Lng-ld-009h1 Sur09134 Sk Splendor 050809

DATA ENTRY FORM VESSEL NAME TERMINAL PORT DATE REPORT ISSUED INTERTEK FILE NUMBER

: : : : :

SK SPLENDOR OMAN LNG SUR, OMAN 5-Aug-2009 SUR/09/134

Program Version Number LNG-LD-009H1 (07-AUG-09)

CUSTOMER NAME ADDRESS #1 ADDRESS #2 ADDRESS #3 ADDRESS #4 ADDRESS #5 CONTACT NAME #1 CONTACT NAME #2 CONTACT NAME #3 CUSTOMER REFERENCE #1 CUSTOMER REFERENCE #2 SPA SUPPLIED BY

: : : : : : : : : : : :

OMAN LNG P.O. BOX 560 MUSCAT 116 SULTANATE OF OMAN

FOR INTERTEK USE ONLY

DO NOT ISSUE THIS PAGE TO CUSTOMERS

ACCOUNTS PAYABLE - NGF / 23 ATIQ AHMED OF039/09-SL100-KG OMAN LNG / KOGAS CORPORATION

IN ORDER FOR THIS PROGRAM TO WORK PROPERLY, MACROS MUST BE ENABLED

REPORT SETUP & GUIDELINES

Report of Quantity

1

SELECT TYPE OF REPORT OF QUANTITY SELECT TYPE OF REPORT OF QUANTITY ( STANDARD OR QUANTITY SPLIT).

1 2

0

Report of Gas Up

SELECT TO DISPLAY OR HIDE THE REPORT OF GAS-UP IF GAS-UP IS REQUIRED, SELECT WHICH CALCUALTION METHOD IS TO BE USED.

0 1 2

0

Report of Cool Down

Contract Used ( SPA )

0 1 2 3 4 5

14

1 2 3 4 5 Secondary 6 Custody 7 Transfer 8 Measurement 9 YES 10 NO 11 12 CTMS 13 "Snapshot" 14 15 Measurement 16 17 0 Page(s) 18 1 19 2 3 4

YES

0

SELECT TO DISPLAY OR HIDE THE REPORT OF COOL DOWN IF COOL DOWN IS REQUIRED, SELECT WHICH COOL DOWN CALCULATION METHOD IS TO BE USED.

SELECT WHICH CONTRACT (SPA) IS TO BE USED FOR CALCULATIONS ALL PAGES WILL AUTOMATICALLY CHANGE TO THE VALUES OF THE APPROPRIATE CALCULATION METHOD AS DESCRIBED IN THE RELEVANT CONTRACT (SPA)

SELECT TO DISPLAY OR HIDE THE SECONDARY CUSTODY TRANSFER MEASUREMENTS. SECONDARY CUSTODY TRANSFER PAGE RECORDS AND CALCULATES THE VOLUMES OF THE SECONDARY GAUGING SYSTEM FOR OPENING & CLOSING AND COMPARES THE VOLUMES TO THE PRIMARY SYSTEMS.

SELECT TO DISPLAY HOW MANY SNAPSHOT MEASUREMENT PAGES ARE NEEDED. CHOSE FROM ZERO TO FOUR ADDITIONAL CTMS "SNAPSHOT" MEASUREMENT PAGES.

0 1 2 3 4

1

Operational Checklist

SELECT TO WHICH OPERATIONAL CHECKLIST TO DISPLAY SELECT THE APPROPRIATE CHECKLIST TO BE DISPLAYED AND REPORTED.

1 2

0

Verification of

GC

Bunker Reports

0 1 2

NONE NONE BOTH FO ONLY DO ONLY

Letter(s) of Protest

Client Specific Reports

Report Revision Number

0 0 1 2 3 4

0

SELECT TO DISPLAY OR HIDE THE VERIFICATION OF GC PAGE IF NO VERIFICATION OF GC IS REQUIRED, OBTAIN A COPY OF THE TERMINAL'S VERIFICATION RECORDS BEFORE & AFTER. OBTAIN COPIES OF THE CERTIFICATIONS FOR THE SPAN GAS AND LAST CALIBRATION OF THE GC.

SELECT TO DISPLAY OR HIDE THE BUNKER REPORTS IF NO BUNKER REPORTS ARE REQUIRED, OBTAIN A COPY OF THE VESSEL'S BUNKER REPORT BEFORE & AFTER FROM THE CHIEF ENGINEER.

SELECT TO DISPLAY HOW MANY LETTER OF PROTEST ARE NEEDED. CHOSE FROM ZERO TO FOUR LETTERS OF PROTEST.

SELECT TO DISPLAY OR HIDE CLIENT SPECIFIC REPORTS SELECT IF ANY ADDITIONAL CLIENT SPECIFIC REPORT IS NEEDED OR NOT.

0 1 2 3 4 5

None

Provisional Final Revision 1 Revision 2 Revision 3 Page Numbers Revision 4 Required

NO

YES NO

SELECT TO IDENTIFY REVISED REPORT SELECT IF REPORT WAS REVISED AND WHICH REVISION NUMBER IS TO BE ISSUED

SELECT TO PLACE PAGE NUMBERS ON BOTTOM OF REPORT PAGES SELECT IF PAGE NUMBERS ARE NEEDED AT THE BOTTOM OF THE PAGES WITHIN THE REPORT

5-Aug-2009 OMAN LNG P.O. BOX 560 MUSCAT 116 SULTANATE OF OMAN ATTN : ATTN :

ACCOUNTS PAYABLE - NGF / 23 ATIQ AHMED

REFERENCE : FOR SERVICES RENDERED TO ATTEND THE LOADING OF L.N.G. ON BOARD THE VESSEL "SK SPLENDOR" FOR THE ENERGY DELIVERED AT OMAN LNG / SUR, OMAN ON 4-Aug-2009 TO 5-Aug-2009 OUR REFERENCE : YOUR REFERENCE :

SUR/09/134 OF039/09-SL100-KG

DEAR SIR / MADAM: ENCLOSED FOR YOUR REVIEW IS OUR REPORT COVERING THE VESSEL "SK SPLENDOR" AT THE ABOVE LOCATION ON THE DATES INDICATED. THE ENERGY VALUES WERE CALCULATED AS PER THE SPA SUPPLIED BY OMAN LNG / KOGAS CORPORATION SHOULD YOU HAVE ANY QUESTIONS REGARDING THIS REPORT PLEASE DO NOT HESITATE TO CONTACT US AT YOUR CONVENIENCE. WE THANK YOU FOR REQUESTING OUR SERVICES.

RESPECTFULLY FOR, INTERTEK CALEB BRETT PONNAPPA CHOKIRA MANAGER

INTERTEK OIL CHEMICAL & AGRI P.O. BOX 39, PC 114 MINA AL FAHAL SULTANATE OF OMAN TELEPHONE +968 (2) 448 0229 LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF LOADING VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

1. LAST PORT INFORMATION LAST PORT TERMINAL / PORT LAST PORT C.C.T. QUANTITY LAST PORT C.C.T. INSPECTION

: :

KOGAS / INCHEON 1,553.335 CUBIC METERS DATE : 20-Jul-2009 TIME : 15:48

2. OPENING CUSTODY TRANSFER INFORMATION OPENING CUSTODY TRANSFER VOLUME OPENING CUSTODY TRANSFER TEMPERATURES OPENING CUSTODY TRANSFER TANK PRESSURE OPENING CUSTODY TRANSFER INSPECTION

: : :

404.978 CUBIC METERS -146.2 °C - Liquid -128.5 °C - Vapor 1166 mbar DATE : 4-Aug-2009 TIME : 10:28

3. CLOSING CUSTODY TRANSFER INFORMATION CLOSING CUSTODY TRANSFER VOLUME CLOSING CUSTODY TRANSFER TEMPERATURE CLOSING CUSTODY TRANSFER TANK PRESSURE CLOSING CUSTODY TRANSFER INSPECTION

: : :

136,292.944 CUBIC METERS -160.2 °C - Liquid -152.0 °C - Vapor 1101.5 mbar DATE : 5-Aug-2009 TIME : 04:17

4. VESSEL COOL DOWN WAS NOT REQUIRED COOL DOWN TRANSFER VOLUME COOL DOWN TRANSFER TEMPERATURE COOL DOWN TRANSFER TANK PRESSURE COOL DOWN TRANSFER INSPECTION

: : :

--- CUBIC METERS --- °C - Liquid --- °C - Vapor --- mbar DATE : --TIME : ---

5-Aug-2009

5. LOAD INFORMATION ** VESSEL DELIVERED VOLUME (LIQUID) AT -160.2 °C : 135,888.000 CUBIC METERS ** VESSEL DELIVERED VOLUME (LIQUID) AT -160.2 °C : 135,888,000 LITERS ** VESSEL DELIVERED VOLUME (LIQUID) AT -160.0 °C : 135,971.000 CUBIC METERS VESSEL DELIVERED VOLUME (GAS) : 2,876.574 MILLION CUBIC FEET @ S.R.C. VESSEL DELIVERED VOLUME (GAS) : 81,455.497 1000 CUBIC METERS @ S.R.C. ** LIQUID TEMPERATURE AFTER LOADING : -160.2 °C ** VAPOR TEMPERATURE BEFORE LOADING : -128.5 °C ** TANK PRESSURE BEFORE LOADING : 1166 mbar ** LNG DENSITY AT -160.2 °C : 459.080 kg / m3 ** LNG DENSITY AT -160.0 °C 458.800 kg / m4 MASS DELIVERED : 62,172.077 METRIC TONS ** GROSS HEATING VALUE (MASS) : 54.44 MJ / kg ** GROSS HEATING VALUE (VOLUME) : 1115 BTU / SCF ** WOBBE INDEX : 1411 BTU / SCF ** INDICATED VALUES ARE ROUNDED IN ACCORDANCE WITH SPECIFIC S.P.A. REQUIREMENTS 6. ADDITIONAL INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF QUANTITY VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. CUSTODY TRANSFER DENSITY

459.080

LNG DENSITY AT -160.2 °C

kg / m3

2. CUSTODY TRANSFER VOLUME & MASS CUBIC METERS

KILOGRAMS

METRIC TONS

135,888.000

62,172,077

62,172.077

QUANTITY CONSUMED BY VESSEL

0.000

0

0.000

QUANTITY USED FOR GAS-UP

0.000

0

0.000

QUANTITY USED FOR COOL DOWN

0.000

0

0.000

135,888.000

62,172,077

62,172.077

MEGAJOULES

MMBTU

KILOWATT HOURS

3,395,719,322

3,218,508

943,255,367

QUANTITY DISPLACED

11,743,022

11,130

3,261,951

QUANTITY DELIVERED

3,383,978,343

3,207,380

939,993,417

QUANTITY CONSUMED BY VESSEL

0

0

0

QUANTITY USED FOR GAS-UP

0

0

0

QUANTITY USED FOR COOL DOWN

0

0

0

3,383,978,343

3,207,380

939,993,417

QUANTITY RECEIVED BY VESSEL

ADJUSTED QUANTITY DELIVERED

3. CUSTODY TRANSFER ENERGY

GROSS QUANTITY DELIVERED

ADJUSTED QUANTITY DELIVERED

THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F.

4. ADDITIONAL INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT ROQ 1 - Standard

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF QUANTITY VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. CUSTODY TRANSFER DENSITY

459.080

LNG DENSITY AT -160.2 °C

kg / m3

2. CUSTODY TRANSFER VOLUME & MASS CUBIC METERS

KILOGRAMS

METRIC TONS

135,888.000

62,172,077

62,172.077

QUANTITY CONSUMED BY VESSEL

0.000

0

0.000

QUANTITY USED FOR GAS-UP

0.000

0

0.000

QUANTITY USED FOR COOL DOWN

0.000

0

0.000

135,888.000

62,172,077

62,172.077

MEGAJOULES

MMBTU

KILOWATT HOURS

3,395,719,322

3,218,508

943,255,367

QUANTITY DISPLACED

11,743,022

11,130

3,261,951

QUANTITY DELIVERED

3,383,978,343

3,207,380

939,993,417

QUANTITY CONSUMED BY VESSEL

0

0

0

QUANTITY USED FOR GAS-UP

0

0

0

QUANTITY USED FOR COOL DOWN

0

0

0

3,383,978,343

3,207,380

939,993,417

QUANTITY RECEIVED BY VESSEL

ADJUSTED QUANTITY DELIVERED

3. CUSTODY TRANSFER ENERGY

GROSS QUANTITY DELIVERED

ADJUSTED QUANTITY DELIVERED

THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F.

4. QUANTITY SPLITS CARGO NUMBER

CUBIC METERS

METRIC TONS

MEGAJOULES

MMBTU

KILOWATT HOURS

1

T-54674-Y03

63,888.000

29,230.319

1,590,983,813

1,507,956

441,939,681

2

T-54674-Y04

42,000.000

19,216.025

1,045,913,476

991,331

290,531,346

3

T-54674-Y05

10,000.000

4,575.244

249,027,018

236,031

69,174,130

4

T-54674-Y06

20,000.000

9,150.488

498,054,036

472,062

138,348,260

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT ROQ 2 - Quantity Split

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF ANALYSIS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN 1. DESCRIPTION SAMPLE DESIGNATED AS SAMPLE TESTED BY SAMPLE REPRESENTING

DATE

:

4-Aug-2009

TO

5-Aug-2009

: LIQUEFIED NATURAL GAS : TERMINAL IN-LINE GC - VERIFIED PRIOR TO LOADING : COMPOSITE CONTINUOUS SAMPLING

2. ANALYSIS TEST

METHOD

METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN

GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261

LIQUID COMPOSITION 90.2400 5.9500 2.2400 0.6900 0.5800 0.0200 0.0000 0.0000 0.2800 0.0000 0.0000

MERCURY MERCAPTANS HYDROGEN SULFIDE CARBONYL SULFIDE TOTAL SULFUR HYDROCARBON DEWPOINT (MAX) 3. QUALITY SPECIFICATIONS (SPA DEFINED) TEST NONE SPECIFIED

% mol % mol % mol % mol % mol % mol % mol % mol % mol % mol % mol ng / Nm3 mg / Nm3 mg / Nm3 mg / Nm3 mg / Nm3 °C

SPECIFICATION N/A

NOT TESTED NOT TESTED NOT TESTED NOT TESTED NOT TESTED NOT TESTED

RESULT N/A

4. ADDITIONAL INFORMATION AND COMMENTS THE TEST RESULTS IN THIS DOCUMENT HAVE BEEN PROVIDED TO INTERTEK CALEB BRETT BY THE TERMINAL AND ARE PASSED ON FOR INFORMATIONAL PURPOSES ONLY. INTERTEK CALEB BRETT MAKES NO REPRESENTATION AS TO THE QUALITY OF THE MATERIAL AND ASSUMES NO RESPONSIBILITY FOR THE ACCURACY OF THE TEST RESULTS, WHICH REMAINS SOLELY WITH THE ABOVE MENTIONED PRODUCER OF THE RESULTS. THE ISSUING OF THIS REPORT DOES NOT CONSTITUTE ANY REPRESENTATION OR WARRANTY CONCERNING THE INFORMATION CONTAINED HEREIN.

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF GAS-UP VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. METHOD OF GAS-UP CALCULATION GAS-UP VALUES ARE CALCULATED BY MULTIPLYING TANK CAPACITY BY A CONSTANT VOLUME FACTOR SUBMITTED BY THE VESSEL. THE FACTOR IS DETERMINED BY THE DESIGN OF THE VESSEL TANKS.

2. CALCULATION OF VAPOR VOLUME USED FOR GAS-UP TANK NAME TANK CAPACITY

m3

FACTOR VOLUME USED

m3

1

2

3

4

37,326.000

37,336.000

37,352.000

37,345.000

1.800

1.800

1.800

1.800

67,186.800

67,204.800

67,233.600

67,221.000

3. CALCULATION VALUES FOR GAS-UP OPERATIONS VAPOR VOLUME USED FOR GAS-UP

=

268,846.200

VAPOR TEMPERTURE AFTER GAS-UP

=

24.0

VAPOR PRESSURE AFTER GAS-UP

=

1171

DENSITY OF VAPOR VOLUME FOR GAS-UP

=

0.7634

DENSITY OF LIQUID (AT LNG LOADING TEMPERATURE)

=

459.080

HIGHER HEATING VALUE (MASS)

=

54.436

HIGHER HEATING VALUE (VOLUME)

=

1115

CUBIC METERS °C mbar kg / m3 at 60°F (Ideal Gas) kg / m3 at -160.2°C MJ / kg at 15°C BTU / SCF at 60/60°F & 14.696 psi

4. VOLUME, MASS, & ENERGY USED FOR GAS-UP OPERATIONS LNG EQUIVALENT USED FOR GAS-UP

=

501.918

CUBIC METERS at -160.2°C

MASS REQUIRED FOR GAS-UP

=

230.420

METRIC TONS

ENERGY REQUIRED FOR GAS-UP

=

12,542,489

ENERGY REQUIRED FOR GAS-UP

=

11,888

MMBTU at @ 60°F

ENERGY REQUIRED FOR GAS-UP

=

3,484,025

MMBTU at @ 60°F

MJ at @ 60°F

5. ADDITION INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT ROGU 1 - Factor Calculation

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF GAS-UP VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. METHOD OF GAS-UP CALCULATION GAS-UP VALUES ARE CALCULATED BY MUTIAL AGREEMENT BETWEEN ALL PARTIES. THE VOLUME AS CALCUALTED BY FLOW METER LOCATED ASHORE. THE VOLUME REPORTED WAS SUBMITTED BY THE TERMINAL.

