Sener Fsru English

CONTENTS SENER OVERVIEW SENER FSRU DESIGN REASONS FSRU DEVELOPMENTS

© SENER, Ingeniería y Sistemas, S.A.





SENER OVERVIEW

GRUPO DE INGENIERÍA Aeronautical Industry

En ineerin & Construction

GAS TURBINES

SENER INGENIERÍA Y SISTEMAS O O

ITP (53,1%)

- Design, development and technology - Manufacturing of components and module integration - In service support

MARKETS

MUNICIPAL WASTE TO ENERGY O

- Civil & Architecture - Energy & Processes - Marine

- Bilbao - Buenos Aires - Madrid - A lgiers - Barcelona - Warsaw - Seville - Abu Dhabi - a enc a - ayama - Lisbon - San Francisco - México DF - São Paulo

- Large civil aircraft - Defence - Industrial turbines - Small civil aircraft - Helicopters

AFFILIATES & PARTICIPATIONS - TURBORREACTORES (100%) - AEROMARITIME GROUP (100%) - ITA (100%) - PRECICAST BILBAO (60%) KEY: O – Operating

BUSINESS UNITS

Energy & Environment

ZABALGARBI (30%)

O

FARM WASTE TREATMENT

TRACJUSA (42%)

O

VALPUREN COMATUR (95%)

O

VALPUREN BAÑUELO (93%)

O

C.S.P.

TORRESOL ENERGY (60%)

AFFILIATES & PARTICIPATIONS - III (100%) - ENGIVIA (100%) - NTE-SENER (100%) - HISDESAT (5%)

C – Construction


ARCOSOL (Vall e 1) (100%)

C

TERMESOL (Valle 2) (100%)

C

SENER OVERVIEW

SENER FACTS AND FIGURES OWNERSHIP Year 2011 Turnover Employees

S.G.I.

S.I.S.

1,160 M€

653 M€

5, 165

2,243

100% Private

Innovation

NON SPANISH SALES

Quality

57 %

Independence


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SENER FSRU DESIGN REASONS

Consi ering t e situation o Nuc ear Power Natura Gas is not t e source o energy of transition" 

Natural Gas is the Source of Energy for the next 30 years



Actually there is a need for additional world wide regasification capacity .



In these circumstances, there are cases where FRSU is an alternative

required by the onshore regasification plants


SENER FSRU DESIGN REASONS Offshore regasification is changing the philosophy of the LNG production chain Upstream

Midstream

Downstream

Traditional Gas Field

Liquefaction Facility

LNG Storage Tank

LNG Tanker

LNG Storage Tank

Vaporizers

To Pipeline System

Storage -Regasification Offshore

Today Gas Field

Future

Liquefaction Facility

LNG Storage Tank

To Pipeline System

Li q u ef a c t i o n , St o r a g e a n d Re ga si f i c a t i o n Of f sh o r e To Pipeline System


SENER FSRU DESIGN REASONS The sum of SENER's capabilities on

Naval Design

LNG Regasification Terminal

SENER FSRU DESIGN


Combined Cycle


Project

Power MW

CCC NORTE (México)

450

CCC PILAR (Argentina)

500

rgen na

CCC San Martín (Argentina)

800

CCC SAN LORENZO (México)

116

CCC TERMOZULIA II (Venezuela) CCC EL VENT (Spain) CCC BIZKAIA ENERGÍA (Spain) CCC ARCOS III (Spain) CCC ESCOMBRERAS (IV) (Spain) CCC ACECA (Spain) CCC VALLADOLID (México) CCC TERMOZULIA III (Venezuela) CCC AGUA PRIETA II (México)

490 400 800 800 800 400 600 500 400


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LNG Regasification Plant. Sagunto (Spain) LNG Regasification Plant. Barcelona (Spain) LNG Regasification Plant. Huelva (Spain) LNG Regasification Plant. Bilbao (Spain) . LNG Dunkerque Regasification Plant (France)


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® System :

Global leader in ship building with 3D CAD/CAE/CAM. Currentl used in 150 shi ards and design offices located in 30 countries © SENER, Ingeniería y Sistemas, S.A.

Project Sea Cloud II Hussar 4000 DWT BARGE Ro-Pax M/S Viking ADCC - Sierra Laurel Chemical vessels for Huelva Rescue Tu s for UNV SWATH Aliswath 3000 DWT BARGE City Cat 40 TAIPAN Texaco captain FPSO (*) Petro jarl IV FPSO Alba FPSO GM 4000 Semisub Drilling Rig * floatin roduction stora e and offloadin


Length (m) 135,70 , 75,13 138,79 , 117,27 140,00 35 46 64,00 63,99 39,70 140,40 214,70 220,00 , 237,20 N.A.

