Download - Cryogenic Tanks Catalogue
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LNG storage tanks
and other uids atcryogenic temperatures
CRYOGENICTANKS
SA
ME
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CRYOGENICTANKS
LNG storage tanks
and other uids atcryogenic temperatures
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CRYOGENIC TANKS
Storage of Liqueed Natural Gas(LNG) at cryogenic temperature(other cryogenic uids: consult)
Design and construction: European Directive on Pressurised
Equipment 97/23/EC (EC mark) ASME VIII div. 1 (ASME mark)
High level of isolation (empty factoryless than 0.06 mbar)
External weathering protection: an-ticorrosive primer and reective
white top coat.
Dimensions and capacities accordingto LAPESA drawing (consult)
Service capacity of gas consumption(STD), up to 8.000 m3/h
Storage capacities from 5 up to 320 m3
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storage withprotection against
overpressure in thechamber
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GENERAL CHARACTERISTICS Presin de trabajo 5 bar LNG design temperature: -196C European Directive 97/23/CE CE Mark ASME VIII div. 1 ASME Mark Inner Tank: austenistic stainless steel Outer Tank: carbon steel Intermediate chamber and vacuum insulated
CHARACTERISTICS OF THE STORAGETANK (INNER TANK)
Made of austenistic stainless steel Maximum working pressure: 5 bar, 9 bar
(other on request)
CHARACTERISTICS OF CASING(OUTER TANK AND VACUUM CHAMBER)
Made of carbon steel (the zones throughwhich pipes pass are in austenitic stainlesssteel).
Protected against pressure in intermediatechamber.
With vacuum measuring connection. Maximum allowable vacuum in chamber: ab-
solute.
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LNG storage tanks
and other uids atcryogenic temperatures
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TESTS AND CONTROLS PERFORMED
100% Weld radiographs Inner tank pressure test Helium leak detector Vacuum in innerchamber from factory
EQUIPMENT Suitable valves for cryogenic service(stainless
steel/bronze) Pressure raiser for P.P.R. Pressure indicator and level indicator by pres-
sure differential (electronic). Optional:pressuretransmitter.
Dual safety valve assembly withkey distribu-tion manifold. Each set has two safety valves.
Vacuum connector for vacuum check. (withpressure stopcock and shock protector)
CERTIFICATES CE mark o ASME mark CE or ASME conformity statement of unit Hydraulic test certifacate. Installation and operating instructions. Vacuum chamber certicate. Safety valves certicate.
FINISH Inner: Particle clean nish stainless steel. Outer: Sand blasted to SA 2-1/2. Primer
60 and 60 white polyurethane.
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Capacity: from 5 to 320 m3
Contents: LNG, AR, He, CO2
Design pressure: from 5 to 44 bar.
Design temperature: as content.
LNG Equipment- Gas phase extra connection to be used
as desired.
- Pressure transmitter (4-20 mA, intrinsi-cally safe ATEX zone 1).
- Pressure gauge and electronic level(24 V) SAMSON brand. Level readingspot (analog-digital in m3 and %) andpressure(ANALOGUE READING/MEASU-REMENT) in gas phase. With level trans-mitter (4-20 mA, intrinsically safe ATEXzone 1). With pressure transmitter con-nection. Includes manifold with bypass
and holders.- Tank pressurizer (different capacities
available)- Union of two lling connections in one
ange DN50 PN10.- Valves Stainless Steel.- Vacuum resistance of the inner contai-
ner.- Sensor type Teledyne (Dv-6) to check
vacuum chamber.
- Vent pipe from safety valve with ameprotection.
- Other requirements: consult.