2. SUBMITTED VOLUME USED FOR GAS-UP =

263,487.600

CUBIC METERS (VAPOR)

VAPOR VOLUME USED FOR GAS-UP

=

263,487.600

CUBIC METERS

VAPOR TEMPERTURE AFTER GAS-UP

=

24.0

VAPOR PRESSURE AFTER GAS-UP

=

1171

DENSITY OF VAPOR VOLUME FOR GAS-UP

=

0.7634

DENSITY OF LIQUID (AT LNG LOADING TEMPERATURE)

=

459.080

HIGHER HEATING VALUE (MASS)

=

54.436

HIGHER HEATING VALUE (VOLUME)

=

1115

SUBMITTED VOLUME USED FOR GAS-UP

3. CALCULATION VALUES FOR GAS-UP OPERATIONS

°C mbar kg / m3 at 60°F (Ideal Gas) kg / m3 at -160.2°C MJ / kg at 15°C BTU / SCF at 60/60°F & 14.696 psi

4. VOLUME, MASS, & ENERGY USED FOR GAS-UP OPERATIONS LNG EQUIVALENT USED FOR GAS-UP

=

491.914

CUBIC METERS at -160.2°C

MASS REQUIRED FOR GAS-UP

=

225.828

METRIC TONS

ENERGY REQUIRED FOR GAS-UP

=

12,289,447

ENERGY REQUIRED FOR GAS-UP

=

11,648

MMBTU at @ 60°F

ENERGY REQUIRED FOR GAS-UP

=

3,413,735

MMBTU at @ 60°F

MJ at @ 60°F

5. ADDITION INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT ROGU 1 - Factor Calculation

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF COOL DOWN VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. METHOD OF COOL DOWN CALCULATION COOL DOWN VALUES ARE CALCULATED BY THE LIQUID VOLUME PER VAPOR TEMPERATURE DIFFERENTIAL METHOD. 2. PROCEDURE FOR METHOD THE DIFFERENCE OF THE VAPOR TEMPERATURES TAKEN DURING OPENING CUSTODY TRANSFER AND AFTER COOL DOWN MEASUREMENT IS MULTIPLIED BY A LIQUID VOLUME PER 1°C. THIS LIQUID VOLUME IS DEFINED WITHIN THE VESSEL'S CALIBRATION TABLES AND IS SUBMITTED BY THE CHIEF OFFICER. THE TANK TEMPERATURE IS IDENTIFIED AS : THE AVERAGE OF ONLY THE BOTTOM 2 TEMPERATURE PROBES LIQUID VOLUME REQUIRED TO LOWER THE VAPOR TEMPERATURE BY 1°C = 2.150 CUBIC METERS CALCULATED DENSITY OF CARGO LOADED = 459.080 kg / m3 at -160.2 °C HIGHER HEATING VALUE OF CARGO LOADED = 54.44 MJ / kg at 15°C 3. TANK TEMPERATURE CALCULATIONS TANK NAME 1 2 TEMP. PRIOR °C 28.00 28.00 TEMP. AFTER °C CASE #1 CASE #1 TEMP. DIFF °C #VALUE! #VALUE! M3 PER 1°C 2.150 2.150 M3 PER TANK #VALUE! #VALUE!

3 27.00 CASE #1 #VALUE! 2.150 #VALUE!

4 27.00 CASE #1 #VALUE! 2.150 #VALUE!

4. REPORTING VALUES FOR COOL DOWN OPERATIONS LIQUID VOLUME REQUIRED FOR COOL DOWN

=

#VALUE!

CUBIC METERS at -160.2 °C

MASS REQUIRED FOR COOL DOWN

=

#VALUE!

METRIC TONS

ENERGY REQUIRED FOR COOL DOWN

=

#VALUE!

MJ at @ 60°F

ENERGY REQUIRED FOR COOL DOWN

=

#VALUE!

MMBTU at @ 60°F

ENERGY REQUIRED FOR COOL DOWN

=

#VALUE!

KWH at @ 60°F

5. ADDITION INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT ROCD 1 - Temperature Differential

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF COOL DOWN VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. METHOD OF COOL DOWN CALCULATION COOL DOWN VALUES ARE CALCULATED BY THE COOL DOWN TABLES METHOD. 2. PROCEDURE FOR METHOD THE ENERGY REQUIRED TO COOL DOWN THE VESSEL TANKS TO THE REQUIRED LOADING TEMPERATURE IS OBTAINED FROM VESSEL'S CERTIFIED COOL DOWN TABLES SUBMITTED BY THE CHIEF OFFICIER. THE TABLES ARE DIVIDED INTO TWO SECTIONS. CASE #1 IS FOR WARM CONDITIONS (AVERAGE TEMPERTAURE BEING HIGHER THAN -40°C). CASE #2 IS FOR COLD CONDITIONS (AVERAGE TEMPERATURE BEING LOWER THAN -40°C). THE TANK TEMPERATURE IS IDENTIFIED AS : THE AVERAGE OF ONLY THE TOP & BOTTOM TEMPERATURE PROBES COOL DOWN TABLES PRESENTED USING : MMBTUS TEMPERATURES FOR CASE #1 TABLES ARE BETWEEN 40.0 °C AND -40.0 °C TEMPERATURES FOR CASE #2 TABLES ARE BETWEEN -40.0 °C AND -130.0 °C CALCULATED DENSITY OF CARGO LOADED = 459.080 kg / m3 at -160.2 °C HIGHER HEATING VALUE OF CARGO LOADED = 54.44 MJ / kg at 15°C 3. TANK TEMPERATURE CALCULATIONS TANK NAME 1 2 TEMPERATURE °C 28.00 28.00 TABLE USED CASE #2 CASE #2 MMBTUS 1625 2988

3 27.00 CASE #2 2988

4 27.00 CASE #2 2794

4. REPORTING VALUES FOR COOL DOWN OPERATIONS LIQUID VOLUME REQUIRED FOR COOL DOWN

=

438.860

CUBIC METERS at -160.2 °C

MASS REQUIRED FOR COOL DOWN

=

201.472

METRIC TONS

ENERGY REQUIRED FOR COOL DOWN

=

10,967,349

ENERGY REQUIRED FOR COOL DOWN

=

10,395

ENERGY REQUIRED FOR COOL DOWN

=

3,046,486

MJ at @ 60°F MMBTU at @ 60°F KWH at @ 60°F

5. ADDITION INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT ROCD 2 - Vessel Tables

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF COOL DOWN VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. METHOD OF COOL DOWN CALCULATION COOL DOWN VALUES ARE CALCULATED BY THE SPRAY NOZZLE FLOW & PRESSURE METHOD. 2. PROCEDURE FOR METHOD THE VOLUME REQUIRED TO COOL DOWN THE VESSEL TANKS TO THE REQUIRED LOADING TEMPERATURE IS OBTAINED BY CALCULATING THE VOLUME BASED ON THE NUMBER OF SPRAY NOZZLES PER TANK, FLOW CAPACITY PER NOZZLE, DURATION OF COOL DOWN, AND THE DENSITY OF THE LNG. CALCULATED DENSITY OF CARGO LOADED HIGHER HEATING VALUE OF CARGO LOADED 3. TANK PROFILE TANK NAME # OF NOZZLES FLOW RATE (L/MIN) DURATION (HOURS) DENSITY FACTOR CUBIC METERS

1 22 1.80 9.80 1.4759 34.366

= =

2 34 1.80 9.80 1.4759 53.111

459.080 kg / m3 at -160.2 °C 54.44 MJ / kg at 15°C

3 34 1.80 9.80 1.4759 53.111

4 32 1.80 9.80 1.4759 49.987

4. REPORTING VALUES FOR COOL DOWN OPERATIONS LIQUID VOLUME REQUIRED FOR COOL DOWN

=

190.575

MASS REQUIRED FOR COOL DOWN

=

87.489

ENERGY REQUIRED FOR COOL DOWN

=

4,762,303

ENERGY REQUIRED FOR COOL DOWN

=

4,514

ENERGY REQUIRED FOR COOL DOWN

=

1,322,862

CUBIC METERS at -160.2 °C METRIC TONS MJ at @ 60°F MMBTU at @ 60°F KWH at @ 60°F

5. ADDITION INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT ROCD 3 - Nozzle Flow

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF COOL DOWN VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. METHOD OF COOL DOWN CALCULATION COOL DOWN VALUES ARE CALCULATED BY USING THE NIGERIA LNG TERMINAL SUBMITTED PROCEDURE. 2. PROCEDURE FOR METHOD THE ENERGEY REQUIRED TO COOL DOWN THE VESSEL TANKS TO THE REQUIRED LOADING TEMPERATURE IS OBTAINED BY THE COMMON INDUSTRY FORMULA OF "ENERGY = VOLUME * DENSITY * HIGHER HEATING VALUE (MASS BASED)". THE VOLUME OF LNG (IN CUBIC METERS) WAS SUBMITTED BY THE TERMINAL. THE DENSITY OF THE LNG WAS CALCULATED BY USING NBS TECHNICAL NOTE 1030 (1980). THE HIGHER HEATING VALUE (MASS BASED) WAS CALCULATED BY USING THE STANDARD ISO 6976.

3. REPORTING VALUES FOR COOL DOWN OPERATIONS LIQUID VOLUME REPORTED FOR COOL DOWN

=

640.830

CUBIC METERS at -160.2 °C

DENSITY OF LNG

=

459.080

kg / m3 at -160.2 °C

HIGHER HEATING VALUE (MASS)

=

54.44

MJ / kg at 15°C

MASS REQUIRED FOR COOL DOWN

=

294.192

METRIC TONS

ENERGY REQUIRED FOR COOL DOWN

=

16,013,781

ENERGY REQUIRED FOR COOL DOWN

=

15,178

ENERGY REQUIRED FOR COOL DOWN

=

4,448,273

MJ at @ 60°F MMBTU at @ 60°F KWH at @ 60°F

4. ADDITION INFORMATION AND COMMENTS PLEASE NOTE THAT WITH RESPECT TO THE CALCULATION OF COOL DOWN QUANTITY THE TERMINAL PROCEDURE DIFFERS FROM NORMAL ACCEPTED INDUSTRY PRACTISE, WE ARE HOWEVER REQUIRED TO REPORT THE QUANTITY IN ACCORDANCE WITH TERMINAL PROCEDURES.

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT ROCD 4 - Submitted Shore

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF COOL DOWN VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. METHOD OF COOL DOWN CALCULATION COOL DOWN VALUES ARE CALCULATED BY THE COOL DOWN TABLES PLUS LIQUID FALL OUT METHOD. 2. PROCEDURE FOR METHOD THE ENERGY REQUIRED TO COOL DOWN THE VESSEL TANKS TO THE REQUIRED LOADING TEMPERATURE IS OBTAINED FROM VESSEL'S CERTIFIED COOL DOWN TABLES SUBMITTED BY THE CHIEF OFFICIER. THE TABLES ARE DIVIDED INTO TWO SECTIONS. CASE #1 IS FOR WARM CONDITIONS (AVERAGE TEMPERTAURE BEING HIGHER THAN °C). CASE #2 IS FOR COLD CONDITIONS (AVERAGE TEMPERATURE BEING LOWER THAN °C). THE TANK TEMPERATURE IS IDENTIFIED AS : THE AVERAGE OF TANK TEMPERATURES COOL DOWN TABLES PRESENTED USING : MMBTUS CALCULATED DENSITY OF CARGO LOADED = 459.080 kg / m3 at -160.2 °C HIGHER HEATING VALUE OF CARGO LOADED = 54.44 MJ / kg at 15°C 3. CALCULATIONS OF CONSUMED VALUES FOR COOL DOWN TANK NAME 1 2 3 TEMP BEFORE °C 29.10 29.40 28.80 TEMP AFTER °C 30.10 29.40 28.80 MMBTUS 2473 3638 3626 VOLUME OF LIQUID CONSUMED FOR COOL DOWN = MASS CONSUMED FOR COOL DOWN = ENERGY CONSUMED FOR COOL DOWN = ENERGY CONSUMED FOR COOL DOWN = ENERGY CONSUMED FOR COOL DOWN = 4. CALCULATIONS OF FALLOUT VALUES AFTER COOL DOWN TANK NAME 1 2 3 VOLUME BEFORE m3 21.371 37.771 38.761 VOLUME AFTER m3 47.856 44.726 60.576 VOLUME LOADED m3 26.485 6.955 21.815 VOLUME OF LIQUID FALLOUT AFTER COOL DOWN = MASS OF FALLOUT AFTER COOL DOWN = ENERGY OF FALLOUT AFTER COOL DOWN = ENERGY OF FALLOUT AFTER COOL DOWN = ENERGY OF FALLOUT AFTER COOL DOWN =

4 29.50 29.50 3358 552.849 253.802 13,815,237 13,090 3,837,566

CUBIC METERS METRIC TONS MJ at 60°F MMBTU at 60°F KWH at 60°F

4 307.075 59.168 -247.907 192.652 88.443 4,814,205 4,560 1,337,279

CUBIC METERS METRIC TONS MJ at 60°F MMBTU at 60°F KWH at 60°F

5. TOTAL VALUES FOR COOL DOWN OPERATIONS TOTAL VOLUME OF LIQUID REQUIRED FOR COOL DOWN

=

745.501

CUBIC METERS

TOTAL MASS REQUIRED FOR COOL DOWN

=

342.245

METRIC TONS

TOTAL ENERGY REQUIRED FOR COOL DOWN

=

18,629,442

TOTAL ENERGY REQUIRED FOR COOL DOWN

=

17,650

TOTAL ENERGY REQUIRED FOR COOL DOWN

=

5,174,845

MJ at 60°F MMBTU at 60°F KWH at 60°F

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT

FOR TERMINAL

ROCD 5 - Vessel Tables + Fall Out

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE + HEAVIER NITROGEN

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.902400 0.059500 0.022400 0.006900 0.005800 0.000200 0.000000 0.002800

16.043 30.070 44.097 58.123 58.123 72.150 72.150 28.0135

0.038122 0.047925 0.062478 0.078332 0.076856 0.091700 0.091562 0.046882

55.57 51.95 50.37 49.39 49.55 48.95 49.04 0

2. DENSITY CALCULATIONS DENSITY

=

DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

459.166

WITH C = K1 +

kg/m3 at -160.2 °C

( K2 - K1 ) * Xn 0.04 K1 = 0.000427

K2 = 0.000685

3. HIGHER HEATING VALUES Hm (MASS)

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi ) Σ ( Xi * Mi * Hi) * 101.325 8.31451 * 288.15

=

15°C

Hv (VOLUME) 15/15°C

=

at 101.325 kPa

WOBBE INDEX

15/15°C at

101.325 kPa

=

Hv / √

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

Hm (MASS) 15°C

Hv (VOLUME) 15/15°C

54.4355

MJ / kg

=

41.6357

MJ / m3

=

52.6895

MJ / m3

at 101.325 kPa

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

=

15/15°C at

101.325 kPa

-160.2 °C -128.5 °C 1166.000 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

404.978 m3 136,292.944 m3 135,887.966 m3

5. ENERGY DELIVERED GROSS QUANTITY DELIVERED

=

VOLUME * DENSITY * HIGHER HEATING VALUE (MASS BASED)

GROSS DELIVERED QUANTITY

=

3,396,507,919

GROSS DELIVERED QUANTITY

=

3,219,267.90

GROSS DELIVERED QUANTITY

=

943,474,422

MJ MMBTU KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 15°C. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON N.B.S. TECHNICAL NOTE 1030 (1980). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO I.S.O. 6976 (1995).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 1

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hmi)

MOLAR HHV MJ / m3 (Hvi)

METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN OXYGEN

0.902400 0.059500 0.022400 0.006900 0.005800 0.000200 0.000000 0.000000 0.002800 0.000000

16.043 30.070 44.097 58.123 58.123 72.150 72.150 86.177 28.0135 31.9988

0.038118 0.047922 0.062475 0.078328 0.076852 0.091695 0.091558 0.104864 0.046876 0.031467

55.57 51.95 50.37 49.39 49.55 48.95 49.04 48.72 0 0

37.71 66.07 93.94 121.40 121.79 149.36 149.66 177.55 0 0

SUMMATION FACTOR (√Bi) 0.0447 0.0922 0.1338 0.1789 0.1871 0.2280 0.2510 0.2950 0.0173 0.0283

2. DENSITY CALCULATIONS DENSITY

=

DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

459.159

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.24 °C

K1 = 0.000422

K2 = 0.000681

3. HIGHER HEATING VALUES Hm (MASS)

Σ ( Xi * Mi * Hmi ) Σ ( Xi * Mi )

=

15°C

Hv (VOLUME) 15/15°C

Hm (MASS) 15°C

Hv (VOLUME)

Σ ( Xi * Hvi ) / Z

=

15/15°C

at 101.325 kPa

=

54.4355

MJ / kg

=

41.7448

MJ / m3

=

52.7692

MJ / m3

at 101.325 kPa

WOBBE INDEX

15/15°C at

101.325 kPa

Hv / √

=

Σ ( Xi * Mi ) 28.96

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

= = =

WOBBE INDEX

1 Z

*

15/15°C at

101.325 kPa

-160.24 °C -128.49 °C 1166.000 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

404.978 m3 136,292.944 m3 135,887.966 m3

5. ENERGY DELIVERED QUANTITY

=

V * D * Hm - Qr

WITH

Qr

=

V *

288.15 ( 273.15 + Tv )