F R A N ®

S f t w a r e t o l d e v e l p e d b y e n e r

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SENER FSRU DEVELOPMENTS

The niche market of this FSRU is in broad outline:

•

s ore erm na s pro ec " ow capac y o sen ou <

"

•Permanent LNG facilities. FSRU new construction specific for each client. • •Far away of facilities which only renting the send out capacity temporarily

Our design ranges covers the following performances Sendout (bcma)

Storage capacity (m3)

Sendout pressure (bar)

Berthing

0,2 – 5,0

20.000 - 200.000

25 - 100

Turret Island Jetty


SENER FSRU DEVELOPMENTS SENER has developed some specific project shown in the following slides

OFF SHORE FSRU TURRET MOORED


ON SHORE JETTY




- FLOATING STORAGE AND REGASIFICATION PLANT FOCUSED TO A 160 MW GT CONSUMER - STORAGE CAPACITY 60.000 M3 - AVERAGE REGASIFICATION SEND-OUT 0,5 BCMA AT 50 BAR AT THE DESIGN SEND-OUT - LNG CARRIERS ROTATION EVERY 15 DAYS - DOUBLE-HULLED STEEL VESSEL WITH FOUR LNG TANK S USING MEMBRANE CONTAINMENT SYSTEM - BOIL-OFF RATE 0,15% VOL. / DAY - GAS SENT TO SHORE VIA EXPORT RISERS THROUGH TURRET - OPERATION WHILE PERMANENTLY MOORED AT A FIELD LOCATION - LARGE PROCESS FACILITIES AREA, LIVING QUARTERS AND HELIDECK - LNG TRANSFER IN SIDE-BY-SIDE CONFIGURATION USING CONVENTIONAL LOADING ARMS




SENER FSRU DEVELOPMENTS - LENGTH Between Perpendiculars.: 161,00 m

- BREADTH: 34,80 m


- DEPTH: 20,60 m

- SCANTLING DRAUGH 9,00 m

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SENER FSRU DEVELOPMENTS -

FSRU is permanently moored to a dual berth jetty jetty A subsea pipeline conducts the NG to an onshore ORF


SENER FSRU DEVELOPMENTS FSRU Double hull non self propelled vessel Insulation of tanks is provided by means of a membrane technology Center line longitudinal bulkhead creates two rows of tanks in order to avoid “sloshing” Accommodation is provided for 45 people, including Re-gasification Plant operators and Ship crew

Main Particulars are as follows: Length over all (LOA) Length between Perpendiculars (LBP) Breadth (Moulded) Depth to Trunk Deck Deadweight at design draught LNG Storage Capacity


245.70 m 245.70 m 47.00 m 32.44 m 74.800 T 163,000 m 3

SENER FSRU DEVELOPMENTS Re-gasification Process

Main re-gasification facilities are

• LNG loading/unloading systems located in the Jetty • LNG handling system • Re-gasification section • BOG (Boil-off gas) handling systems • NG handling systems which send the NG to the subsea pipeline

Main Particulars are as follows: Operating pressure range: Operating temperature range: Design gas send-out pressure: Maximum gas send-out flow: Gas send-out temperature (min.):

40 bar g (start up) / 80 bar g (max) 0 °C – 38 °C 95 bar g 2,5 MTPA = 365300 Ncm/h = (3,2 bcma) 6 °C


SENER FSRU DEVELOPMENTS Jetty

Double berth pilled jetty Able to receive a LNG carriers ranging from 240 to 315 m LOA (up to 217,000 m 3 capacity and 12 m of draft) and the FSRU vessel Supported by 1.800 mm diameter piles Total Surface 3.400 m 2


SENER FSRU DEVELOPMENTS Subsea Gas Pipeline

Connects the Jetty with the ORF (Onshore receiving facilities) Nominal diameter of 20” Two fiber-optic cables are installed with the same routing as the gas pipeline

Onshore Receiving Facilities (ORF)

Gas is treated at the Pipeline Filters and measured at the Metering , Block valves are incorporated to allow isolation

.

Operating pressure range is 40 bar g (start up) / 80 bar g (max) and ° – ° .


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FSRU is permanently moored to a dual berth jetty jetty An access platform conducts the NG to an onshore ORF The LNG carriers will be moored to the other side of the jetty © SENER, Ingeniería y Sistemas, S.A.

SENER FSRU DEVELOPMENTS FSRU

Double hull non self propelled vessel Insulation of tanks is provided by means of a membrane technology Does not include a center line longitudinal bulkhead There is no sloshing problems thanks to this location in sheltered waters, so the FSRU structure can be lightened .

Main Particulars are as follows:

Length between Perpendiculars (LBP) Breadth (Moulded) Depth to Trunk Deck

245.70 m 47.00 m 32.44 m 182,000 m 3

LNG Storage Capacity


3


Re-gasification Process

Main re-gasification facilities are

• LNG loading/unloading systems located in the Jetty • LNG handling system • Re-gasification section • BOG (Boil-off gas) handling systems • NG handling systems which send the NG to the pipeline

Main Particulars are as follows: Operating pressure range: Operating temperature range: Design gas send-out pressure: Maximum gas send-out flow: Gas send-out temperature (min.):

40 bar g (start up) / 80 bar g (max) 0 °C – 38 °C 95 bar g 2,5 MTPA = 365300 Ncm/h = (3,2 bcma) 6 °C



Jetty

Double berth pilled jetty Able to receive a LNG carriers ranging from 240 to 315 m LOA (up to 217,000 m 3 capacity and 12 m of draft) and the FSRU vessel Supported by 1.200 mm diameter piles Total Surface 9.400 m 2



Access Platform

Includes the pipe rack 12m width earth embankment which starts at the shore and finishes at the end of the jetty (mooring dolphins)

Onshore Receiving Facilities (ORF)

Gas is treated at the Pipeline Filters and measured at the Metering , Block valves are incorporated to allow isolation

.

Operating pressure range is 40 bar g (start up) / 80 bar g (max) and ° – ° .


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