VERTICAL CRYOGENIC TANKS
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SYSTEM AGAINST
OVERPRESSURE IN
CHAMBER
LIFTING LUGS
(WITH EMPTY
TANK/VESSEL) THICKNESS 20 mm
VACUUM
CHAMBERLEGS ANCHORAGE DETAILS (APPROXIMATE DATA)
VACUUM
CONNECTION VACUUM INDICATOR PIPING AND EQUIPMENT AREA
TANKS2200 V SERIES
MODELS LC5V-22 LC6V-22 LC11V-22 LC16V-22 LC2 0V-22
Volume (m3) 4,9 6,2 10,9 15,7 19,9
L (mm) 3.830 4.350 6.350 8.350 10.130
Tare approx. (Tons.) for 5 bar 3,3 3,7 5,0 6,3 7,6
DATAFOR LNG
Stored liquid weight at
95% (Tons.)2.168 2.707 4.790 6.872 8.726
Pressure elevator PPR for NG
consumption (Nm3/h)370 370 370 370 370
TANKS3800 V SERIES
MODELS LC80V LC107V LC120V LC150V LC200V
Volume (m3) 82,6 107,4 118,6 154,6 199,6
L (mm) 11.300 14.050 15.300 19.300 24.300
Tare approx. (Tons.) for 5 bar 24,1 28,9 31,0 38,0 46,7
DATAFOR LNG
Stored liquid weight at
95% (Tons.)36,1 46,9 51,8 67,5 87,2
Pressure elevator PPR for NG
consumption (Nm3/h)1.000 1.000 1.000 1.000 1.000
TANKS4200 V SERIES
MODELS LC195V LC240V LC285V LC307V LC318V
Volume (m3) 195 240 285 307 318
L (mm) 19.660 23.660 27.660 29.660 30.661
Tare approx. (Tons.) for 5 bar 47,0 55,7 64,3 68,7 71,1
DATAFOR LNG
Stored liquid weight at
95% (Tons.)85,2 104,9 124,5 134,2 139,0
Pressure elevator PPR for NG
consumption (Nm3/h)1.000 1.000 1.000 1.000 1.000
TANKS3000 V SERIES
MODELS LC30V-30 LC40V-30 LC50V-30 LC60V-30 LC8 0V-30
Volume (m3) 30,8 40,5 50,2 59,9 79,5
L (mm) 8.300 10.300 12.300 14.300 18.300
Tare approx. (Tons.) for 5 bar 11,6 14,0 16.3 18.7 23.7
DATAFOR LNG
Stored liquid weight at
95% (Tons.)13,7 17,9 22,2 26,2 35,0
Pressure elevator PPR for NG
consumption (Nm3/h)1.000 1.000 1.000 1.000 1.000
Anticipate electrical supply for electronic level.NOTES:
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HORIZONTAL CRYOGENIC TANKS
Capacity: from 5 to 320 m3
Contents: LNG, AR, He, CO2
Design pressure: from 5 to 44 bar.
Design temperature: as content.
LNG Equipment- Gas phase extra connection to be used as desired.- Pressure transmitter (4-20 mA, intrinsically safe ATEX zone 1).- Pressure gauge and electronic level (24 V) SAMSON brand. Level reading spot (analog-digital in m3 and %)
and pressure(ANALOGUE READING/MEASUREMENT) in gas phase. With level transmitter (4-20 mA, intrin-sically safe ATEX zone 1). With pressure transmitter connection. Includes manifold with bypass and holders.
- Tank pressurizer (different capacities available)- Union of two lling connections in one ange DN50 PN10.- Valves Stainless Steel.- Vacuum resistance of the inner container.- Sensor type Teledyne (Dv-6) to check vacuum chamber.- Vent pipe from safety valve with ame protection.- Other requirements: consult.
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SYSTEM AGAINST OVERPRESSURE
IN CHAMBER
(amount according to model)PIPING AND EQUIPMENT AREA
TECHNICAL TYPE PLATE
FIXED SUPPORT
OVERFLOW
PRODUCT
LOAD
PRESSURE BOOSTER (PPR)
SAFETY
SYSTEM
LEVEL AND
PRESSURE
INDICATOR
PRODUCT
OUTPUT
M27 HOLE
LIFTING LUGS
(WITH EMPTY TANK/VESSEL)
VACUUM CONNECTION
SLIDING SUPPORT
elongated holes for M27
VACUUM INDICATOR
VACUUM CHAMBER
TANKS3000 H SERIES TANKS3800 H SERIES
TANKS4200 H SERIES
MODELS LC80 LC107 LC120 LC150 LC200 LC226 LC245
Volume (m3) 82,6 107,4 118,6 154,6 199,6 226 245
A (mm) 10.292 13.042 14.322 18.332 23.292 26.500 29.500
B (mm) 7.200 10.000 11.000 15.300 20.000 23.200 26.200
Tare approx. (Tons.) for 5 bar 24,4 29,6 32,1 39,8 48,7 54,6 60,2
DATAFOR LNG
Stored liquid weight at
95% (Tons.)36,1 46,9 51,8 67,5 87,2 98,8 107,1
Pressure elevator PPR for NG
consumption (Nm3/h)1.000 1.000 1.000 1.000 1.000 1.000 1.000
MODELS LC30-30 LC40-30 LC50-30 LC60-30 LC80-30
Volume (m3) 30,8 40,5 50,2 59,9 79,5
A (mm) 7.374 9.374 11.374 13.374 17.374
B (mm) 4.800 6.800 8.800 10.800 14.800
Tare approx. (Tons.) for 5 bar 11,3 13,6 15,9 18,3 23,3
DATAFOR LNG
Stored liquid weight at
95% (Tons.)13,7 17,9 22,2 26,2 35,0
Pressure elevator PPR for NG
consumption (Nm3/h)1.000 1.000 1.000 1.000 1.000
MODELS LC195 LC240 LC285 LC307 LC318
Volume (m3) 195 240 285 307 318
A (mm) 18.700 22.700 26.700 28.700 29.700B (mm) 15.500 19.500 23.500 25.500 26.500
Tare approx. (Tons.) for 5 bar 46,2 54,9 63,5 67,9 70,3
DATAFOR LNG
Stored liquid weight at
95% (Tons.)85,2 104,9 124,5 134,2 139,0
Pressure elevator PPR for NG
consumption (Nm3/h)2.000 2.000 2.000 2.000 2.000
Anticipate electrical supply for electronic level.NOTES:
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WORLDWIDE PROJECTS
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