*

Pa 1013.25

*

37.782 (Real Gas)

GROSS QUANTITY

=

3,396,458,942

MJ

or

3,219,221.48

MMBTU

or

943,460,817

KWH

ENERGY DISPLACED

=

11,768,417

MJ

or

11,154.31

MMBTU

or

3,269,005

KWH

NET QUANTITY

=

3,384,690,525

MJ

or

3,208,067.18

MMBTU

or

940,191,812

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 15°C. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON I.S.O. 6578 (1991). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO I.S.O. 6976 (1995).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 2

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0028

16.043 30.070 44.097 58.123 58.123 72.150 72.150 28.0135

0.038122 0.047925 0.062478 0.078332 0.076856 0.091700 0.091562 0.046882

55.57 51.95 50.37 49.39 49.55 48.95 49.04 0

METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE + HEAVIER NITROGEN 2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.16

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.2 °C

K1 = 0.000427

K2 = 0.000685

3. HIGHER HEATING VALUES Hm (MASS)

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi ) Σ ( Xi * Mi * Hi) * 26.8392 23.64

=

15°C

Hv (VOLUME) 60/60°F

=

at 14.696 PSI

WOBBE INDEX

60/60°F at

14.696 PSI

Hv / √

=

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

54.4

=

1117.5

BTU / SCF

=

1414.2

BTU / SCF

at 14.696 PSI

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

=

60/60°F at

14.696 PSI

-160.2 °C -128.5 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

MJ / kg

404.978 m3 136,292.944 m3 135,887.000 m3

5. ENERGY DELIVERED Q

=

( V * D * Hm - Qr ) / 1055.12

With Qr

=

V *

288.15 ( 273.15 + Tv )

*

Pa 1013.25

*

37.7 (Ideal Gas)

GROSS QUANTITY

=

3,394,020,913

MJ

or

3,216,911

MMBTU

or

942,783,587

KWH

ENERGY DISPLACED

=

11,742,891

MJ

or

11,130

MMBTU

or

3,261,914

KWH

NET QUANTITY

=

3,382,277,424

MJ

or

3,205,780

MMBTU

or

939,521,673

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON N.B.S. TECHNICAL NOTE 1030 (1980). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO I.S.O. 6976 (1995).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 3

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE + HEAVIER NITROGEN

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.902400 0.059500 0.022400 0.006900 0.005800 0.000200 0.000000 0.002800

16.043 30.070 44.097 58.123 58.123 72.150 72.150 28.0135

0.038116 0.047922 0.062475 0.078328 0.076852 0.091695 0.091558 0.046855

55.57 51.95 50.37 49.39 49.55 48.95 49.04 0

2. DENSITY CALCULATIONS DENSITY

=

DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

459.226

WITH C = K1 +

kg/m3 at -160.24 °C

( K2 - K1 ) * Xn 0.04 K1 = 0.000427

K2 = 0.000683

3. HIGHER HEATING VALUES Hm (MASS)

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi ) Σ ( Xi * Mi * Hi) 23.64

=

15°C

Hv (VOLUME) 15/15°C

=

at 101.325 kPa

WOBBE INDEX

15/15°C at

101.325 kPa

=

Hv / √

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

Hm (MASS) 15°C

Hv (VOLUME) 15/15°C

54.436

MJ / kg

=

41.636

MJ / m3

=

52.690

MJ / m3

at 101.325 kPa

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

=

15/15°C at

101.325 kPa

-160.24 °C -128.49 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

404.978 m3 136,292.944 m3 135,887.966 m3

5. ENERGY DELIVERED GROSS QUANTITY DELIVERED

=

VOLUME * DENSITY * HIGHER HEATING VALUE (MASS BASED)

GROSS DELIVERED QUANTITY

=

3,396,985,335

GROSS DELIVERED QUANTITY

=

3,219,720

GROSS DELIVERED QUANTITY

=

943,607,038

MJ MMBTU KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 15°C. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON N.B.S. TECHNICAL NOTE 1030 (1980). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO I.S.O. 6976 (1995).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT

FOR TERMINAL

FOR VESSEL

SPA Contract # 4

LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE + HEAVIER NITROGEN

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.902400 0.059500 0.022400 0.006900 0.005800 0.000200 0.000000 0.002800

16.043 30.070 44.097 58.123 58.123 72.150 72.150 28.0135

0.038122 0.047925 0.062478 0.078332 0.076856 0.091700 0.091562 0.046882

55.52 51.9 50.33 49.35 49.51 48.91 49.01 0

2. DENSITY CALCULATIONS DENSITY

=

DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

459.166

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.2 °C

K1 = 0.000427

K2 = 0.000685

3. HIGHER HEATING VALUES Hm (MASS)

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi ) Σ ( Xi * Mi * Hi) * 101.325 8.31451 * 288.15 * Z

=

25°C

Hv (VOLUME) 25/15°C

=

at 101.325 kPa

WOBBE INDEX

25/15°C at

101.325 kPa

Hv / √

=

Σ ( Xi * Mi ) 28.96

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

25°C

Hv (VOLUME) 25/15°C

=

54.3803

MJ / kg

=

41.7030

MJ / m3

=

52.7163

MJ / m3

at 101.325 kPa

WOBBE INDEX

1 Z

*

= = =

Hm (MASS)

25/15°C at

101.325 kPa

-160.2 °C -128.5 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

404.978 m3 136,292.944 m3 135,888.000 m3

5. ENERGY DELIVERED QUANTITY

=

V * D * Hm - Qr

WITH

Qr

=

V *

288.15 ( 273.15 + Tv )

*

Pa 1013.25

*

38.8 (Real Gas)

GROSS QUANTITY

=

3,393,063,009

MJ

or

3,216,002.76

MMBTU

or

942,517,503

KWH

ENERGY DISPLACED

=

12,086,344

MJ

or

11,455.64

MMBTU

or

3,357,318

KWH

NET QUANTITY

=

3,380,976,665

MJ

or

3,204,547.12

MMBTU

or

939,160,185

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 25°C. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON N.B.S. TECHNICAL NOTE 1030 (1980). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO I.S.O. 6976 (1995).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 5

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000 0.0000

16.043 30.070 44.097 58.124 58.124 72.151 72.151 86.178 28.013 44.010 31.999

0.038122 0.047925 0.062479 0.078332 0.076857 0.091699 0.091562 0.104877 0.046866 0.027180 0.031474

55.560 51.926 50.39 49.4 49.54 48.94 49.05 48.72 0 0 0

METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN 2. DENSITY CALCULATIONS DENSITY

=

DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

459.082

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.2 °C

K1 = 0.000419

K2 = 0.000685

3. HIGHER HEATING VALUES Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

=

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi )

=

1.13285 * Σ ( Xi * Mi * Hi )

Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

at 14.696 PSIA

=

54.4233

=

1115.0

BTU / SCF

=

1411.0

BTU / SCF

at 14.696 PSIA

WOBBE INDEX

60/60°F at

14.696 PSIA

Hv / √

=

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

60/60°F at

14.696 PSIA

-160.2 °C -128.5 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

MJ / kg

404.978 m3 136,292.944 m3 135,888.000 m3

5. ENERGY DELIVERED Q

=

( V * D * Hm - Qr ) / 1055.12

With Qr

=

V *

288.15 ( 273.15 + Tv )

*

Pa 1013.25

*

37.7 (Ideal Gas)

GROSS QUANTITY

=

3,394,935,649

MJ

or

3,217,765

MMBTU

or

943,037,680

KWH

ENERGY DISPLACED

=

11,743,022

MJ

or

11,130

MMBTU

or

3,261,951

KWH

NET QUANTITY

=

3,383,192,627

MJ

or

3,206,640

MMBTU

or

939,775,730

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON N.B.S. INTERAGENCY REPORT 77-867. THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO I.P. 251/76.

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 6

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hmi)

MOLAR HHV MJ / m3 (Hvi)

METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN OXYGEN

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000

16.0426 30.0694 44.0962 58.1230 58.1230 72.1498 72.1498 86.1760 28.0134 31.9988

0.038123 0.047925 0.062479 0.078332 0.076856 0.091699 0.091562 0.104868 0.046900 0.031474

55.57 51.95 50.37 49.39 49.55 48.95 49.04 48.72 0 0

39.78 69.69 99.09 128.07 128.48 157.57 157.87 187.30 0 0

SUMMATION FACTOR (√Bi) 0.0490 0.1000 0.1453 0.2049 0.2069 0.2510 0.2864 0.3286 0.0224 0.0316

2. DENSITY CALCULATIONS DENSITY

=

DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

459.093

WITH C = K1 +

kg/m3 at -160.2 °C

( K2 - K1 ) * Xn 0.04 K1 = 0.000423

K2 = 0.000682

3. HIGHER HEATING VALUES Hm (MASS)

Σ ( Xi * Mi * Hmi ) Σ ( Xi * Mi )

=

15°C

Hv (VOLUME) 15/0°C

Hm (MASS) 15°C

Hv (VOLUME)

Σ ( Xi * Hvi ) / Z

=

15/0°C

at 101.325 kPa

=

54.44

MJ / kg

=

44.06

MJ / m3

=

55.69

MJ / m3

at 101.325 kPa

WOBBE INDEX

15/0°C at

101.325 kPa

=

Hv / √

Σ ( Xi * Mi ) 28.96

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

= = =

*

WOBBE INDEX

1 Z

15/0°C at

101.325 kPa

-160.2 °C -128.5 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

404.978 m3 136,292.944 m3 135,887.966 m3

5. ENERGY DELIVERED GROSS QUANTITY DELIVERED

=

VOLUME * DENSITY * HIGHER HEATING VALUE (MASS BASED)

GROSS DELIVERED QUANTITY

=

3,396,251,049

GROSS DELIVERED QUANTITY

=

3,219,024

GROSS DELIVERED QUANTITY

=

943,403,069

MJ MMBTU KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 15°C. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON I.S.O. 6578 (1991). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO I.S.O. 6976 (1995).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 7

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000 0.0000

16.043 30.070 44.097 58.123 58.123 72.150 72.150 86.177 28.013 44.010 31.9988

0.038123 0.047925 0.062479 0.078332 0.076856 0.091699 0.091562 0.104868 0.046900 ----0.031474

55.58 51.950 50.37 49.39 49.55 48.95 49.05 48.72 0 0 0

2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.08

WITH C = K1 +

kg/m3 at -160.2 °C

( K2 - K1 ) * Xn 0.04 K1 = 0.00042

K2 = 0.00068

3. HIGHER HEATING VALUES Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

=

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi )

=

1.13285 * Σ ( Xi * Mi * Hi )

Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

at 14.696 PSIA

=

54.4361

=

1115.3

BTU / SCF

=

1411.4

BTU / SCF

at 14.696 PSIA

WOBBE INDEX

60/60°F at

14.696 PSIA

=

Hv / √

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

60/60°F at

14.696 PSIA

-160.2 °C -128.5 °C 116.6 kPa

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

MJ / kg

405 m3 136,293 m3 135,888 m3

5. ENERGY DELIVERED GROSS QUANTITY DELIVERED

=

VOLUME * DENSITY * HIGHER HEATING VALUE (MASS BASED)

GROSS DELIVERED QUANTITY

=

3,395,912,432

GROSS DELIVERED QUANTITY

=

3,218,703

GROSS DELIVERED QUANTITY

=

943,309,009

MJ MMBTU KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 15°C. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON I.P. PART XII (1998). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO GPA 2145 SI (2000).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 8

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000

16.043 30.070 44.097 58.123 58.123 72.150 72.150 86.177 28.013 44.010

0.038122 0.047925 0.062479 0.078332 0.076857 0.091699 0.091562 0.104877 0.046866 0.027180

55.575 51.950 50.37 49.39 49.55 48.95 49.05 48.72 0 0

2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.08

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.2 °C

K1 = 0.000419

K2 = 0.000685

3. HIGHER HEATING VALUES Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

=

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi )

=

1.13285 * Σ ( Xi * Mi * Hi )

Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

at 14.696 PSIA

=

54.4361

=

1115.3

BTU / SCF

=

1411.4

BTU / SCF

at 14.696 PSIA

WOBBE INDEX

60/60°F at

14.696 PSIA

Hv / √

=

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

60/60°F at

14.696 PSIA

-160.2 °C -128 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

MJ / kg

404.978 m3 136,292.944 m3 135,887.000 m3

5. ENERGY DELIVERED Q

=

( V * D * Hm - DV ) / 1055.12

With DV

=

V *

288.15 ( 273.15 + Tv )

*

Pa 1013.25

*

37.7 * C

C = ( 0.5 )

GROSS QUANTITY

=

3,395,694,333

MJ

or

3,218,485

MMBTU

or

943,248,426

KWH

ENERGY DISPLACED

=

5,851,242

MJ

or

5,546

MMBTU

or

1,625,345

KWH

NET QUANTITY

=

3,389,843,091

MJ

or

3,212,940

MMBTU

or

941,623,081

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON N.B.S. INTERAGENCY REPORT 77-867. THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO GPA 2145 SI (1992).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 9

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000 0.0000

16.043 30.070 44.097 58.123 58.123 72.150 72.150 86.177 28.013 44.010 31.9988

0.038123 0.047925 0.062479 0.078332 0.076856 0.091699 0.091562 0.104868 0.046900 0.027183 0.031474

55.58 51.950 50.37 49.39 49.55 48.95 49.05 48.72 0 0 0

METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN 2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.11

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.2 °C

K1 = 0.000423

K2 = 0.000682

3. HIGHER HEATING VALUES Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

=

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi )

=

1.13285 * Σ ( Xi * Mi * Hi )

Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

at 14.696 PSIA

=

54.4361

=

1115.3

BTU / SCF

=

1411.4

BTU / SCF

at 14.696 PSIA

WOBBE INDEX

60/60°F at

14.696 PSIA

Hv / √

=

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

60/60°F at

14.696 PSIA

-160.2 °C -128.5 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

MJ / kg

404.978 m3 136,292.944 m3 135,887.000 m3

5. ENERGY DELIVERED Q

=

( V * D * Hm - Qr ) / 1055.12

With Qr

=

V *

288.15 ( 273.15 + Tv )

*

Pa 1013.25

*

37.707 (Ideal Gas)

GROSS QUANTITY

=

3,395,916,235

MJ

or

3,218,695

MMBTU

or

943,310,065

KWH

ENERGY DISPLACED

=

11,745,116

MJ

or

11,132

MMBTU

or

3,262,532

KWH

NET QUANTITY

=

3,384,171,119

MJ

or

3,207,560

MMBTU

or

940,047,533

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON I.P. PART XII (1998). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO GPA 2145 (2000).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 10

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000 0.0000

16.043 30.070 44.097 58.123 58.123 72.150 72.150 86.177 28.013 44.010 31.9988

0.038123 0.047925 0.062479 0.078332 0.076856 0.091699 0.091562 0.104868 0.046900 0.027183 0.031474

55.58 51.950 50.37 49.39 49.55 48.95 49.05 48.72 0 0 0

2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.11

WITH C = K1 +

kg/m3 at -160.2 °C

( K2 - K1 ) * Xn 0.04 K1 = 0.000423

K2 = 0.000682

3. HIGHER HEATING VALUES Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

=

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi )

=

1.13285 * Σ ( Xi * Mi * Hi )

Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

at 14.696 PSIA

=

54.4361

=

1115.3

BTU / SCF

=

1411.4

BTU / SCF

at 14.696 PSIA

WOBBE INDEX

60/60°F at

14.696 PSIA

=

Hv / √

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

60/60°F at

14.696 PSIA

-160.2 °C -128.5 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

MJ / kg

404.978 m3 136,292.944 m3 135,887.000 m3

5. ENERGY DELIVERED GROSS QUANTITY DELIVERED

=

VOLUME * DENSITY * HHV (MASS BASED) / 1055.12

GROSS DELIVERED QUANTITY

=

3,395,911,071

GROSS DELIVERED QUANTITY

=

3,218,690

GROSS DELIVERED QUANTITY

=

943,308,631

MJ MMBTU KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON I.P. PART XII (1998). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO GPA 2145 (2000).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 11

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000 0.0000

16.042 30.069 44.096 58.122 58.122 72.149 72.149 86.175 28.013 44.010 31.9990

0.038123 0.047925 0.062479 0.078332 0.076856 0.091699 0.091562 0.104868 0.046900 0.027183 0.031474

55.58 51.952 50.370 49.39 49.55 48.950 49.05 48.72 0 0 0

2. DENSITY CALCULATIONS DENSITY

=

DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

459.082

WITH C = K1 +

kg/m3 at -160.2 °C

( K2 - K1 ) * Xn 0.04 K1 = 0.000423

K2 = 0.000682

3. HIGHER HEATING VALUES Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

=

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi )

=

1.13285 * Σ ( Xi * Mi * Hi )

Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

at 14.696 PSIA

=

54.4372

=

1115.2

BTU / SCF

=

1411.3

BTU / SCF

at 14.696 PSIA

WOBBE INDEX

60/60°F at

14.696 PSIA

=

Hv / √

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

60/60°F at

14.696 PSIA

-160.2 °C -128.5 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

MJ / kg

404.978 m3 136,292.944 m3 135,888.000 m3

5. ENERGY DELIVERED GROSS QUANTITY DELIVERED

=

VOLUME * DENSITY * HHV (MASS BASED) / 1055.12

GROSS DELIVERED QUANTITY

=

3,395,805,565

GROSS DELIVERED QUANTITY

=

3,218,590

GROSS DELIVERED QUANTITY

=

943,279,324

MJ MMBTU KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON I.S.O. 6578 (1991). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO GPA 2145 (2003).

