Seat: SiC (Q1 , Q2)O-rings: Flexible graphite, Bellows: Alloy 718Other parts: SS316 (1 .4571), Ni42 (1 .3917)
Operating limits refer to default seal face combination Carbon/SIC.
Default and optional materials available.
We
We
UFL850P
UFL650
UFLWT800/900
UFL850N/900N
*)
9
Operating limitsp 1(max) = 25 bar g (363 PSI)t1 = -20 … 176 °C (-4 … 350 °F)v g(max) = 23 m/s (75 ft/s)
MaterialsFace: Carbon (A), SiC (Q1 , Q2)Seat: SiC (Q1 , Q2)O-rings: FKM, FFKM, EPDM, NBR, HNBR …Springs: Alloy C-276**)Other parts: SS316 (1 .4571)
CSNon-contacting containment seal
Operating limitsp 1(max) = 2 bar g (29 PSI), dry operationt1 = -40 … 176 °C (-40 … 350 °F)v g(max) = 23 m/s (75 ft/s)
In the event of primary seal failure the CS will work as a conventional wet lubricated seal in pressures up to 60 bar g (870 PSI) for at least 8 hours. MaterialsFace: Special carbonSeat: Pressureless sintered SiCO-rings: FKM, FFKM, EPDM, FVMQ …Springs: Alloy C-276Other parts: SS316 **) in C-4 available, Sealmatic recommendation.
CSContacting containment seal
Containment Seals Type A
A containment seal is a safety seal. In case of primary seal failure it shall operate for a minimum of 8 hours at seal chamber conditions. It can be found in the default configuration ''2CW-CS'' and the optional configuration ''2NC-CS''
Containment seals can be of non-contacting or contacting kind. Non-contacting containment seals feature aerodynamic grooves which provide a reliable lift-off of the seal faces even at low velocities.
Contacting containment seals are used in connection with liquid buffer systems but may also be used as dry running seal in connection with a Nitrogen purge.
Operating limitsp 1(max) = 25 bar g (363 PSI)t1 = -20 … 176 °C (-4 … 350 °F)v g(max) = 23 m/s (75 ft/s)
Materials*)Face: Carbon (A), SiC (Q1 , Q2)Seat: SiC (Q1 , Q2)O-rings: FKM, FFKM, EPDM, NBR, HNBR …Springs: Alloy C-276**)Other parts: SS316 (1 .4571)
Operating limitsp 1(max) = 25 bar g (363 PSI)t1 = -20 … 176 °C (-4 … 350 °F)v g(max) = 23 m/s (75 ft/s)
Materials*)Face: Carbon (A), SiC (Q1 , Q2)Seat: SiC (Q1 , Q2)O-rings: FKM, FFKM, EPDM, NBR, HNBR …Springs: Alloy C-276**)Other parts: SS316 (1 .4571)
Operating limitsp 1(max) = 41 bar g (600 PSI)t1 = -20 … 176 °C (-4 … 350 °F)v g(max) = 23 m/s (75 ft/s)
Materials*)Face: Carbon (A), SiC (Q1 , Q2)Seat: SiC (Q1 , Q2)O-rings: FKM, FFKM, EPDM, NBR, HNBR …Springs: Alloy C-276**)Other parts: SS316 (1 .4571)
Operating limits refer to default seal face combination Carbon/SIC.*) Default and optional materials available. **) in C-4 available, Sealmatic recommendation.
3NC-BB
3NC-BB
3NC-FB
Gas SealsType A
10
Plan 23Used for hot liquidapplications or where
the temperatureand pressure in the
seal chamber isclose to the vapour
curve of the product.Recirculation by
means of a pumpingring in seal chamberthrough a cooler and
back to seal chamber.
Plan 31Used in applications
with suspended solids where the SG
of the particles is 2x that of the liquid.
Recirculation from pump discharge
through a cyclone separator, clean fluid
to seal chamber, dirty fluid to suction.
Plan 22 (21 )Used for hot applications or where
the temperature and pressure in the
seal chamber is close to the vapour
curve of the product. Recirculation from
pump discharge through a flow control orifice and cooler into
the seal chamber.
Plan 21: Without strainer St
St
Plan 01For general
applications. Product pumped is clean, good lubrication
properties and heat removal from the mechanical seal.
Internal circulation from the pump
discharge to the seal.
Plan 02Seal chamber
cooling and neck bush are necessary,
unless otherwise specified. Dead
end seal chamber with no circulation.
Plugged connections for possible future
circulation and quench.
Plan 13
Used where the seal chamber pressure is
at discharge pressure (mainly vertical
pumps). Recirculation from seal chamber
through a flow control orifice and back to
pump suction
Plan 11 (12)
Used when the product being
pumped has occasional particles
only. Recirculation from pump discharge
through a strainer and flow control orifice to
the seal.
Plan 12: With strainer St
St
Plan 14Used where cooling
flow is supplied to seal while providing
venting of seal chamber (generally
used for vertical pumps). Recirculation from pump discharge
through a flow control orifice to the seal and
simultaneously from the seal chamber through a control
orifice to pump suction.
