Gela-Malta (Cost Estimate) Rev 2 3

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Transcript of Gela-Malta (Cost Estimate) Rev 2 3

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www.eni.it

Gela - Malta Project

April 2009

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Basis and Criteria of the Study

Results

Budgetary Estimate Summary

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SUMMARY OF THE STUDY

The study represents an updating of a previous evaluationperformed in 2002 and is based on the following requirements:

Malta shore approach at Delimara,

Export pressure = 54 barg

Minimum delivery pressure = 39 barg,

Flowrate scenario:

Max Peak = 106570 Sm3 /h

The hydraulic study performed according to the same approachadopted in 2002 leads to the definition of the following pipelinediameter

OD = 18”  

The expected accuracy of the estimate is ± 20%

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Basic Data

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Gas Composition and Characteristics

Equation of State = PR Peneloux

Gas Composition 

Component  Mol% 

Methane 86.7854

Ethane 6.2315

Propane 1.4872

i-Butane 0.2707

n-Butane 0.4140

i-Pentane 0.1305

n-Pentane 0.1080

Exane 0.0375

Eptane 0.0053

Nitrogen 4.1520

Carbon Dioxide 0.3711

Water 0.0068

Total  100.0000 

Gas Characteristic

@ STD Conditions: 1.013bar, 15°C

Value

Gas Molecular Weight (kg/kmol) 18.39

Gas Density (kg/m3)  0.779

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Malta Required Flowrate

0

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   1   0   3   x

   S   C   M   /   h

Hour 

Mid-season week day Mid-season Weekend day Summer Week day

Summer Weekend day Winter Week day Winter Weekend day

Peak day

 

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Pipeline Data

Pipeline characteristics 

Pipe Material Steel Grade API 5L-X65

SMYS 450 MPa

SMTS 535 MPa

Steel Density 7850 kg/m3 

Young Modulus 207000 MPa

Poisson Ratio 0.3

Coefficient Of thermal Expansion 1.16 x 10-5 °C-1 

Sea Water Density 1026 kg/m3 

Concrete Density 3040 kg/m3 

Corrosion Coating Density 1300 kg/m3 

Corrosion Coating Thickness 2.5 mm

Corrosion Allowance 0 mm

Out of roundness1.5% OD

but maximum 15 mm

Thickness tolerance±0.75 mm for t ≤ 15 mm

±1.00 mm for t > 15 mm

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Soil Data

KP KPSOIL GELA-MALTA 

Dr  Su  D50 

From To kN/m3  Deg.  %  kN/m

2  mm 

0 4.4

Fine SAND with occasion Shell becoming medium

toward coast 9 44 85-100 --

0.09-0.16 0.7

(max.)

4.4 7.9Silty Fine SAND with Occasional Shell. PossiblePresence of clayey SAND.

9 32 35-65 -- 0.07-0.1

7.9 10.2 Very Soft Silty CLAY with Occasional Shell 7.5 -- -- 2 0.009-0.013

10.2 21.2 Very Soft Silty CLAY 4.5-5.5 -- -- 2-4 <0.002

21.2 36Very Soft Silty/Sandy CLAY. Occasional presenceof Shell Fragments.

7 -- -- 8-10 0.01-0.03

36 51Very Soft Silty CLAY. Occasionally some intrusionsof sandy CLAY,

5.5* -- -- 6* 0.003

51 95Very Soft Sandy CLAY, containing some shellfragments

8.0* -- -- 8-15* 0.01-0.04

95 115Very Soft Silty/Sandy CLAY at top, changing infine SAND in depth.

4.0*

1-2*

<0.002

8.5* 40* 50-65* <0.074

115 136Fine to Medium SAND with Occasional Shells.Possible intercalation of Clay and Silt.

8.5*36-44*

60-100*

-- 0.06-0.2*

136 145Fine SAND with high content of Shells,concretions and corals.

9.0*40-44*

80-100*

--0.09-0.16 0.7

(max.)*

145 148Fine to Medium SAND with high content ofshells/corals fragment.

8.5*36-44*

60-100*

-- 0.06-0.2*

148 LTE Gravely SAND. High Probability of Rock Outcrops. 7.0-8.5*30-36*

35-65* -- 0.1-0.9*

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Hydraulic Analysis - Inlet and Delivery Gas Conditions

Gas Condition  Value

Inlet Gas Pressure (barg) 54

Inlet Gas Temperature (°C)  18

Delivery Gas Pressure (barg) ≥39 

Delivery Gas Temperature (°C) As per result of the hydraulic simulations,

in peak day conditions 

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Hydraulic Analysis – Data Input

Pipe and Soil data:

Steel grade: X65

Pipe internal roughness: 25 micronsCorrosion Coating Thickness: 2.5 mm.