Mohamed-Hamid BOUABDELLI FOR INTERTEK SPA Contract # 12

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000 0.0000

16.043 30.070 44.097 58.123 58.123 72.150 72.150 86.177 28.013 44.010 31.9988

0.038123 0.047925 0.062479 0.078332 0.076856 0.091699 0.091562 0.104868 0.046900 0.027183 0.031474

55.58 51.950 50.37 49.39 49.55 48.95 49.05 48.72 0 0 0

METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN 2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.11

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.2 °C

K1 = 0.000423

K2 = 0.000682

3. HIGHER HEATING VALUES Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

=

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi )

=

1.13285 * Σ ( Xi * Mi * Hi )

Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

at 14.696 PSIA

=

54.4361

=

1115.3

BTU / SCF

=

1411.4

BTU / SCF

at 14.696 PSIA

WOBBE INDEX

60/60°F at

14.696 PSIA

Hv / √

=

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

60/60°F at

14.696 PSIA

-160.2 °C -128.5 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

MJ / kg

404.978 m3 136,292.944 m3 135,887.000 m3

5. ENERGY DELIVERED Q

=

( V * D * Hm - Qr ) / 1055.12

With Qr

=

V *

288.15 ( 273.15 + Tv )

*

Pa 1013.25

*

37.707 * 0.50

GROSS QUANTITY

=

3,395,916,235

MJ

or

3,218,695

MMBTU

or

943,310,065

KWH

ENERGY DISPLACED

=

5,872,558

MJ

or

5,566

MMBTU

or

1,631,266

KWH

NET QUANTITY

=

3,390,043,677

MJ

or

3,213,120

MMBTU

or

941,678,799

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON I.P. PART XII (1998). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO GPA 2145 (2000).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 13

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000 0.0000

16.043 30.070 44.097 58.123 58.123 72.150 72.150 86.177 28.013 44.010 31.999

0.038122 0.047925 0.062479 0.078332 0.076857 0.091699 0.091562 0.104877 0.046866 0.027180 0.031474

55.58 51.95 50.37 49.39 49.55 48.95 49.05 48.72 0 0 0

METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN 2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.08

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.2 °C

K1 = 0.000419

K2 = 0.000685

3. HIGHER HEATING VALUES Hm (MASS)

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi )

=

15°C

Hv (VOLUME) 60/60°F

Hm (MASS) 15°C

Hv (VOLUME)

Σ ( Xi * Mi * Hi) * 1.13285

=

60/60°F

at 14.696 psia

=

54.4361

=

1115

BTU / SCF

=

1411

BTU / SCF

at 14.696 psia

WOBBE INDEX

60/60°F at

14.696 psia

Hv / √

=

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING 5. ENERGY DELIVERED V * D * Hm - Qr QUANTITY = 1055.12

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

60/60°F at

14.696 psia

-160.2 °C -128.5 °C 1166 mbar

WITH

Qr

=

V *

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

288.15 ( 273.15 + Tv )

*

Pa 1013.25

= = =

*

MJ / kg

404.978 m3 136,292.944 m3 135,888.000 m3

37.7 (Ideal Gas)

GROSS QUANTITY

=

3,395,719,322

MJ

or

3,218,508

MMBTU

or

943,255,367

KWH

ENERGY DISPLACED

=

11,743,022

MJ

or

11,130

MMBTU

or

3,261,951

KWH

NET QUANTITY

=

3,383,978,343

MJ

or

3,207,380

MMBTU

or

939,993,417

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON N.B.S. INTERAGENCY REPORT 77-867. THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO G.P.A. 2145 SI (1989).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 14

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000 0.0000

16.043 30.070 44.097 58.123 58.123 72.150 72.150 86.177 28.013 44.010 31.999

0.038122 0.047925 0.062479 0.078332 0.076857 0.091699 0.091562 0.104877 0.046866 0.027180 0.031474

55.58 51.95 50.37 49.39 49.55 48.95 49.05 48.72 0 0 0

2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.08

WITH C = K1 +

kg/m3 at -160.2 °C

( K2 - K1 ) * Xn 0.04 K1 = 0.000419

K2 = 0.000685

3. HIGHER HEATING VALUES Hm (MASS)

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi )

=

15°C

Hv (VOLUME) 60/60°F

=

Hm (MASS) 15°C

Hv (VOLUME)

Σ ( Xi * Mi * Hi) * 1.13285

60/60°F

at 14.696 psia

=

54.4361

=

1115

BTU / SCF

=

1411

BTU / SCF

at 14.696 psia

WOBBE INDEX

60/60°F at

14.696 psia

=

Hv / √

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

60/60°F at

14.696 psia

-160.2 °C -128.5 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

MJ / kg

404.978 m3 136,292.944 m3 135,888.000 m3

5. ENERGY DELIVERED GROSS QUANTITY DELIVERED

=

VOLUME * DENSITY * HIGHER HEATING VALUE (MASS BASED) / 1055.12

GROSS DELIVERED QUANTITY

=

3,395,721,161

GROSS DELIVERED QUANTITY

=

3,218,510

GROSS DELIVERED QUANTITY

=

943,255,878

MJ MMBTU KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON N.B.S. INTERAGENCY REPORT 77-867. THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO G.P.A. 2145 SI (1996).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 15

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000 0.0000

16.043 30.070 44.097 58.123 58.123 72.150 72.150 86.177 28.013 44.010 31.9988

0.038123 0.047925 0.062479 0.078332 0.076856 0.091699 0.091562 0.104868 0.046900 ----0.031474

55.58 51.950 50.37 49.39 49.55 48.95 49.05 48.72 0 0 0

2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.08

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.2 °C

K1 = 0.00042

K2 = 0.00068

3. HIGHER HEATING VALUES Hm (MASS)

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi ) Σ ( Xi * Mi * Hi ) * 101.325 8.314510 * 288.15

=

15°C

Hv (VOLUME) 15/15°C

=

at 101.325 kPa

WOBBE INDEX

15/15°C at

101.325 kPa

Hv / √

=

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

Hm (MASS) 15°C

Hv (VOLUME) 15/15°C

54.4361

MJ / kg

=

41.6362

MJ / m3

=

52.6900

MJ / m3

at 101.325 kPa

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

=

15/15°C at

101.325 kPa

-160.2 °C -128.5 °C 116.6 kPa

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

405 m3 136,293 m3 135,888 m3

5. ENERGY DELIVERED QUANTITY

=

V * D * Hm - Qr

WITH

Qr

=

V *

288.15 ( 273.15 + Tv )

*

Pa 101.33

*

37.707 (Ideal Gas)

GROSS QUANTITY

=

3,395,912,432

MJ

or

3,218,703

MMBTU

or

943,309,009

KWH

ENERGY DISPLACED

=

11,745,871

MJ

or

11,133

MMBTU

or

3,262,742

KWH

NET QUANTITY

=

3,384,166,561

MJ

or

3,207,570

MMBTU

or

940,046,267

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 15°C. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON I.P. PART XII (1998). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO GPA 2145 (2000).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 16

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000 0.0000

16.043 30.070 44.097 58.123 58.123 72.150 72.150 86.177 28.0135 44.010 31.9988

0.038123 0.047925 0.062479 0.078332 0.076856 0.091699 0.091562 0.104868 0.046900 0.027192 0.031474

55.574 51.950 50.37 49.39 49.55 48.95 49.04 48.75 0 0 0

METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN 2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.11

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.2 °C

K1 = 0.000423

K2 = 0.000682

3. HIGHER HEATING VALUES Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

=

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi )

=

1.13285 * Σ ( Xi * Mi * Hi )

Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

at 14.696 PSIA

=

54.4355

=

1115

BTU / SCF

=

1411

BTU / SCF

at 14.696 PSIA

WOBBE INDEX

60/60°F at

14.696 PSIA

Hv / √

=

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

60/60°F at

14.696 PSIA

-160.2 °C -128.5 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

MJ / kg

404.978 m3 136,292.944 m3 135,888.000 m3

5. ENERGY DELIVERED Q

=

( V * D * Hm - Qr ) / 1055.12

With Qr

=

V *

273.15 ( 273.15 + Tv )

*

Pa 1013.25

*

39.78 (Ideal Gas)

GROSS QUANTITY

=

3,395,903,795

MJ

or

3,218,683

MMBTU

or

943,306,610

KWH

ENERGY DISPLACED

=

11,745,889

MJ

or

11,133

MMBTU

or

3,262,747

KWH

NET QUANTITY

=

3,384,157,906

MJ

or

3,207,550

MMBTU

or

940,043,863

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON I.S.O. 6578 (1991). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO I.S.O. 6976 (1995).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 17

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmole (Mi)

MOLAR VOL. m3 / kmole (Vi)

MOLAR HHV MJ / kg (Hi)

0.9024 0.0595 0.0224 0.0069 0.0058 0.0002 0.0000 0.0000 0.0028 0.0000 0.0000

16.043 30.070 44.097 58.124 58.124 72.151 72.151 86.178 28.013 44.010 31.999

0.038122 0.047925 0.062479 0.078332 0.076857 0.091699 0.091562 0.104877 0.046866 0.027180 0.031474

55.560 51.926 50.39 49.4 49.54 48.94 49.05 48.72 0 0 0

METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN CARBON DIOXIDE OXYGEN 2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.08

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.2 °C

K1 = 0.000419

K2 = 0.000685

3. HIGHER HEATING VALUES Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

=

Σ ( Xi * Mi * Hi ) Σ ( Xi * Mi )

=

1.13285 * Σ ( Xi * Mi * Hi )

Hm (MASS) 15°C

Hv (VOLUME) 60/60°F

at 14.696 PSIA

=

54.4233

=

1115

BTU / SCF

=

1411

BTU / SCF

at 14.696 PSIA

WOBBE INDEX

60/60°F at

14.696 PSIA

Hv / √

=

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

60/60°F at

14.696 PSIA

-160.2 °C -128.5 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

MJ / kg

404.978 m3 136,292.944 m3 135,888.000 m3

5. ENERGY DELIVERED Q

=

( V * D * Hm - Qr ) / 1055.12

With Qr

=

V *

288.15 ( 273.15 + Tv )

*

Pa 1013.25

*

37.7 (Ideal Gas)

GROSS QUANTITY

=

3,394,920,859

MJ

or

3,217,751

MMBTU

or

943,033,572

KWH

ENERGY DISPLACED

=

11,743,022

MJ

or

11,130

MMBTU

or

3,261,951

KWH

NET QUANTITY

=

3,383,177,837

MJ

or

3,206,621

MMBTU

or

939,771,621

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON N.B.S. INTERAGENCY REPORT 77-867. THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO I.P. 251/76.

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 18

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

REPORT OF CALCULATIONS VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. COMPOSITION FACTORS COMPONENTS

MOLAR FRACTION (Xi)

MOLAR WT. kg / kmol (Mi)

MOLAR VOL. m3 / kmol (Vi)

MOLAR HHV MJ / kmol (Hi)

METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE N-HEXANE NITROGEN OXYGEN

0.902400 0.059500 0.022400 0.006900 0.005800 0.000200 0.000000 0.000000 0.002800 0.000000

16.043 30.070 44.097 58.123 58.123 72.150 72.150 86.177 28.014 31.999

0.038123 0.047925 0.062479 0.078332 0.076856 0.091699 0.091562 0.104868 0.046900 0.031474

891.56 1562.14 2221.1 2870.58 2879.76 3531.68 3538.6 4198.24 0 0

2. DENSITY CALCULATIONS DENSITY

=

Σ ( Xi * Mi ) Σ ( Xi * Vi ) - Xm * C

DENSITY

=

459.10

( K2 - K1 ) * Xn 0.04

WITH C = K1 +

kg/m3 at -160.2 °C

K1 = 0.000423

K2 = 0.000682

3. HIGHER HEATING VALUES Hm (MASS)

Σ ( Xi * Hi ) Σ ( Xi * Mi ) Σ ( Xi * Hi ) * 101.325 8.314510 * 288.15

=

15°C

Hv (VOLUME) 15/15°C

=

at 101.325 kPa

WOBBE INDEX

15/15°C at

101.325 kPa

Hv / √

=

4. QUANTITIES DELIVERED LIQUID TEMPERATURE AFTER LOADING VAPOR TEMPERATURE BEFORE LOADING ABSOLUTE PRESSURE BEFORE LOADING

Hm (MASS) 15°C

Hv (VOLUME) 15/15°C

54.4346

MJ / kg

=

41.6351

MJ / m3

=

52.6886

MJ / m3

at 101.325 kPa

WOBBE INDEX

Σ ( Xi * Mi ) 28.96

= = =

=

15/15°C at

101.325 kPa

-160.2 °C -128.0 °C 1166 mbar

VESSEL O.C.T. VOLUME VESSEL C.C.T. VOLUME LOADED VOLUME

= = =

404.978 m3 136,292.944 m3 135,888.000 m3

5. ENERGY DELIVERED QUANTITY

=

V * D * Hm - Qr

WITH

Qr

=

V *

( 273.15 + 15 ) ( 273.15 + Tv )

*

Pa 1013.25

*

37.7 (Ideal Gas)

GROSS QUANTITY

=

3,395,968,923

MJ

or

3,218,745

MMBTU

or

943,324,701

KWH

ENERGY DISPLACED

=

11,703,236

MJ

or

11,092

MMBTU

or

3,250,899

KWH

NET QUANTITY

=

3,384,265,686

MJ

or

3,207,650

MMBTU

or

940,073,802

KWH

6. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 15°C. THE DENSITY CALCULATION (REVISED KLOSEK-MCKINLEY METHOD) IS BASED ON I.S.O. 6578 (1991). THE HIGHER HEATING VALUES AND QUANTITY OF ENERGY DELIVERED IS DETERMINED ACCORDING TO I.S.O. 6976 (1995).

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT SPA Contract # 19

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

OPENING CUSTODY TRANSFER VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

1. OPENING CUSTODY TRANSFER MEASUREMENTS TANK NAME 1 2 SYSTEM TYPE PRIMARY PRIMARY 1ST READING m 0.035 0.033 2ND READING m 0.035 0.032 3RD READING m 0.035 0.032 4TH READING m 0.035 0.033 5TH READING m 0.035 0.032 AVG. GAUGE m 0.035 0.032 DENSITY CORR. m 0.000 0.000 TEMP. CORR. m 0.000 0.000 TRIM CORR. m -0.003 -0.004 LIST CORR. m 0.007 0.010 CORR. GAUGE m 0.039 0.038

3 PRIMARY 0.033 0.033 0.033 0.033 0.032 0.033 0.000 0.000 -0.004 0.010 0.039

4 PRIMARY 0.287 0.297 0.290 0.290 0.290 0.291 0.000 0.000 -0.011 0.000 0.280

2. OPENING CUSTODY TRANSFER TEMPERATURES TANK NAME 1 2 TEMP PROBE #1 °C -119.60 V -123.00 V TEMP PROBE #2 °C -127.10 V -126.90 V TEMP PROBE #3 °C -129.60 V -129.00 V TEMP PROBE #4 °C -132.40 V -131.40 V TEMP PROBE #5 °C -133.10 V -131.90 V TEMP PROBE #6 °C -143.20 L -141.50 L

3 -123.10 V -127.20 V -129.10 V -131.80 V -132.30 V -142.20 L

4 -118.20 V -125.40 V -129.00 V -133.60 V -136.10 V -157.90 L

TANK AVERAGE °C -128.36 V -128.44 V -128.70 V TANK AVERAGE °C -143.20 L -141.50 L -142.20 L AVERAGE VAPOR TEMPERATURE = -128.5 °C 3. OPENING CUSTODY TRANSFER PRESSURES TANK NAME 1 2 PRESSURE 1166 1166 AVERAGE TANK PRESSURE = 1166 4. OPENING CUSTODY TRANSFER VOLUMES TANK NAME 1 2 TANK VOLUME m3 21.371 37.771 THERMAL CORR. 1.000000 1.000000 CORR. VOLUME m3 21.371 37.771

3 1166 mbar

TRIM LIST

: 10:28

-146.2 °C

4 1166 ATMOSPHERIC PRESSURE =

3 38.761 1.000000 38.761

= =

TIME

-128.46 V -157.90 L AVERAGE LIQUID TEMPERATURE =

998

mbar

4 307.075 1.000000 307.075

OPENING CUSTODY TRANSFER VOLUME =

5. ADDITION INFORMATION AND COMMENTS FWD DRAFT = 9.60 m AFT DRAFT = 9.78 m

: 4-Aug-2009

0.18 m 0.21 °P

404.978

CUBIC METERS

VESSEL DECK LINES

=

EMPTY

Mohamed-Hamid BOUABDELLI FOR INTERTEK Arrival Inspection

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

AFTER GAS-UP MEASUREMENT VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

1. OPENING CUSTODY TRANSFER MEASUREMENTS TANK NAME 1 2 SYSTEM TYPE PRIMARY PRIMARY 1ST READING m 0.000 0.000 2ND READING m 0.000 0.000 3RD READING m 0.000 0.000 4TH READING m 0.000 0.000 5TH READING m 0.000 0.000 AVG. GAUGE m 0.000 0.000 DENSITY CORR. m 0.000 0.000 TEMP. CORR. m 0.000 0.000 TRIM CORR. m 0.000 0.000 LIST CORR. m 0.000 0.000 CORR. GAUGE m 0.000 0.000