Plan 32 Used when the product being
pumped does not have good lubrication
properties, contains suspended solids or is hazardous. Flush
injecton of clean fluid into the seal chamber
from an external source.
Plan 41 Used in applications
with suspended solids where the SG
of the particles is 2 x that of the liquid.
Temperature and pressure in the seal chamber is close to the vapour pressure
of the product.Recirculation from
pump discharge through a cyclone
separator, delivering clean fluid to a cooler
and then to the seal chamber.
cyclone separator
API PlansProcess Side
11
Plan 75Application
when pump fluid condenses at ambient
temperatures. Containment seal chamber drain for
condensing leakage.
A C
B
Plan 76Application where
pump fluid does not condense at
ambient temperature. Containment seal
chamber vent for non-condensing leakage.
Device to be located below pump shaftTo drainTo flare
C
A
C
B
Plan 74Used in applications where the product is
harmful/hazardous. Externally supplied barrier gas used to
positively prevent process fluid
from leaking to atmosphere.
Pressure of barrier gas higher than seal
chamber pressure.
N 2A
A
connect to plan 75connect to plan 76N 2
quench connection to be located downwards
A
B
C
D
Plan 72 (71)Applicable with
hydrocarbons normally used in conjunction with
plan 75 or plan 76. Externally supplied
gas buffer (pressure lower than seal
chamber pressure). Buffer gas may be used to dilute seal
leakage.
A B
C
Plan 71: Plugged connections
Plan 51Used with products that usually solidify when coming into contact with air /
ambient temperature. External reservoir providing a dead-ended blanket for
fluid to the quench connection of the
gland.
Plan 52Used where the pumped product is
harmful / hazardous and / or buffer fluid
may not contaminate the product. External reservoir at pressure below seal chamber
pressure. Pumping device providing
buffer liquid forced circulation.
Plan 53BUsed for applications where products have
high pressure and are harmful/hazardous.
Pre-pressurized bladder accumulator provides pressure to
circulation system. Heat removed by air/
water heat exchanger. Pumping device providing forced
circulation.
Plan 53AUsed for hot
applications or where products
have low pressure and are harmful/
hazardous. External reservoir pressurized above seal chamber
pressure providing barrier fluid to
mechanical seals. Pumpng device
providing forced circulation.
A
Plan 53CUsed for applications where products have
high pressure and are harmful/hazardous.
Pressurization by reference line from seal chamber to a
piston accumulator provides pressurized
barrier fluid. Pumping device providing
forced circulation.
N 2A
Plan 54Used in harmful/
hazardous applications.
Pressurized clean barrier fluid from
an external system. Fluid circulation by
an external pump or pressure system.
thermosiphon system
API PlansBetween seals
12
API PlansAtmospheric side
Used for leakage detection
on single seal. Atmospheric side
leakage collection and monitoring (alarm high) in external vessel.
Plan 65A
B
Plan 62 (61 )Used to keep
atmospheric side of seal clean. External source providing a
flow-through quench at atmospheric side.
D
Plan 61: Plugged Quench connection
Selection of Buffer and Barrier Mediums
Sealed fluid Barrier/buffer fluid Special notes General demands
Above 10 °C
Hydrocarbon fluid
100 mm2/s at 38 °C and1 mm2/s to 10 mm2/s at 100 °C
Three years continuous operation without adverse deterioration.Non-critical normal buffer/barrier fluid leakage.Compatibility with the sealed medium.Compatibility with the materials of the sealing systeminitial boiling point min. 28 °C above exposed temperature.Flash point > service temperature (if O2 is present).Compatibility with max./ min. process temperature.Freezing temperature < ambient temperature at site.Viscosity < 500 mm 2/s at minimum temperature.Viscosity over the entire operating-temperature range.Consider gas solubility in viscous barrier fluids (> 10 bar).
