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



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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



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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


DATAFOR LNG


95% (Tons.)36,1 46,9 51,8 67,5 87,2


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


DATAFOR LNG


95% (Tons.)85,2 104,9 124,5 134,2 139,0


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


95% (Tons.)13,7 17,9 22,2 26,2 35,0


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


95% (Tons.)36,1 46,9 51,8 67,5 87,2 98,8 107,1


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


DATAFOR LNG


95% (Tons.)13,7 17,9 22,2 26,2 35,0


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


DATAFOR LNG


95% (Tons.)85,2 104,9 124,5 134,2 139,0


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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Cryogenic Tanks Catalogue

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