3 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

4 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

3 23.99 V 23.67 V 23.63 V 23.64 V 23.52 V

4 25.22 V 25.10 V 25.13 V 24.99 V 24.90 V

TANK AVERAGE °C 23.88 V 23.53 V 23.69 V TANK AVERAGE °C AVERAGE VAPOR TEMPERATURE = 24.0 °C

25.07 V

2. OPENING CUSTODY TRANSFER TEMPERATURES TANK NAME 1 2 TEMP PROBE #1 °C 24.02 V 23.77 V TEMP PROBE #2 °C 23.91 V 23.52 V TEMP PROBE #3 °C 23.93 V 23.50 V TEMP PROBE #4 °C 23.80 V 23.49 V TEMP PROBE #5 °C 23.74 V 23.37 V TEMP PROBE #6 °C

3. OPENING CUSTODY TRANSFER PRESSURES TANK NAME 1 2 PRESSURE 1172 1171 AVERAGE TANK PRESSURE = 1171 4. OPENING CUSTODY TRANSFER VOLUMES TANK NAME 1 2 TANK VOLUME m3 0.000 0.000 THERMAL CORR. 1.000000 1.000000 CORR. VOLUME m3 0.000 0.000

3 1172 mbar

TRIM LIST

: 03:05

°C

4 1169 ATMOSPHERIC PRESSURE =

3 0.000 1.000000 0.000

= =

TIME

AVERAGE LIQUID TEMPERATURE =

1008

mbar

4 0.000 1.000000 0.000

OPENING CUSTODY TRANSFER VOLUME =

5. ADDITION INFORMATION AND COMMENTS FWD DRAFT = 9.00 m AFT DRAFT = 9.20 m

: 7-Aug-2009

0.20 m 0.00

0.000

CUBIC METERS

VESSEL DECK LINES

=

EMPTY

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT After Gas Up Inspection

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

AFTER COOL-DOWN MEASUREMENT VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

1. AFTER COOL DOWN MEASUREMENTS TANK NAME 1 2 SYSTEM TYPE PRIMARY PRIMARY 1ST READING m 0.069 0.027 2ND READING m 0.069 0.027 3RD READING m 0.069 0.027 4TH READING m 0.069 0.027 5TH READING m 0.069 0.027 AVG. GAUGE m 0.069 0.027 DENSITY CORR. m 0.000 0.000 TEMP. CORR. m 0.000 0.000 TRIM CORR. m -0.004 -0.003 LIST CORR. m 0.005 0.010 CORR. GAUGE m 0.070 0.034

3 PRIMARY 0.042 0.042 0.042 0.042 0.042 0.042 0.000 0.000 -0.005 0.009 0.046

4 PRIMARY 0.044 0.044 0.044 0.044 0.044 0.044 0.000 0.000 -0.004 0.006 0.046

2. AFTER COOL DOWN TEMPERATURES TANK NAME 1 2 TEMP PROBE #1 °C -122.00 V -119.20 V TEMP PROBE #2 °C -124.20 V -122.00 V TEMP PROBE #3 °C -125.70 V -124.50 V TEMP PROBE #4 °C -127.70 V -126.30 V TEMP PROBE #5 °C -127.70 V -126.90 V TEMP PROBE #6 °C -158.50 L -155.10 L

3 -118.90 V -121.90 V -124.60 V -126.60 V -127.60 V -158.30 L

4 -119.40 V -122.30 V -124.70 V -126.60 V -126.90 V -158.80 L

TANK AVERAGE °C -125.46 V -123.78 V -123.92 V TANK AVERAGE °C -158.50 L -155.10 L -158.30 L AVERAGE VAPOR TEMPERATURE = -124.3 °C 3. AFTER COOL DOWN PRESSURES TANK NAME 1 PRESSURE 1069 AVERAGE TANK PRESSURE = 4. AFTER COOL DOWN VOLUMES TANK NAME 1 TANK VOLUME m3 47.856 THERMAL CORR. 1.000000 CORR. VOLUME m3 47.856

2 1070 1069.75

2 44.726 1.000000 44.726

3 1070 mbar

TRIM LIST

: 12:03

-157.7 °C

4 1070 ATMOSPHERIC PRESSURE =

3 60.576 1.000000 60.576

= =

TIME

-123.98 V -158.80 L AVERAGE LIQUID TEMPERATURE =

998

mbar

4 59.168 1.000000 59.168

AFTER COOL DOWN VOLUME =

5. ADDITION INFORMATION AND COMMENTS FWD DRAFT = 9.45 m AFT DRAFT = 9.61 m Data from Snapshot CTS

: 7-Aug-2009

0.16 m 0.15 °P

212.326

CUBIC METERS

VESSEL DECK LINES

=

EMPTY

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT After Cool Down Inspection

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

CLOSING CUSTODY TRANSFER VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

1. CLOSING CUSTODY TRANSFER MEASUREMENTS TANK NAME 1 2 SYSTEM TYPE PRIMARY PRIMARY 1ST READING m 26.360 26.236 2ND READING m 26.355 26.250 3RD READING m 26.385 26.243 4TH READING m 26.355 26.254 5TH READING m 26.393 26.250 AVG. GAUGE m 26.370 26.247 DENSITY CORR. m 0.000 0.000 TEMP. CORR. m 0.000 0.000 TRIM CORR. m -0.030 -0.042 LIST CORR. m 0.000 0.001 CORR. GAUGE m 26.340 26.206

3 PRIMARY 26.257 26.241 26.242 26.236 26.248 26.245 0.000 0.000 -0.042 0.000 26.203

4 PRIMARY 26.232 26.251 26.243 26.243 26.237 26.241 0.000 0.000 -0.036 0.000 26.205

2. CLOSING CUSTODY TRANSFER TEMPERATURES TANK NAME 1 2 TEMP PROBE #1 °C -145.40 V -155.00 V TEMP PROBE #2 °C -160.20 L -160.20 L TEMP PROBE #3 °C -160.20 L -160.30 L TEMP PROBE #4 °C -160.20 L -160.30 L TEMP PROBE #5 °C -160.20 L -160.20 L TEMP PROBE #6 °C -160.30 L -160.30 L

3 -155.10 V -160.20 L -160.20 L -160.30 L -160.20 L -160.20 L

4 -152.40 V -160.30 L -160.30 L -160.20 L -160.20 L -160.30 L

TANK AVERAGE °C -145.40 V -155.00 V -155.10 V TANK AVERAGE °C -160.22 L -160.26 L -160.22 L AVERAGE VAPOR TEMPERATURE = -152.0 °C 3. CLOSING CUSTODY TRANSFER PRESSURES TANK NAME 1 2 PRESSURE 1101 1101 AVERAGE TANK PRESSURE = 1101.5 4. CLOSING CUSTODY TRANSFER VOLUMES TANK NAME 1 2 TANK VOLUME m3 24,159.419 38,797.660 THERMAL CORR. 1.000000 1.000000 CORR. VOLUME m3 24,159.419 38,797.660

3 1102 mbar

3 38,818.221 1.000000 38,818.221

CLOSING CUSTODY TRANSFER VOLUME =

: 5-Aug-2009

TIME

-152.40 V -160.26 L AVERAGE LIQUID TEMPERATURE =

: 04:17

-160.2 °C

4 1102 ATMOSPHERIC PRESSURE =

990

mbar

4 34,517.644 1.000000 34,517.644

136,292.944

CUBIC METERS

5. ADDITION INFORMATION AND COMMENTS FWD DRAFT = 11.45 m TRIM = 0.05 m VESSEL DECK LINES AFT DRAFT = 11.50 m LIST = 0.34 °P SAMPLES FOR OMAN LNG TESTING WERE SEALED (# 046725 / # 046769 SAMPLES FOR OMAN LNG RETAIN WERE SEALED (# 046797 / # 046736) SAMPLES FOR SHIP SEALED (# 046707 / # 046761) DRY LINES OF GC WERE DONE BEFORE START FIRST STANDARD GAS INJECTION

=

FULL

Mohamed-Hamid BOUABDELLI FOR INTERTEK Departure Inspection

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

SECONDARY CUSTODY TRANSFER VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

1. OPENING SECONDARY CUSTODY TRANSFER MEASUREMENTS TANK NAME 1 2 3 1ST READING m 0.039 0.037 0.039 2ND READING m 0.035 0.038 0.037 3RD READING m 0.040 0.038 0.037 4TH READING m 0.039 0.036 0.037 5TH READING m 0.039 0.036 0.039 AVG. GAUGE m 0.038 0.037 0.038 DENSITY CORR. m 0.000 0.000 0.000 TEMP. CORR. m 0.000 0.000 0.000 TRIM CORR. m -0.004 -0.004 -0.005 LIST CORR. m 0.009 0.012 0.012 CORR. GAUGE m 0.043 0.045 0.045 2. OPENING SECONDARY CUSTODY TRANSFER VOLUMES TANK NAME 1 2 3 TANK VOLUME m3 23.611 44.882 44.875 THERMAL CORR. 1.000000 1.000000 1.000000 CORR. VOLUME m3 23.611 44.882 44.875 OPENING SECONDARY CUSTODY TRANSFER VOLUME = OPENING CUSTODY TRANSFER VOLUME = DIFFERENCE = 3. CLOSING SECONDARY CUSTODY TRANSFER MEASUREMENTS TANK NAME 1 2 3 1ST READING m 26.366 26.249 26.250 2ND READING m 26.367 26.256 26.253 3RD READING m 26.372 26.254 26.249 4TH READING m 26.368 26.253 26.248 5TH READING m 26.369 26.250 26.248 AVG. GAUGE m 26.368 26.252 26.250 DENSITY CORR. m 0.000 0.000 0.000 TEMP. CORR. m 0.000 0.000 0.000 TRIM CORR. m -0.035 -0.047 -0.047 LIST CORR. m 0.005 0.005 0.005 CORR. GAUGE m 26.338 26.210 26.208 4. CLOSING SECONDARY CUSTODY TRANSFER VOLUMES TANK NAME 1 2 3 TANK VOLUME m3 24,157.993 38,801.440 38,822.552 THERMAL CORR. 1.000000 1.000000 1.000000 CORR. VOLUME m3 24,157.993 38,801.440 38,822.552 CLOSING SECONDARY CUSTODY TRANSFER VOLUME = CLOSING CUSTODY TRANSFER VOLUME = DIFFERENCE =

:

4-Aug-2009

TO

5-Aug-2009

4 0.289 0.290 0.290 0.295 0.295 0.292 0.000 0.000 -0.012 0.003 0.283

4 310.528 1.000000 310.528 423.896 CUBIC METERS 404.978 CUBIC METERS 18.918 CUBIC METERS

4 26.254 26.256 26.256 26.256 26.255 26.255 0.000 0.000 -0.044 0.005 26.216

4 34,526.897 1.000000 34,526.897 136,308.882 CUBIC METERS 136,292.944 CUBIC METERS 15.938 CUBIC METERS

5. ADDITION INFORMATION AND COMMENTS SEA CONDITION : ROLLING

Mohamed-Hamid BOUABDELLI FOR INTERTEK

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

VESSEL MEASUREMENT - REFERENCE ONLY VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN 1. VESSEL TANK MEASUREMENTS TANK NAME 1 SYSTEM TYPE PRIMARY 1ST READING m 0.000 2ND READING m 0.000 3RD READING m 0.000 4TH READING m 0.000 5TH READING m 0.000 AVG. GAUGE m 0.000 DENSITY CORR. m 0.000 TEMP. CORR. m 0.000 TRIM CORR. m 0.000 LIST CORR. m 0.000 CORR. GAUGE m 0.000

DATE

2 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

3 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

4 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

2 30.08 V 29.78 V 29.25 V 29.26 V 29.12 V

3 29.44 V 29.18 V 28.80 V 28.67 V 28.65 V

4 29.70 V 29.61 V 29.48 V 29.48 V 29.33 V

TANK AVERAGE °C 29.26 V 29.50 V 28.95 V TANK AVERAGE °C AVERAGE VAPOR TEMPERATURE = 29.3 °C

29.52 V

2. VESSEL TANK TEMPERATURES TANK NAME 1 TEMP PROBE #1 °C 29.76 V TEMP PROBE #2 °C 29.46 V TEMP PROBE #3 °C 29.08 V TEMP PROBE #4 °C 29.28 V TEMP PROBE #5 °C 28.71 V TEMP PROBE #6 °C

3. VESSEL TANK PRESSURES TANK NAME 1 PRESSURE 1106 AVERAGE TANK PRESSURE = 4. VESSEL TANK VOLUMES TANK NAME 1 TANK VOLUME m3 0.000 THERMAL CORR. 1.000000 CORR. VOLUME m3 0.000

2 1107 1106.5

2 0.000 1.000000 0.000

3 1106 mbar

TRIM LIST

: 06:07

°C

4 1107 ATMOSPHERIC PRESSURE =

3 0.000 1.000000 0.000

= =

TIME

AVERAGE LIQUID TEMPERATURE =

992

mbar

4 0.000 1.000000 0.000

VESSEL VOLUME =

5. ADDITION INFORMATION AND COMMENTS FWD DRAFT = 9.00 m AFT DRAFT = 9.02 m

: 5-Jun-2007

0.02 m 0.02 °S

0.000

CUBIC METERS

VESSEL DECK LINES

=

EMPTY

ABDELOUAHEB ZENNIR FOR INTERTEK Vessel Measurement 1

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

VESSEL MEASUREMENT - REFERENCE ONLY VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN 1. VESSEL TANK MEASUREMENTS TANK NAME 1 SYSTEM TYPE PRIMARY 1ST READING m 0.000 2ND READING m 0.000 3RD READING m 0.000 4TH READING m 0.000 5TH READING m 0.000 AVG. GAUGE m 0.000 DENSITY CORR. m 0.000 TEMP. CORR. m 0.000 TRIM CORR. m 0.000 LIST CORR. m 0.000 CORR. GAUGE m 0.000

DATE

2 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

3 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

4 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

2 30.08 V 29.78 V 29.25 V 29.26 V 29.12 V

3 29.44 V 29.18 V 28.80 V 28.67 V 28.65 V

4 29.70 V 29.61 V 29.48 V 29.48 V 29.33 V

TANK AVERAGE °C 29.26 V 29.50 V 28.95 V TANK AVERAGE °C AVERAGE VAPOR TEMPERATURE = 29.3 °C

29.52 V

2. VESSEL TANK TEMPERATURES TANK NAME 1 TEMP PROBE #1 °C 29.76 V TEMP PROBE #2 °C 29.46 V TEMP PROBE #3 °C 29.08 V TEMP PROBE #4 °C 29.28 V TEMP PROBE #5 °C 28.71 V TEMP PROBE #6 °C

3. VESSEL TANK PRESSURES TANK NAME 1 PRESSURE 1106 AVERAGE TANK PRESSURE = 4. VESSEL TANK VOLUMES TANK NAME 1 TANK VOLUME m3 0.000 THERMAL CORR. 1.000000 CORR. VOLUME m3 0.000

2 1107 1106.5

2 0.000 1.000000 0.000

3 1106 mbar

TRIM LIST

: 06:07

°C

4 1107 ATMOSPHERIC PRESSURE =

3 0.000 1.000000 0.000

= =

TIME

AVERAGE LIQUID TEMPERATURE =

992

mbar

4 0.000 1.000000 0.000

VESSEL VOLUME =

5. ADDITION INFORMATION AND COMMENTS FWD DRAFT = 9.00 m AFT DRAFT = 9.02 m

: 5-Jun-2007

0.02 m 0.02 °S

0.000

CUBIC METERS

VESSEL DECK LINES

=

EMPTY

ABDELOUAHEB ZENNIR FOR INTERTEK Vessel Measurement 2

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

VESSEL MEASUREMENT - REFERENCE ONLY VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN 1. VESSEL TANK MEASUREMENTS TANK NAME 1 SYSTEM TYPE PRIMARY 1ST READING m 0.000 2ND READING m 0.000 3RD READING m 0.000 4TH READING m 0.000 5TH READING m 0.000 AVG. GAUGE m 0.000 DENSITY CORR. m 0.000 TEMP. CORR. m 0.000 TRIM CORR. m 0.000 LIST CORR. m 0.000 CORR. GAUGE m 0.000

DATE

2 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

3 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

4 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

2 30.08 V 29.78 V 29.25 V 29.26 V 29.12 V

3 29.44 V 29.18 V 28.80 V 28.67 V 28.65 V

4 29.70 V 29.61 V 29.48 V 29.48 V 29.33 V

TANK AVERAGE °C 29.26 V 29.50 V 28.95 V TANK AVERAGE °C AVERAGE VAPOR TEMPERATURE = 29.3 °C

29.52 V

2. VESSEL TANK TEMPERATURES TANK NAME 1 TEMP PROBE #1 °C 29.76 V TEMP PROBE #2 °C 29.46 V TEMP PROBE #3 °C 29.08 V TEMP PROBE #4 °C 29.28 V TEMP PROBE #5 °C 28.71 V TEMP PROBE #6 °C

3. VESSEL TANK PRESSURES TANK NAME 1 PRESSURE 1106 AVERAGE TANK PRESSURE = 4. VESSEL TANK VOLUMES TANK NAME 1 TANK VOLUME m3 0.000 THERMAL CORR. 1.000000 CORR. VOLUME m3 0.000