Below 10 °C5 mm2/s to 40 mm 2/s at 38 °C and1 mm2/s to 10 mm2/s at 100 °C
Aqueous streams
Mixture of water and ethylene glycol
Ethylene glycol may be considered as hazardous material and/or waste
Don‘t use commercially available automotive antifreeze (plating of additives at seal parts)
Mixture of water and propylene glycol
Hydrocarbon streamsParafin-based high purity oils
With little or no additive for wear/oxidation resistance (plating of additives at seal parts)
Synthetic-based oils –
ISO 21049API 682
Seal categoryStep I
Seal arrangementStep II
Seal typeStep III
API plansStep IV
Letters and numbers C1, C2, C3 A1, A2, A3 A, B, C01 , 02, 1 1 , 12, 13, 14, 21 , 22, 23, 31 , 32, 41 , 51 , 52, 53A, 53B, 53C, 54, 61 , 62, 65, 71 , 72, 74, 75, 76
Note
Arrangement 1 can be a 1CW-FX or 1CW-FLArrangement 2 can be a 2CW-CW, 2CW-CS or 2NC-CS Arrangement 3 can be a 3CW-FB, 3CW-FF, 3CW-BB, 3NC-FB, 3NC-FF or 3NC-BB
Seal materials are not part of this code (default materials assumed)
A code for engineered mechanical seals (ES) is not specified
ExampleFeatures: category 2, arrangement 2, type A, flush plan 1 1 and flush plan 52
Code: C2A2A1152
13
Objectives and Category Details
*) All technical specifications are based on extensive tests and our many years of experience. The diversity of possible applications means, however, that they can serve only as guide values. We must be notified of the exact conditions of application before we can provide any guarantee for a specific case. Subject to change.**) API / ISO paragraphs in brackets***) Please also ask for Sealmatic CTX API mechanical seals
API 682 and ISO 21049**) Category 1∗∗∗) Category 2 Category 3
Objective 1*): seal operation Continuously for 25,000 h without need for replacement
Objective 2*): containment seal operationAt least 25.000 h without need for replacement at any containment seal chamber pressure equal to or less than the seal leakage pressure switch setting (< 0,7 bar g (10 PSI)) and for at least 8 h at the seal chamber conditions.
Objective 3*): emissionsComplying with local emissions regulations or exhibiting a maximum screening value of 1 ,000 ml/m3 (1 ,000 ppm vol.) as measured by the EPA Method 21 , whichever is more stringent.
Basic design features (4.1 .3 / 6.1 ) Balanced mechanical seal, inside-mounted, cartridge design, type SS316 (1 .4571) or better for sleeve and housing
Throttle bushing requirement for arrangement 2 and 3 seals (7.2.3 / 7.3.3.1 )
Fixed carbon, if specified
Flush connection to the process sidefor arrangement 3 seals (7.3.3.2)
If specified
Shaft diameter (1 ) 20 mm (0.75 inch) to 110 mm (4.3 inch)
Seal chamber size (4.1 .2)ISO 3069 type C, ASME B73.1 and ASME B73.2
ISO 13709 / API 610 10th edition
Cartridge seal sleeve size increments required
None 10 mm increments (6.2.2.3.1 )
Temperature range (4.1 .2) -40 to 260 °C (-40 to 500 °F) -40 to 400 °C (-40 to 750 °F)
Pressure range, absolute (4.1 .2) 22 bar a (315 PSI) 42 bar a (615 PSI)
Face materials (6.1 .6.2)Premium blister-resistant carbon (A) vs. self-sintered silicon carbide (Q1)
Premium blister-resistant carbon (A)vs. reaction-bonded silicon carbide (Q2)
Gland plate metal-to-metal contact requirement
Required (6.2.1 .2.2) Required inside and outside the stud circle diameter (6.2.2.2.2)
Tangential buffer/barrier fluid outlet for arr. 2 and 3 seals (7.2.4.2 / 7.3.4.3)
If specified Required
Throttle bushing design requirement for arrangement 1 seals (7.1 .2.1 )
Fixed carbon Fixed, non-sparking metalFloating carbon
Floating carbon option (7.1 .2.2)
Scope of vendor qualification testTest as category 1 Test as category 2 Test as category 3, entire seal
assembly as a unit (10.3.1 .2.2)Unless faces interchangeable with category 3 (10.3.1 .2.3)
Distributed inlet flush requirements arr. 1 and 2 with rotating flexible element
When required or if specified (6.1 .2.14 / 6.2.1 .2.1 ) Required (6.2.3.2)
Seal circulation device head flow curve provided (8.6.2.2)
If specified Required
Proposal data requirements (11 .2.1 )Minimal Rigorous
Contract data requirements (11 .3.1 )
14
Year
2004
2003
2002
1996
1995
1990
Pump specification
API 610, 10th edition
-
ISO 13709
API 610, 9th edition
API 610, 8th edition
-
API 610, 7th edition
Note
Same wording and structure as in the ISO documents
Enhancements to API 682, 2nd edition
Enhancements to API 610, 9th edition
Seal chambers in API 610, new seal coding system in API 682
References API 682 1st edition
First stand alone API seal standardRevised seal coding system
Contains basic seal specificationDefines seal coding system
Mechanical seal specification
API 682, 3rd edition
ISO 21049
-
-
API 682, 1st edition
-
API 682, 2nd edition
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The specifications, drawings, images etc included in this catalogue are intended to be generic and must be interpreted as equivalent or functionally equivalent. The identification of many items is facilitated by illustrations (photographs and general assembly drawings) and mention of, or reference to any specific standards, or trade names, including those that might appear on the photographs, drawings, images etc is intended for illustration purposes only, and does not imply an endorsement or imitation or preference of any specific standard, brand, manufacturer or supplier. Neither does the information imply the availability of any mentioned items. The items discussed alongwith the images, drawings etc portrayed are representative of industry catalogues, standards, terminology and specifications hence, accounting for any resemblance which otherwise may be co-incidental.
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