Pipeline MaterialThermal Conductivity

W/m K

Steel 50

Corrosion Coating (PE) 0.3

Overweight Concrete 2.33

Soil Thermal Conductivity

W/m K

Wet Sand  2 

Dry Sand at Gela 1

Dry Sand at Malta  1.5 

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Hydraulic Analysis – Data Input

Pipeline Burial Configuration:

The pipeline is assumed buried in the onshore sections and in the coastalareas (i.e. for WD<30m at Gela side and for WD<35-40m at Malta side).The pipeline is considered unburied in the deep water.

Pipeline Burial Depth(from the pipeline top)

m

Onshore Sections 1.5

Offshore Sections 1

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Results

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Scenario 16” OD Pipeline Gela – Malta (Delimara):Process Analyses Results

Scenario A - 16" ND Pipeline

- Pressure Trends-

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0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23

Time [h]

   P  r  e  s  s  u  r  e   [   b  a  r  g   ]

Pressure Supply at Gela Terminal (P/L Inlet)

Pressure Delivery at Delimara Terminal (P/L Outlet)

Minimum Delivery

Scenario A - 16" ND Pipeline

- Flow Rates Trends-

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0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23Time [h]

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Gas Supply at Gela Terminal (P/L Inlet)

Gas Delivery at Delimara Terminal (P/L Outlet)

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Scenario 18” OD Pipeline Gela – Malta (Delimara):Process Analyses Results

Scenario A - 18" ND Pipeline

- Flow Rates Trends-

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120,000

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23Time [h]

   F   l  o  w   R  a   t  e   [   S  c  m   /   h   ]

Gas Supply at Gela Terminal (P/L Inlet)

Gas Delivery at Delimara Terminal (P/L Outlet)

Scenario A - 18" ND Pipeline

- Pressure Trends-

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Pressure Supply at Gela Terminal (P/L Inlet)

Pressure Delivery at Delimara Terminal (P/L Outlet)

Minimum Delivery

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Scenario 18” OD Pipeline Gela – Malta (Delimara):Wall Thickness Analyses Results

Gela - Malta (Delimara) - OD=18" - Pd=75 bar 

WT=10.3

WT=15.9

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KP (m)

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   W  a   l   l   T   h   i  c   k  n  e  s  s   (  m  m   )

WD (m) Min WT (mm) Selected WT (mm)

Min Buckle Arrestors Thickness (mm) Selected Buckle Arrestors Thickness (mm) Min Prop Buckl

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Scenario 18” OD Pipeline Gela – Malta (Delimara):On Bottom Stability and Layability Analyses Results

Gela - Malta (Delimara) - OD = 18" - Pd=75 bar 

CCT= 90.0

CCT= 60.0

CCT= 40.0

CCT= 60.0

CCT= 90.0

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KP (m)

   W  a   t  e  r   D  e  p   t   h   (  m   )

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   T   h   i  c   k  n  e  s  s   (  m  m   )

WD (m) Selected CCT (mm)

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Budgetary 

Estimates

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Budgetary Estimates - CAPEX 

CAPITAL COSTS 

Scenario 

OD = 18" 

Lenght (km)  154.0 

Steel Weight (Kton)  17.763 

Inch  18 

Management and Design  Meuro  15 

Materials Meuro  53 

Construction  Meuro  138 

TOTAL  Meuro  206 

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Budgetary Estimates - OPEX 

OPERATING COST 

Scenario 

OD = 18" 

Periodical cost for Pipelines and Shore approaches Surveys(Every two year operations) 

Meuro  2.2 

Periodical cost for Internal Line Inspection(Every seven years operations) 

Meuro  1.4 

TOTAL per year  Meuro/year  1.3 

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The budgetary cost estimate has been evaluated in Euro on the basis of in house data

bank. Particularly, the following cost for procurement of steel pipeline have been considered:

Budgetary Estimates Notes

2,000 Euro/ton

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Main exclusions from the budgetary estimate:

• Capital taxes, import duties and levies

• Owner costs, taxes, etc.

• Paid interests and/or financial charges

• Financial arrangements, bonds, guarantees, cash flow burning and similar

• Taxes, duties, fees, VAT, etc. of any nature

• Costs associated with the Builder All Risk (BAR), Third Party Liability (TPL) or other

related Project Insurances including Insurances during the operation period

• Land acquisition and Right of Way

•  All permits and licences including special Project environmental protection

arrangements

• Certification

•  Any extraordinary intervention on pipelines and plants.

• Weather Down-Time or Weather Stand-By

Budgetary Estimates Exclusions