2 1107 1106.5

2 0.000 1.000000 0.000

3 1106 mbar

TRIM LIST

: 06:07

°C

4 1107 ATMOSPHERIC PRESSURE =

3 0.000 1.000000 0.000

= =

TIME

AVERAGE LIQUID TEMPERATURE =

992

mbar

4 0.000 1.000000 0.000

VESSEL VOLUME =

5. ADDITION INFORMATION AND COMMENTS FWD DRAFT = 9.00 m AFT DRAFT = 9.02 m

: 5-Jun-2007

0.02 m 0.02 °S

0.000

CUBIC METERS

VESSEL DECK LINES

=

EMPTY

ABDELOUAHEB ZENNIR FOR INTERTEK Vessel Measurement 3

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

VESSEL MEASUREMENT - REFERENCE ONLY VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN 1. VESSEL TANK MEASUREMENTS TANK NAME 1 SYSTEM TYPE PRIMARY 1ST READING m 0.000 2ND READING m 0.000 3RD READING m 0.000 4TH READING m 0.000 5TH READING m 0.000 AVG. GAUGE m 0.000 DENSITY CORR. m 0.000 TEMP. CORR. m 0.000 TRIM CORR. m 0.000 LIST CORR. m 0.000 CORR. GAUGE m 0.000

DATE

2 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

3 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

4 PRIMARY 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000

2 30.08 V 29.78 V 29.25 V 29.26 V 29.12 V

3 29.44 V 29.18 V 28.80 V 28.67 V 28.65 V

4 29.70 V 29.61 V 29.48 V 29.48 V 29.33 V

TANK AVERAGE °C 29.26 V 29.50 V 28.95 V TANK AVERAGE °C AVERAGE VAPOR TEMPERATURE = 29.3 °C

29.52 V

2. VESSEL TANK TEMPERATURES TANK NAME 1 TEMP PROBE #1 °C 29.76 V TEMP PROBE #2 °C 29.46 V TEMP PROBE #3 °C 29.08 V TEMP PROBE #4 °C 29.28 V TEMP PROBE #5 °C 28.71 V TEMP PROBE #6 °C

3. VESSEL TANK PRESSURES TANK NAME 1 PRESSURE 1106 AVERAGE TANK PRESSURE = 4. VESSEL TANK VOLUMES TANK NAME 1 TANK VOLUME m3 0.000 THERMAL CORR. 1.000000 CORR. VOLUME m3 0.000

2 1107 1106.5

2 0.000 1.000000 0.000

3 1106 mbar

TRIM LIST

: 06:07

°C

4 1107 ATMOSPHERIC PRESSURE =

3 0.000 1.000000 0.000

= =

TIME

AVERAGE LIQUID TEMPERATURE =

992

mbar

4 0.000 1.000000 0.000

VESSEL VOLUME =

5. ADDITION INFORMATION AND COMMENTS FWD DRAFT = 9.00 m AFT DRAFT = 9.02 m

: 5-Jun-2007

0.02 m 0.02 °S

0.000

CUBIC METERS

VESSEL DECK LINES

=

EMPTY

ABDELOUAHEB ZENNIR FOR INTERTEK Vessel Measurement 4

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

GENERAL INFORMATION VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

1. VESSEL - CUSTODY TRANSFER MEASUREMENT SYSTEMS VESSEL TANK DESIGN TYPE : MEMBRANE PRIMARY GAUGING DEVICE MAKE : FOXBORO SECONDARY GAUGING DEVICE MAKE : WHESSOE TEMPERATURE DEVICE MAKE : FOXBORO PRESSURE DEVICE MAKE : FOXBORO

:

4-Aug-2009

TO

5-Aug-2009

NUMBER OF TANKS : 4 TYPE : RADAR TYPE : FLOAT NUMBER PER TANK : 6 RANGE : 800 MBAR TO 1400 MBAR

2. VESSEL - CARGO TANK CAPACITY & TEMPERATURE PROBE HEIGHT PROFILES TANK NAME 1 2 3 4 GAUGE HEIGHT m 41.491 41.509 41.511 41.498 TANK CAPACITY m3 37,326.000 37,336.000 37,352.000 37,345.000 TEMP PROBE #1 26.586 26.471 26.495 26.496 TEMP PROBE #2 25.525 25.604 25.520 25.517 TEMP PROBE #3 22.847 22.839 22.849 22.844 TEMP PROBE #4 13.480 13.432 13.482 13.475 TEMP PROBE #5 6.791 6.776 6.794 6.789 TEMP PROBE #6 0.025 0.025 0.026 0.025

3. VESSEL - CARGO QUANTITY CONSUMED AS FUEL BY VESSEL METER I.D. O.C.T. READING C.C.T. READING OBSERVED CONDITIONS 1. ENGINE ROOM OP : 0 kg CL : 0 kg MASS BASED CALCS 2. 3. 4. 5. 6. 7. THE ENERGY OF GAS CONSUMED AS FUEL IS BASED ON : THE HIGHER HEATING VALUE OF LNG CARGO 4. TERMINAL - GAS CHROMATOGRAPHY EQUIPMENT TESTING EQUIPMENT MAKE : AC.AGILENT CERTIFIED REFERENCE GAS SUPPLIER : SCOTT GAS GC VERIFICATION BEFORE : YES

MODEL SERIAL # AFTER

5. TERMINAL - PRIMARY SAMPLING SYSTEM SAMPLE COLLECTOR : GAS SAMPLE HOLDER SAMPLING SYSTEM TYPE # OF SAMPLES PER SET : 3 SIZE OF SAMPLE FREQUENCY OF SAMPLING : SAMPLED AFTER COMPLETION OF BULK LOADING

APPLY YES

: 6890 : 7800102 : NO

: CONTINUOUS : 2250 cc

6. TERMINAL - SHORE STORAGE & CAPACITY TANKS 1 2 TANK ID # T 3101 T 3102 CAPACITY (M3) 135,000 135,000 7. ADDITION INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

OPERATIONAL CHECKLIST VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. SHORE OPERATIONS - PRIOR TO LOAD DID THE TERMINAL SUPPLY A CURRENT REPORT OF CALIBRATION FOR THE GC ? WAS THE GC VERIFIED AGAINST A CERTIFIED REFERENCE GAS PRIOR TO LOADING / USAGE ? DOES THE CERTIFIED REFERENCE GAS HAVE A CURRENT CERTIFICATE OF CALIBRATION ?

YES YES YES

2. VESSEL OPERATIONS - ON ARRIVAL ARE ALL PRIMARY CUSTODY GAUGING DEVISES OPERATIONAL ON ARRIVAL ? DOES THE PRIMARY SYSTEM HAVE A CURRENT CERTIFICATE OF CALIBRATION ? ARE ALL SECONDARY CUSTODY GAUGING DEVISES OPERATIONAL ON ARRIVAL ? DOES THE SECONDARY SYSTEM HAVE A CURRENT CERTIFICATE OF CALIBRATION ? ARE ALL CUSTODY REMOTE TEMPERATURE DEVISES OPERATIONAL ON ARRIVAL ? DOES THE TEMPERATURE SYSTEM HAVE A CURRENT CERTIFICATE OF CALIBRATION ? ARE ALL CUSTODY PRESSURE DEVISES OPERATIONAL ON ARRIVAL ? DOES THE PRESSURE SYSTEM HAVE A CURRENT CERTIFICATE OF CALIBRATION ? WERE THE TANKS "BOTTLED UP" DURING OPENING CUSTODY TRANSFER MEASUREMENT ? DOES THE VESSEL HAVE CURRENT CERTIFIED TANK STRAPPING TABLES ? ARE THE TANK STRAPPING TABLES WRITTEN IN ENGLISH ? DOES THE TANK STRAPPING TABLES EXPLAIN HOW TO UTILIZED THE TABLES ? DOES THE TANK STRAPPING TABLES HAVE GAUGE CORRECTION FACTORS (TRIM, LIST, ETC) ? DOES THE TANK STRAPPING TABLES HAVE 100% CAPACITIES FOR INDIVIDUAL TANKS ? DOES THE TANK STRAPPING TABLES HAVE GAUGE HEIGHTS FOR INDIVIDUAL TANKS ? DOES THE TANK STRAPPING TABLES HAVE TEMPERATURE PROFILES FOR INDIVIDUAL TANKS ?

YES YES YES YES YES YES YES YES YES YES YES YES YES YES YES YES

3. SHORE OPERATIONS - DURING LOAD WAS CORRECT NUMBER OF SAMPLES PULLED AT THE PROPER TIME DURING LOAD ?

YES

4. VESSEL OPERATIONS - ON DEPARTURE ARE ALL PRIMARY CUSTODY GAUGING DEVISES OPERATIONAL ON DEPARTURE ? ARE ALL SECONDARY CUSTODY GAUGING DEVISES OPERATIONAL ON DEPARTURE ? ARE ALL CUSTODY REMOTE TEMPERATURE DEVISES OPERATIONAL ON DEPARTURE ? ARE ALL CUSTODY PRESSURE DEVISES OPERATIONAL ON DEPARTURE ? WERE THE TANKS "BOTTLED UP" DURING CLOSING CUSTODY TRANSFER MEASUREMENT ?

YES YES YES YES YES

5. SHORE OPERATIONS - AFTER LOAD WAS THE GC VERIFIED AGAINST A CERTIFIED REFERENCE AFTER LOADING / USAGE ? DID THE TERMINAL SUPPLY A CERTIFICATE OF VERIFICATION FOR THE GC ? DID THE TERMINAL SUPPLY A COMPOSITIONAL PRINT OUT OF THE GC DURING LOAD ?

YES YES YES

6. ADDITIONAL INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT Checklist 1 - Discontinuous Sampling System

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

OPERATIONAL CHECKLIST VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. SHORE OPERATIONS - PRIOR TO LOAD WAS THE GAS SAMPLING EQUIPMENT (LINES, TANK, ETC.) INSPECTED AND PURGED ? WAS THE GAS SAMPLING EQUIPMENT SET UP PROPERLY TO RECEIVE SAMPLE ?

YES YES

2. VESSEL OPERATIONS - ON ARRIVAL WERE ALL PRIMARY CUSTODY GAUGING DEVISES OPERATIONAL ON ARRIVAL ? DID THE PRIMARY SYSTEM HAVE A CURRENT CERTIFICATE OF CALIBRATION ? WERE ALL SECONDARY CUSTODY GAUGING DEVISES OPERATIONAL ON ARRIVAL ? DID THE SECONDARY SYSTEM HAVE A CURRENT CERTIFICATE OF CALIBRATION ? WERE ALL CUSTODY REMOTE TEMPERATURE DEVISES OPERATIONAL ON ARRIVAL ? DID THE TEMPERATURE SYSTEM HAVE A CURRENT CERTIFICATE OF CALIBRATION ? WERE ALL CUSTODY PRESSURE DEVISES OPERATIONAL ON ARRIVAL ? DID THE PRESSURE SYSTEM HAVE A CURRENT CERTIFICATE OF CALIBRATION ? WERE THE TANKS "BOTTLED UP" DURING OPENING CUSTODY TRANSFER MEASUREMENT ? DID THE VESSEL HAVE CURRENT CERTIFIED TANK STRAPPING TABLES ? WERE THE TANK STRAPPING TABLES WRITTEN IN ENGLISH ? DID THE TANK STRAPPING TABLES EXPLAIN HOW TO UTILIZED THE TABLES ? DID THE TANK STRAPPING TABLES HAVE GAUGE CORRECTION FACTORS (TRIM, LIST, ETC) ? DID THE TANK STRAPPING TABLES HAVE 100% CAPACITIES FOR INDIVIDUAL TANKS ? DID THE TANK STRAPPING TABLES HAVE GAUGE HEIGHTS FOR INDIVIDUAL TANKS ? DID THE TANK STRAPPING TABLES HAVE TEMPERATURE PROFILES FOR INDIVIDUAL TANKS ?

YES YES YES YES YES YES YES YES YES YES YES YES YES YES YES YES

3. SHORE OPERATIONS - DURING LOAD WERE THE CORRECT NUMBER OF SPOT SAMPLES PULLED AT THE PROPER TIME DURING LOAD ?

YES

4. VESSEL OPERATIONS - ON DEPARTURE WERE ALL PRIMARY CUSTODY GAUGING DEVISES OPERATIONAL ON DEPARTURE ? WERE ALL SECONDARY CUSTODY GAUGING DEVISES OPERATIONAL ON DEPARTURE ? WERE ALL CUSTODY REMOTE TEMPERATURE DEVISES OPERATIONAL ON DEPARTURE ? WERE ALL CUSTODY PRESSURE DEVISES OPERATIONAL ON DEPARTURE ? WERE THE TANKS "BOTTLED UP" DURING CLOSING CUSTODY TRANSFER MEASUREMENT ?

YES YES YES YES YES

5. SHORE OPERATIONS - AFTER LOAD DID THE GAS SAMPLING EQUIPMENT WORK PROPERLY THROUGHOUT THE ENTIRE LOAD ? WERE THE CORRECT NUMBER OF TESTING SAMPLES COLLECTED FROM THE GAS SAMPLE HOLDER ? DID THE TERMINAL SUPPLY A CURRENT REPORT OF CALIBRATION FOR THE GC ? WAS THE GC VERIFIED AGAINST A CERTIFIED REFERENCE GAS PRIOR TO TESTING ? WAS THE GC VERIFIED AGAINST A CERTIFIED REFERENCE GAS AFTER TESTING ? DID THE CERTIFIED REFERENCE GAS HAVE A CURRENT CERTIFICATE OF ANALYSIS ? DID THE TERMINAL SUPPLY A CERTIFICATE OF VERIFICATION FOR THE GC AFTER TESTING ? DID THE TERMINAL SUPPLY A COMPOSITIONAL PRINT OUT OF THE GC ANALYSIS ?

YES YES YES YES YES YES YES YES

6. ADDITIONAL INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT Checklist 2 - Continuous Sampling System

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

VERIFICATION OF GC VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

4-Aug-2009

TO

5-Aug-2009

1. OPENING VERIFICATION OF GC CERTIFIED VARIANCE TEST GC VARIANCE TEST GC VARIANCE TEST GC VARIANCE COMPONENT RESULTS ALLOWED RUN #1 PCT. RUN #2 PCT. RUN #3 PCT. METHANE 91.9398 1.00% 91.9301 0.01% 91.9397 0.00% 91.9355 0.00% ETHANE 5.0400 10.00% 5.0499 -0.20% 5.0412 -0.02% 5.0422 -0.04% PROPANE 1.0020 10.00% 1.0028 -0.08% 1.0034 -0.14% 1.0020 0.00% ISO BUTANE 0.1520 10.00% 0.1526 -0.39% 0.1523 -0.20% 0.1530 -0.66% N-BUTANE 0.2030 10.00% 0.2031 -0.05% 0.2027 0.15% 0.2030 0.00% ISO PENTANE 0.0531 10.00% 0.0532 -0.19% 0.0528 0.56% 0.0535 -0.75% N-PENTANE 0.0538 10.00% 0.0543 -0.93% 0.0534 0.74% 0.0540 -0.37% HEXANE + HVR 0.0503 10.00% 0.0501 0.40% 0.0500 0.60% 0.0508 -0.99% NITROGEN 1.0130 10.00% 1.0130 0.00% 1.0139 -0.09% 1.0150 -0.20% CARBON DIOXIDE 0.4930 10.00% 0.4909 0.43% 0.4906 0.49% 0.4910 0.41% OXYGEN 0.0000 10.00% 0.0000 0.00% 0.0000 0.00% 0.0000 0.00% TOTAL 100.0000 100.0000 100.0000 100.0000 OPENING VERIFICATION FOUND WITHIN VARIANCE YES DATE : 26-May-2007 TIME : 08:00 2. CLOSING VERIFICATION OF GC CERTIFIED VARIANCE TEST GC VARIANCE TEST GC VARIANCE TEST GC VARIANCE COMPONENT RESULTS ALLOWED RUN #1 PCT. RUN #2 PCT. RUN #3 PCT. METHANE 91.9398 1.00% 91.9301 0.01% 91.9397 0.00% 91.9355 0.00% ETHANE 5.0400 10.00% 5.0499 -0.20% 5.0412 -0.02% 5.0422 -0.04% PROPANE 1.0020 10.00% 1.0028 -0.08% 1.0034 -0.14% 1.0020 0.00% ISO BUTANE 0.1520 10.00% 0.1526 -0.39% 0.1523 -0.20% 0.1530 -0.66% N-BUTANE 0.2030 10.00% 0.2031 -0.05% 0.2027 0.15% 0.2030 0.00% ISO PENTANE 0.0531 10.00% 0.0532 -0.19% 0.0528 0.56% 0.0535 -0.75% N-PENTANE 0.0538 10.00% 0.0543 -0.93% 0.0534 0.74% 0.0540 -0.37% HEXANE + HVR 0.0503 10.00% 0.0501 0.40% 0.0500 0.60% 0.0508 -0.99% NITROGEN 1.0130 10.00% 1.0130 0.00% 1.0139 -0.09% 1.0150 -0.20% CARBON DIOXIDE 0.4930 10.00% 0.4909 0.43% 0.4906 0.49% 0.4910 0.41% OXYGEN 0.0000 10.00% 0.0000 0.00% 0.0000 0.00% 0.0000 0.00% TOTAL 100.0000 100.0000 100.0000 100.0000 CLOSING VERIFICATION FOUND WITHIN VARIANCE YES DATE : 26-May-2007 TIME : 10:00 3. EQUIPMENT INFORMATION AND CERTIFIED REFERENCE GAS TESTING EQUIPMENT MAKE : AC.AGILENT LAST CALIBRATION DATE : 15-Feb-2007 CERTIFIED REFERENCE GAS SUPPLIER : SCOTT GAS CERTIFICATION DATE : 15-Feb-2007

MODEL TIME SERIAL # TIME

: : : :

6890 17:00 7800102 17:00

4. ADDITIONAL INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT Verification of GC 1 - Site Specific

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

VERIFICATION OF GC VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN INSTRUMENT : GC C (HP 5890)

DATE

LABORATORY TEMP :

1. REFERENCE STANDARD GAS COMPONENT METHANE CH4 ETHANE C2H6 PROPANE C3H8 ISO BUTANE i-C4H10 N-BUTANE n-C4H10 ISO PENTANE i-C5H12 N-PENTANE n-C5H12 NITROGEN N2 OXYGEN O2 CARBON DIOXIDE CO2 TOTAL 2. SAMPLE GAS COMPONENT

90.4013 4.4400 3.3500 0.7080 0.6850 0.0286 0.0286 0.2870 0.0297 0.0418 100.0000

First Sample Count Peak Area (C)

METHANE CH4 ETHANE C2H6 PROPANE C3H8 ISO BUTANE i-C4H10 N-BUTANE n-C4H10 ISO PENTANE i-C5H12 N-PENTANE n-C5H12 NITROGEN N2 OXYGEN O2 CARBON DIOXIDE CO2 TOTAL 3. NORMALIZATION COMPONENT

Cylinder # :

Concent Mol % (A)

276,238 692,500 440,672 89,076 72,378 0 0 2,494 0 0

Average Sample Count Peak Area (E)

METHANE CH4 ETHANE C2H6 PROPANE C3H8 ISO BUTANE i-C4H10 N-BUTANE n-C4H10 ISO PENTANE i-C5H12 N-PENTANE n-C5H12 NITROGEN N2 OXYGEN O2 CARBON DIOXIDE CO2 TOTAL

276,275.5 692,603.0 440,803.5 89,093.0 72,333.0 0.0 0.0 2,491.0 0.0 0.0

: 13-Nov-2007

First RSG Count Peak Area

272,177 606,946 702,057 198,637 193,331 10,178 9,918 32,198 3,195 5,791

Cylinder # : CPC-01 Second Sample Unnormal Count Mol % Peak Area (C) x (A) / (B) (D) 91.662 5.062 2.103 0.317 0.256 0.000 0.000 0.022 0.000 0.000 99.422

Unnormal Mol % (E) x (A) / (B)

276,313 692,706 440,935 89,110 72,288 0 0 2,488 0 0

Reported Value Mol%

91.674 5.063 2.104 0.317 0.256 0.000 0.000 0.022 0.000 0.000 99.436

92.19 5.09 2.12 0.32 0.26 0.00 0.00 0.02 0.00 0.00 100.00

: 15:00

23-23.5 °C

GS 66889

Second RSG Count Peak Area

272,701 607,832 701,594 198,953 193,667 10,224 9,937 32,521 3,283 5,636

TIME

Repeatability

Average RSG Count Peak Area (B)

0.19 0.15 0.07 0.16 0.17 0.45 0.19 1.00 2.72 2.71

272,439.0 607,389.0 701,825.5 198,795.0 193,499.0 10,201.0 9,927.5 32,359.5 3,239.0 5,713.5

Seal # :

004659

Unnormal Mol % (D) x (A) / (B)

Repeatability

91.687 5.064 2.105 0.317 0.256 0.000 0.000 0.022 0.000 0.000 99.451

Load Port Mol %

0.03 0.03 0.06 0.04 0.12 0.00 0.00 0.24 0.00 0.00

Difference %

92.8085 4.7397 1.8893 0.2689 0.2151 0.0022 0.0000 0.0762 0.0000 0.0000 100.000

-0.6185 0.3503 0.2307 0.0511 0.0449 -0.0022 -0.0562

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT Verification of GC 2 - Site Specific

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

BUNKER SURVEY VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN 1. VESSEL HISTORY FROM CHIEF ENGINEER BUNKER PRODUCT : FUEL OIL LAST PORT OF CALL : SINGAPORE BUNKERS ON DEPARTURE : 1337.000 BUNKERS AT E.O.S.P. : 1463.160 BUNKERS RECEIVED INTRANSIT : 3713.910 BUNKERS RECEIVED IN PORT : 0.000 2. INSPECTION UPON ARRIVAL VESSEL'S ULLAGES TANK METERS TANK 1 FWD 24.200 TANK 2 STB 4.970 TANK 2 PORT 8.401 TANK 4 STB 3.633 TANK 1 SETTLING 8.790 TANK 2 SETTLING 5.476

TOTALS DATE : 3-Jun-2008

G.O.V. m3 0.000 481.000 474.000 141.000 212.000 197.000

G.O.V. m3 0.000 482.000 474.000 140.000 213.000 123.000

G.O.V. = 1432.000 TIME : 15:00

4. ADDITIONAL INFORMATION AND COMMENTS QUANTITY OF BUNKERS CONSUMED DURING VOYAGE QUANTITY OF BUNKERS CONSUMED DURING LOAD

TEMP. °C 20.0 42.8 49.0 39.7 60.0 60.0

V.C.F. T54B - 2004 0.99658 0.98092 0.97664 0.98306 0.96902 0.96902

DRAFT FWD

TEMP. °C 20.0 43.0 44.0 39.0 55.0 55.0

:

4-Aug-2009

TO

:

G.S.V. m3 0.000 471.823 462.927 138.611 205.432 190.897

DENSITY @ 15°C 0.9894 0.9894 0.9894 0.9894 0.9894 0.9894

G.S.V. = 1469.691 M.T. = 9.60 m DRAFT AFT :

V.C.F. T54B - 2004 0.99658 0.98078 0.98009 0.98354 0.97249 0.97249

DRAFT FWD

: :

:

5-Aug-2009

DAYS AT SEA : 9.00 AT ANCH : 0.00 AVERAGE BUNKER CONSUMPTION PER DAY AT SEA : 200.000 METRIC TONS AT LOAD : 20.000 METRIC TONS AT DISC : 20.000 METRIC TONS AT ANCHOR : 20.000 METRIC TONS

METRIC TONS METRIC TONS METRIC TONS METRIC TONS

G.O.V. = 1505.000 TIME : 07:40

3. INSPECTION PRIOR TO SAILING VESSEL'S ULLAGES TANK METERS TANK 1 FWD 0.000 TANK 2 STB 4.950 TANK 2 PORT 8.420 TANK 4 STB 3.630 TANK 1 SETTLING 8.790 TANK 2 SETTLING 5.130

TOTALS DATE : 5-Jun-2008

DATE

G.S.V. m3 0.000 472.736 464.563 137.696 207.140 119.616

DENSITY @ 15°C 0.9894 0.9894 0.9894 0.9894 0.9894 0.9894

G.S.V. = 1401.751 M.T. = 11.45 m DRAFT AFT :

M. TONS ( AIR ) 0.000 466.302 457.511 136.990 203.029 188.663

1452.495 9.78 m

M. TONS ( AIR ) 0.000 467.205 459.127 136.085 204.717 118.217

1385.351 11.50 m

3598.415 METRIC TONS 67.144 METRIC TONS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT Bunker - Fuel Oil

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

BUNKER SURVEY VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN 1. VESSEL HISTORY FROM CHIEF ENGINEER BUNKER PRODUCT : MARINE DIESEL OIL LAST PORT OF CALL : SINGAPORE BUNKERS ON DEPARTURE : 159.890 BUNKERS AT E.O.S.P. : 133.800 BUNKERS RECEIVED INTRANSIT : 0.000 BUNKERS RECEIVED IN PORT : 0.000 2. INSPECTION UPON ARRIVAL VESSEL'S ULLAGES TANK METERS D.O TK 6.062 D.O SERVICE 3.908

TOTALS DATE : 3-Jun-2008

G.O.V. m3 80.200 77.300

G.O.V. m3 80.200 77.300

G.O.V. = 157.500 TIME : 15:00

4. ADDITIONAL INFORMATION AND COMMENTS QUANTITY OF BUNKERS CONSUMED DURING VOYAGE QUANTITY OF BUNKERS CONSUMED DURING LOAD

TEMP. °C 25.0 25.0

V.C.F. T54B - 2004 0.99180 0.99180

DRAFT FWD

TEMP. °C 25.0 25.0

:

4-Aug-2009

TO

:

G.S.V. m3 79.542 76.666

DENSITY @ 15°C 0.8600 0.8600

G.S.V. = 156.209 M.T. = 9.60 m DRAFT AFT :

V.C.F. T54B - 2004 0.99180 0.99180

DRAFT FWD

: :

:

5-Aug-2009

DAYS AT SEA : 9.00 AT ANCH : 0.00 AVERAGE BUNKER CONSUMPTION PER DAY AT SEA : 0.000 METRIC TONS AT LOAD : 0.000 METRIC TONS AT DISC : 1.000 METRIC TONS AT ANCHOR : 0.000 METRIC TONS

METRIC TONS METRIC TONS METRIC TONS METRIC TONS

G.O.V. = 157.500 TIME : 07:40

3. INSPECTION PRIOR TO SAILING VESSEL'S ULLAGES TANK METERS D.O TK 6.063 D.O SERVICE 3.908

TOTALS DATE : 5-Jun-2008

DATE

G.S.V. m3 79.542 76.666

DENSITY @ 15°C 0.8600 0.8600

G.S.V. = 156.209 M.T. = 11.45 m DRAFT AFT :

M. TONS ( AIR ) 68.319 65.849

134.168 9.78 m

M. TONS ( AIR ) 68.319 65.849

134.168 11.50 m

25.722 METRIC TONS 0.000 METRIC TONS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT Bunker - Diesel Oil

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

TIME LOG VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN 1. TIMES DATE 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 4-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009 5-Aug-2009

HOUR 05:15 09:15 06:54 08:15 09:15 09:22 09:22 09:32 09:49 10:00 10:30 10:33 09:15 10:27 10:28 10:40 12:15 12:20 12:59 02:47 03:25 04:21 04:22 04:25 04:39 05:00 05:15 06:30 06:05 06:25 06:26 06:52 07:17 07:30 07:40 08:00 08:00

DATE

:

4-Aug-2009

TO

5-Aug-2009

EVENT END OF SEA PASSAGE NOTICE OF READINESS TENDERED PILOT ON BOARD FIRST LINE ASHORE VESSEL ALL FAST TERMINAL GANGWAY DOWN & SECURE INSPECTOR ON BOARD COMMENCED CONNECTION OF CARGO & VAPOR ARMS COMPLETED CONNECTION OF CARGO & VAPOR ARMS COMMENCED PRE-LOAD KEY / SAFETY MEETING COMPLETED PRE-LOAD KEY / SAFETY MEETING COMMENCED TESTING OF E.S.D. NOTICE OF READINESS ACCEPTED COMMENCED OPENING CUSTODY TRANSFER INSPECTION COMPLETED OPENING CUSTODY TRANSFER INSPECTION COMMENCED COOL DOWN OF CARGO ARMS & VESSEL LINES COMPLETED COOL DOWN OF CARGO ARMS & VESSEL LINES COMMENCED LOADING OF CARGO FULL RATE LOADING LOADING RATE DOWN START COMPLETED LOADING COMMENCED CLOSING CUSTODY TRANSFER INSPECTION COMPLETED CLOSING CUSTODY TRANSFER INSPECTION COMMENCED DISCONNECTION OF VARGO & VAPOR ARMS COMPLETED DISCONNECTION OF CARGO & VAPOR ARMS POST LOADING MEETING & DOCUMENTATION VESSEL CLEAR ETS ANALYSIS COMPLETED COMMENCED CLOSING CUSTODY TRANSFER INSPECTION COMPLETED CLOSING CUSTODY TRANSFER INSPECTION COMMENCED DISCONNECTION OF CARGO & VAPOR ARMS COMPLETED DISCONNECTION OF CARGO & VAPOR ARMS POST LOADING MEETING & DOCUMENTATION VESSEL CLEARED VESSEL SAILED ANALYSIS COMPLETED

2. ADDITIONAL INFORMATION AND COMMENTS Sampling started : 17:15 0n 31st July 2008 and completed at 06:20 0n 01st August 2008 Analysis completed : 09:15 on 1st August 2008

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT Time Log - Page 1

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

TIME LOG VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN 1. TIMES DATE

HOUR

DATE

:

4-Aug-2009

TO

5-Aug-2009

EVENT

2. ADDITIONAL INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT Time Log - Page 2

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

TIME LOG VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN 1. TIMES DATE

HOUR

DATE

:

4-Aug-2009

TO

5-Aug-2009

EVENT

2. ADDITIONAL INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT Time Log - Page 3

FOR TERMINAL

FOR VESSEL LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

LETTER OF PROTEST VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

TIME

:

TO :

SIR : ON BEHALF OF OUR CLIENT(S), WE HAVE BEEN APPOINTED INSPECTORS ON THE ABOVE NAMED VESSEL. ACTING FOR AND ON THEIR BEHALF, WE HEREBY NOTIFY YOU THAT ON THE LISTED DATE AND TIME THE FOLLOWING OCCURRED.

WE HEREBY RESERVE THE RIGHT OF OUR PRINCIPALS TO REFER TO THIS MATTER AT A LATER DATE AND TAKE SUCH ACTION AS MAY BE DEEMED NECESSARY. KINDLY ACKNOWLEDGE RECEIPT ON THE COPY THEREOF AND RETURN IT TO US. THE SIGNATURE THUS OBTAINED ARE FOR RECEIPT ONLY AND IN NO WAY ACKNOWLEDGE RESPONSIBILITY FOR THE INCIDENT. RECEIVED BY

YOURS FAITHFULLY,

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT LOP 1

LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

LETTER OF PROTEST VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

TIME

:

TO :

SIR : ON BEHALF OF OUR CLIENT(S), WE HAVE BEEN APPOINTED INSPECTORS ON THE ABOVE NAMED VESSEL. ACTING FOR AND ON THEIR BEHALF, WE HEREBY NOTIFY YOU THAT ON THE LISTED DATE AND TIME THE FOLLOWING OCCURRED.

WE HEREBY RESERVE THE RIGHT OF OUR PRINCIPALS TO REFER TO THIS MATTER AT A LATER DATE AND TAKE SUCH ACTION AS MAY BE DEEMED NECESSARY. KINDLY ACKNOWLEDGE RECEIPT ON THE COPY THEREOF AND RETURN IT TO US. THE SIGNATURE THUS OBTAINED ARE FOR RECEIPT ONLY AND IN NO WAY ACKNOWLEDGE RESPONSIBILITY FOR THE INCIDENT. RECEIVED BY

YOURS FAITHFULLY,

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT LOP2

LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

LETTER OF PROTEST VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

TIME

:

TO :

SIR : ON BEHALF OF OUR CLIENT(S), WE HAVE BEEN APPOINTED INSPECTORS ON THE ABOVE NAMED VESSEL. ACTING FOR AND ON THEIR BEHALF, WE HEREBY NOTIFY YOU THAT ON THE LISTED DATE AND TIME THE FOLLOWING OCCURRED.

WE HEREBY RESERVE THE RIGHT OF OUR PRINCIPALS TO REFER TO THIS MATTER AT A LATER DATE AND TAKE SUCH ACTION AS MAY BE DEEMED NECESSARY. KINDLY ACKNOWLEDGE RECEIPT ON THE COPY THEREOF AND RETURN IT TO US. THE SIGNATURE THUS OBTAINED ARE FOR RECEIPT ONLY AND IN NO WAY ACKNOWLEDGE RESPONSIBILITY FOR THE INCIDENT. RECEIVED BY

YOURS FAITHFULLY,

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT LOP 3

LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

LETTER OF PROTEST VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

:

TIME

:

TO :

SIR : ON BEHALF OF OUR CLIENT(S), WE HAVE BEEN APPOINTED INSPECTORS ON THE ABOVE NAMED VESSEL. ACTING FOR AND ON THEIR BEHALF, WE HEREBY NOTIFY YOU THAT ON THE LISTED DATE AND TIME THE FOLLOWING OCCURRED.

WE HEREBY RESERVE THE RIGHT OF OUR PRINCIPALS TO REFER TO THIS MATTER AT A LATER DATE AND TAKE SUCH ACTION AS MAY BE DEEMED NECESSARY. KINDLY ACKNOWLEDGE RECEIPT ON THE COPY THEREOF AND RETURN IT TO US. THE SIGNATURE THUS OBTAINED ARE FOR RECEIPT ONLY AND IN NO WAY ACKNOWLEDGE RESPONSIBILITY FOR THE INCIDENT. RECEIVED BY

YOURS FAITHFULLY,

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT LOP 4

LNG-LD-009H1 (07-AUG-09) - 14

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

NIGERIA LNG CERTIFICATE OF LOADING VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

1. IDENTIFICATION (a) CARGO RECEIVER (NLNG CUSTOMER) (b) NIGERIA LNG CARGO NUMBER (c) COMMENCED LOADING OF LNG (d) COMPLETED LOADING ON LNG 2. BASIC DATA (a) (b) (c) (d) (e)

(f)

(g) 3. RESULTS (a) (b) (c) (d)

DATE DATE

: 15-Apr-2008

: : : :

BRITISH GAS 963 11-May-2008 13-May-2008

LIQUID LNG VOLUME LOADED : AVERAGE TEMPERATURE OF LIQUID AFTER LOADING : AVERAGE TEMPERATURE OF VAPOR BEFORE LOADING : AVERAGE ABSOLUTE PRESSURE BEFORE LOADING : LNG CARGO COMPOSITION: COMPONENTS MOLE PERCENTAGE N2 NITROGEN 0.28 C1 METHANE 90.24 C2 ETHANE 5.95 C3 PROPANE 2.24 i-C4 ISO BUTANE 0.69 n-C4 N-BUTANE 0.58 i-C5 ISO PENTANE 0.02 n-C5 + N-PENTANE & HEAVIER 0 IMPURITIES CARBON DIOXIDE : MERCURY : MERCAPTAN : HYDROGEN SULFIDE : CARBONYL SULFIDE : TOTAL SULFUR : HYDROCARBON DEWPOINT (MAX - between 1-80 bar gauge) :

LNG DENSITY AT -160.2 °C GROSS CALORIFIC VALUE (MASS) GROSS CALORIFIC VALUE (VOLUME) WOBBE INDEX (VOLUME)

: : : :

TIME TIME

: 23:00 : 01:00

135,888.000 CUBIC METERS -160.2 °C -128.5 °C 1166 mbar

0 N/A N/A N/A N/A N/A N/A

mol % ng / Nm3 mg / Nm3 mg / Nm3 mg / Nm3 mg / Nm3 °C

459.080 kg / m3 54.44 MJ / kg 1115 BTU / SCF 1411 BTU / SCF

4. TOTAL QUANTITY OF LNG UNLOADED GROSS QUANTITY DELIVERED QUANTITY DISPLACED QUANTITY CONSUMED BY VESSEL QUANTITY FOR GAS-UP QUANTITY FOR COOL DOWN ADJUSTED QUANTITY DELIVERED

MEGAJOULES 3,395,719,322 11,743,022 0 0 0 3,383,978,343

MMBTU 3,218,508 11,130 0 0 0 3,207,380

KILOWATT HOURS 943,255,367 3,261,951 0 0 0 939,993,417

5. ADDITIONAL INFORMATION AND COMMENTS THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F.

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT CSR 1 - Nigeria LNG Certificate of Loading

LNG-LD-009H1 (07-AUG-09) - 14

BG DATA SHEET - LOAD

Vessel Name: Cargo No: Dates: File #:

SK SPLENDOR OF039/09-SL100-KG JAN 4-5, 2009 SUR/09/134

Terminal / Port: Last Port of Call: Dates at Last Port: Last Port CCT Volume:

135,888.000 3,207,380 3,207,380 62,172.077 0.000 0 0.000 0 404.978 136,292.944 135,888.000 -160.2 459.080 458.800 54.44 51593 1115 1117.6 1411 1414.3 3,218,508 11,130 3,207,380 0 3,207,378 1148.357 20-Jul-2009 4-Aug-2009

m3 MMBtu (60°F) MMBtu (60°F) MT m3 MMBtu (60°F) m3 MMBtu (60°F) m3 m3 m3 Deg. C KG/M3 KG/M3 MJ / kg (15°C) BTU / kg (60°F) BTU / SCF (60/60°F & 14.696 psi) BTU / SCF (60/60°F & 14.73 psi) BTU / SCF (60/60°F & 14.696 psi) BTU / SCF (60/60°F & 14.73 psi) MMBtu (60°F) MMBtu (60°F) MMBtu (60°F) MMBtu (60°F) MMBtu (60°F) m3 Date 15:48 Time Date 10:28 Time Hrs E to W Days % per day % per day

OMAN LNG INCHEON 20-Jul-2009 1,553.335

LNG Data Total Load Volume Total Load Quantity BG - Total Load Quantity Total Load Quantity Cooldown Volume Cooldown Volume Gas up Volume Gas up Volume Vessel OCT Volume before loading Vessel CCT Volume after loading Vessel Volume Received Observied Liquid Temp after loading LNG Density @ -160.2 °C LNG Density @ -160.0 °C Higher Heating Value (mass) BG - Higher Heating Value (mass) Higher Heating Value (Volume) BG - Higher Heating Value (Volume) Wobbe Index BG - Wobbe Index Gross Energy Received Vapor Return Energy Delivered Gas Consumed During Load Net Energy Received Intransit Difference Last Port of call CCT inspection: Load Port OCT inspection Time zone adjustment between ports Length of Voyage Estimated LNG Boil-off per day Vessel Design Limits

Bunker Data (Fuel Oil) Bunkers on Closing Last Port Bunker Survey Bunkers on Opening Load Port Bunker Survey Bunkers on Closing Load Port Bunker Survey Bunkers Received intransit Average Daily Consumption Rates: At Load At Discharge At Sea At Anchorage:

1,337.000 1452.495 3-Jun-2008 1385.351 5-Jun-2008 3713.910

MT Date MT Date MT Date MT

20.000 20.000 200.000 20.000

MT MT MT MT

90.2400 5.9500 2.2400 0.6900 0.5800 0.0200 0.0000 0.0000 0.2800 0.0000

% mol % mol % mol % mol % mol % mol % mol % mol % mol % mol

Time 07:40

Time

15:00

Time

10:28 04:17

Time Time

Quality Methane CH4 Ethane C2H6 Propane C3H8 i-Butane i-C4H10 n-Butane n-C4H10 i-Pentane i-C5H12 n-Pentane n-C5H12 n-Hexane n-C6H14 Nitrogen N2 Carbon Dioxide CO2

Impurities Mercury Mercaptans Mercaptans Hydrogen Sulphide Hydrogen Sulphide Total Sulphur Total Sulphur

ng/Nm3 mg/Nm3 ppm mg/Nm3 ppm mg/Nm3 ppm

Time log Summary Additions OCT Inspection Completed CCT Inspection Completed

4-Aug-2009 5-Aug-2009

Date Date

m3

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

BP CERTIFICATE OF LOADING VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN

DATE

: 15-Apr-2008

1. QUALITY COMPONENTS METHANE 90.24 Mol % NITROGEN ETHANE 5.95 Mol % CARBON DIOXIDE PROPANE 2.24 Mol % OXYGEN ISO BUTANE 0.69 Mol % MERCURY N-BUTANE 0.58 Mol % MERCAPTAN ISO PENTANE 0.02 Mol % HYDROGEN SULFIDE N-PENTANE 0 Mol % CARBONYL SULFIDE N-HEXANE 0 Mol % TOTAL SULFUR AVERAGE TEMPERATURE OF LIQUID AFTER LOADING AVERAGE TEMPERATURE OF VAPOR BEFORE LOADING AVERAGE ABSOLUTE PRESSURE BEFORE LOADING LNG DENSITY AT -160.2 °C GROSS CALORIFIC VALUE (MASS) GROSS CALORIFIC VALUE (VOLUME) WOBBE INDEX (VOLUME) THE STANDARD REFERENCE CONDITIONS IDENTIFIES TEMPERATURE OF 60°F.

IMPURITIES 0.28 Mol % 0 Mol % 0 Mol % N/A ng / Nm3 N/A mg / Nm3 N/A mg / Nm3 N/A mg / Nm3 N/A mg / Nm3 -160.2 °C -128.5 °C 1166 mbar 459.080 kg / m3 54.44 MJ / kg 1115 BTU / SCF 1411 BTU / SCF

2. QUANTITY VESSEL VOLUME ON ARRIVAL

( OPENING CUSTODY TRANSFER )

404.978 CUBIC METERS

VESSEL VOLUME ON DEPARTURE

( CLOSING CUSTODY TRANSFER )

136,292.944 CUBIC METERS

VESSEL VOLUME DELIVERED ADJUSTED MASS DELIVERED

( ROUNDED AS PER THE S.P.A. )

GROSS QUANTITY DELIVERED QUANTITY DISPLACED QUANTITY CONSUMED BY VESSEL QUANTITY FOR GAS-UP QUANTITY FOR COOL DOWN ADJUSTED QUANTITY DELIVERED

MEGAJOULES 3,395,719,322 11,743,022 0 0 0 3,383,978,343

135,888.000 CUBIC METERS 62,172.077 METRIC TONS MMBTU KILOWATT HOURS 3,218,508 943,255,367 11,130 3,261,951 0 0 0 0 0 0 3,207,380 939,993,417

3. STATEMENT OF FACTS DATE 13-Apr-2008 13-Apr-2008 14-Apr-2008

HOUR 11:30 11:30 02:36

EVENT END OF SEA PASSAGE NOTICE OF READINESS TENDERED PILOT ON BOARD

14-Apr-2008

06:42

VESSEL ALL FAST

14-Apr-2008

06:42

NOTICE OF READINESS ACCEPTED

14-Apr-2008

08:12

CARGO ARMS CONNECTED

14-Apr-2008

09:00

COMMENCED CARGO OPERATIONS

15-Apr-2008

00:18

COMPLETED CARGO OPERATIONS

15-Apr-2008 15-Apr-2008

00:48 02:54

CARGO ARMS DISCONNECTED VESSEL DEPARTURE

4. ADDITIONAL INFORMATION AND COMMENTS

Mohamed-Hamid BOUABDELLI FOR INTERTEK CALEB BRETT CSR 3 - BP Certificate of Loading

LNG-LD-009H1 (07-AUG-09) - 14

LOADING REPORT

CAPTION TELEX TREATMENT DATE :

5/5/2009

TANKER NAME :

SK SPLENDOR

CAPITAL

SUR, OMAN

(NO COUNTRY ex : Idku)

OF039/09-SL100-KG

CAPITAL

PORT :

CARGO REFERENCE NUMBER :

DD/MM/YYYY

1.QUALITY: ----------

INPUT CELLS FORMS AAAAAA TO BE ADJUSTED (drop-down list) (depending on operation, reference temperature...)

VOLUMETRIC/METERING REFERENCE TEMPERATURE (for calculations) : COMBUSTION REFERENCE TEMPERATURE (for calculations) : REFERENCE PRESSURE :

LNG CARGO COMPOSITION MESURED ON OPERATION

60 60 14.7

PSIA

459.080

KG/M3 (GNL)

1166

mbar

-128.5

°C

COMPONENTS METHANE : ETHANE : PROPANE : ISOBUTANE : NORMAL BUTANE : ISOPENTANE : NORMAL PENTANE : NORMAL HEXANE : NITROGEN : CARBON DIOXIDE : MERCURY : HYDROGEN SULFIDE : MERCAPTAN : TOTAL SULFUR :

90.24 5.95 2.24 0.69 0.58 0.02 0 0 0.28 0

AVERAGE TEMPERATURE OF LNG DELIVERED :

-160.2

UNIT % % % % % % % % % % ng / Nm3 mg / Nm3 mg / Nm3 mg / Nm3 LNG DENSITY (@ observed Temp) : °C

LNG GROSS CALORIFIC VALUE (MASS) :

54.44

MJ / kg (@15°C)

VAPOUR GROSS CALORIFIC VALUE (VOLUME) :

1115

BTU / SCF (@60/60°F)

WOBBE INDEX :

1411

BTU / SCF (@60/60°F)

404.978 136,292.944 135,888.000 62,172,077 62,172,077 3,207,380

UNIT M3 (GNL) M3 (GNL) M3 (GNL) KG KG MMBTU (@60°F)

11,130

MMBTU (@60°F)

VAPOUR AVERAGE PRESSURE : VAPOUR AVERAGE TEMPERATURE :

2.QUANTITY : ---------INSPECTOR FIGURES ( WITHOUT COOLING DOWN AND GASSING UP IF ANY) VOLUME BEFORE OPERATION : VOLUME AFTER OPERATION : TOTAL VOLUME DELIVERED : GROSS MASS DELIVERED : NET MASS DELIVERED (less gas return & ship consumption) : TOTAL ENERGY DELIVERED (less gas return & ship consumption) : ENERGY OF GAS RETURN :

3.STATEMENT OF FACTS : -----------------END OF SEA PASSAGE : ARRIVAL AT ANCHOR AREA : PILOT ON BOARD : BERTHING COMPLETED : NOTICE OF READINESS TENDERED : NOTICE OF READINESS RECEIVED : OPEN CUSTODY TRANSFER COMPLETED : OPERATION COMMENCED (1rst pump) : OPERATION COMPLETED : CLOSING CUSTODY TRANSFER COMPLETED : DOCUMENTS ON BOARD : VESSEL DEPARTURE : ETA NEXT PORT : NEXT PORT CALL :

5/5/2009 2:30 5/5/2009 2:30 5/5/2009 2:30 5/5/2009 2:30 5/5/2009 2:30 5/5/2009 2:30 5/5/2009 2:30 5/5/2009 2:30 5/5/2009 2:30 5/5/2009 2:30 5/5/2009 2:30 5/5/2009 2:30 5/5/2009 2:30 BONNY ISLAND, NIGERIA

4.OBSERVATIONS : ----------Delay before berthing / Delay before loading / Stops during loading / etc...

DD/MM/YY HH:MM DD/MM/YY HH:MM DD/MM/YY HH:MM DD/MM/YY HH:MM DD/MM/YY HH:MM DD/MM/YY HH:MM DD/MM/YY HH:MM DD/MM/YY HH:MM DD/MM/YY HH:MM DD/MM/YY HH:MM DD/MM/YY HH:MM DD/MM/YY HH:MM DD/MM/YY HH:MM (NO COUNTRY ex : MONTOIR)

COOLING DOWN + GASSING UP QUANTITY IF APPLICABLE VOLUME : ENERGY USED : (COOLING DOWN + GASSING UP)

0.000 0

UNIT M3 (GNL) MMBTU (@60°F)

OUR REF

: SUR/09/134

YOUR REF : OF039/09-SL100-KG

SAILING SUMMARY REPORT VESSEL : SK SPLENDOR TERMINAL/PORT : OMAN LNG / SUR, OMAN 1. TIME LOG DATE 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 11-May-2009 12-May-2009 12-May-2009 12-May-2009 12-May-2009 12-May-2009 12-May-2009 12-May-2009

HOUR 06:30 07:00 08:15 08:45 08:45 09:00 09:05 09:10 09:35 10:40 10:45 10:54 11:05 12:12 20:13 20:23 20:33 22:20 09:20 09:46 10:53 11:10 11:54 13:15 13:45

2. QUALITY COMPONENTS METHANE ETHANE PROPANE ISO BUTANE N-BUTANE ISO PENTANE N-PENTANE & HEAVIER NITROGEN CARBON DIOXIDE HYDROGEN SULFIDE TOTAL SULFUR

DATE

EVENT VESSEL END OF SEA PASSAGE PILOT ON BOARD FIRST LINE ASHORE NOTICE OF READINESS TENDERED VESSEL ALL FAST COMMENCED PRE-LOAD KEY / SAFETY MEETING BETWEEN VESSEL & TERMINAL COMMENCED CONNECTION OF CARGO & VAPOR ARMS NOTICE OF READINESS ACCEPTED COMPLETED CONNECTION OF CARGO & VAPOR ARMS COMPLETED PRE-LOAD KEY / SAFETY MEETING BETWEEN VESSEL & TERMINAL COMPLETED TESTING OF E.S.D. (WARM CONDITION) COMPLETED OPENING CUSTODY TRANSFER INSPECTION COMPLETED OPENING CUSTODY TRANSFER CALCULATIONS COMMENCED COOL DOWN OPERATIONS OF CARGO ARMS & SHIP'S TANKS COMPLETED COOL DOWN OPERATIONS OF CARGO ARMS & SHIP'S TANKS COMPLETED TESTING OF E.S.D. (COLD CONDITION) COMMENCED LOADING OF CARGO VESSEL REACHED FULL LOADING RATE VESSEL COMMENCED REDUCTION OF LOADING RATE COMPLETED LOADING OF CARGO COMPLETED CLOSING CUSTODY TRANSFER INSPECTION COMPLETED CLOSING CUSTODY TRANSFER CALCULATIONS COMPLETED DISCONNECTION OF CARGO & VAPOR ARMS DOCUMENTS ON BOARD DOCUMENTATION COMPLETED

METHOD GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261 GPA 2261

SPA SPECIFICATIONS NOT LESS THAN 85 % NOT MORE THAN 8 % NOT MORE THAN 3 %

RESULTS UNITS 90.24 mol % 5.95 mol % 2.24 mol % 0.69 mol % 0.58 mol % 0.02 mol % 0.00 mol % 0.28 mol % 0.00 mol % N/A mg / Nm3 N/A mg / Nm3

NOT MORE THAN 2 %

NOT MORE THAN 1 % NOT MORE THAN 5 mg / Nm3 NOT MORE THAN 30 mg / Nm3

3. QUANTITY LIQUID LNG VOLUME ON BOARD BEFORE LOADING LIQUID LNG VOLUME ON BOARD AFTER LOADING LIQUID LNG VOLUME LOADED LNG DENSITY AT -160.2 °C GROSS CALORIFIC VALUE (VOLUME) AVERAGE TEMPERATURE OF LIQUID AFTER LOADING MASS DELIVERED (Liquid Delivered - Vapor Return + Consumed as Fuel) QUANTITY DELIVERED (Liquid Delivered - Vapor Return + Consumed as Fuel) GAS-UP QUANTITY COOL DOWN QUANTITY BEST REGARDS

: 12-May-2009

: : : : : : : : : :

404.978 136,292.944 135,888.000 459.080 1115 -160.2 62,172.077 3,207,380 0 0

CUBIC METERS CUBIC METERS CUBIC METERS kg / m3 BTU / SCF °C METRIC TONS MMBTU MMBTU MMBTU

PONNAPPA CHOKIRA CSR 5 - Chubu Sailing Summary Report

LNG-LD-009H1 (07-AUG-09) - 14