Variation of Pipeline Licence WA-32-PL (Scarborough Export Trunkline) (2NKNS6)

Administered by Department of Industry, Science and Resources

Legislation au C2026G00427 In force Gazette

Legislation content

 

COMMONWEALTH OF AUSTRALIA

 

Sections 226 and 708

Offshore Petroleum and Greenhouse Gas Storage Act 2006

 

VARIATION OF PIPELINE LICENCE WA-32-PL

(SCARBOROUGH EXPORT TRUNKLINE) (2NKNS6)

 

I, STEVEN ROBERT TAYLOR, the Delegate of the National Offshore Petroleum Titles Administrator, on behalf of the Commonwealth-Western Australia Offshore Petroleum Joint Authority hereby vary Pipeline Licence WA-32-PL, dated 20 April 2022 (the Licence), for which:

 

Woodside Energy Scarborough Pty Ltd

(ACN 650 177 227)

JERA Scarborough Pty Ltd

(ACN 674 641 206)

LJ Scarborough Pty Ltd

(ACN 670 113 327)

Woodside Energy (Australia) Pty Ltd

(ACN 006 923 879)

 

are the registered titleholders, as set out below.

 

The variation takes effect on the day on which this notice of variation is published in the Australian Government Gazette.

 

Made under the Offshore Petroleum and Greenhouse Gas Storage Act 2006
of the Commonwealth of Australia

 

 

 

STEVEN ROBERT TAYLOR

DELEGATE OF THE TITLES ADMINISTRATOR

ON BEHALF OF THE COMMONWEALTH-WESTERN AUSTRALIA
OFFSHORE PETROLEUM JOINT AUTHORITY

 

 

 

 

 

 

 

 

 

VARIATION OF

PIPELINE LICENCE WA-32-PL

  1.       The ROUTE OF THE PIPELINE Licence is varied by deleting the current text and replacing it with the following:

ROUTE OF THE PIPELINE

The pipeline route is described in the table hereunder and displayed in the attached map (Attachment 1), commencing at the Export Riser Base Manifold downstream connector point to the boundary of the offshore area of Western Australia with State Waters within a corridor of 100 m (± 50 m centred on the pipeline). Coordinates are based on Geodetic Datum of Australia (GDA94).

Feature Name

KP

Easting

(mE)

Northing

(mN)

Bend Radius

(m)

Export riser base manifold (RBM) spool tie-in flange

N/A

105 661.73

7 793 914.40

 

Pipeline end termination (PLET) spool tie-in (connector hub face)

433.06

105 628.36

7 793 940.43

 

PLET 32" Ball valve

433.052

105 629.50

7 793 950.03

 

Turning point 35 end

431.133

106 093.49

7 795 804.34

2500

Turning point 35 start

429.216

107 191.58

7 797 317.87

Turning point 34 end

426.199

109 748.37

7 798 920.33

2500

Turning point 34 start

424.416

111 458.06

7 799 272.63

Turning point 33 end

383.338

152 052.96

7 792 995.56

5000

Turning point 33 start

382.44

152 923.34

7 792 779.59

Turning point 32 end

355.933

177 974.12

7 784 114.78

5000

Turning point 32 start

352.427

181 408.49

7 784 175.38

Hot-tap tee assembly 1 (HTTA-1)

346.077

187 332.71

7 786 461.61

 

Turning point 31 end

327.539

204 627.49

7 793 135.05

5000

Turning point 31 start

325.591

206 264.93

7 794 168.84

Turning point 30 end

300.291

224 637.26

7 811 562.04

5000

Turning point 30 start

295.288

229 275.86

7 812 784.66

Turning point 29 end

289.593

234 804.32

7 811 416.50

5000

Turning point 29 start

286.045

238 256.52

7 811 805.47

Turning point 28 end

276.346

246 916.97

7 816 172.07

5000

Turning point 28 start

274.936

248 070.50

7 816 974.87

Turning point 27 end

273.055

249 447.88

7 818 255.51

5000

Turning point 27 start

267.461

254 659.28

7 819 255.83

Hot-tap tee assembly 2 (HTTA-2)

259.247

262 319.27

7 816 289.27

 

Turning point 26 end

240.613

279 693.15

7 809 553.93

5000

Turning point 26 start

238.012

282 249.27

7 809 272.52

Turning point 25 end

228.208

291 942.36

7 810 741.73

5000

Turning point 25 start

224.016

295 866.67

7 809 660.75

Turning point 24 end

216.961

301 316.58

7 805 180.95

4000

Turning point 24 start

216.771

301 461.07

7 805 056.28

Turning point 23 end

216.431

301 713.02

7 804 828.19

4000

Turning point 23 start

216.045

302 011.22

7 804 583.35

Turning point 22 end

215.407

302 523.07

7 804 202.87

4000

Turning point 22 start

215.27

302 631.80

7 804 119.11

Turning point 21 end

214.034

303 597.66

7 803 348.31

4000

Turning point 21 start

213.677

303 886.34

7 803 138.32

Crossing at Pyxis flowline

212.250

305 077.91

7 802 350.46

 

Crossing at Pyxis umbilical

212.242

305 082.74

7 802 347.30

 

End of slope crossing excavation

208.930

307 846.47

7 800 520.19

 

Start of slope crossing excavation

208.821

307 936.47

7 800 459.44

 

Turning point 20 end

202.954

312 830.32

7 797 223.77

5000

Turning point 20 start

200.212

314 600.24

7 795 174.14

In-line tee assembly (ILTA)

200.028

314 680.42

7 795 008.93

 

36" to 32" transition

199.987

314 697.95

7 794 971.16

 

Crossing at Pluto MEG flowline

194.577

316 991.41

7 790 072.04

 

Crossing at Pluto flowline B

194.513

317 018.05

7 790 014.02

 

Crossing at Pluto flowline A

194.456

317 041.78

7 789 962.10

 

Crossing at Pluto umbilical

194.397

317 066.49

7 789 908.01

 

Crossing at Brunello flowline

192.512

317 866.57

7 788 201.72

 

Crossing at Julimar flowline

192.466

317 886.33

7 788 159.65

 

Crossing at Julimar Brunello MEG pipeline

192.355

317 933.29

7 788 059.24

 

Crossing at Julimar Brunello umbilical A

192.291

317 960.54

7 788 000.92

 

Crossing at Wheatstone pipeline

190.732

318 621.94

7 786 589.79

 

Turning point 19 end

186.813

320 283.75

7 783 040.80

2000

Turning point 19 start

184.528

322 114.29

7 781 889.27

Turning point 18 end

176.312

330 330.48

7 781 968.91

5000

Turning point 18 start

175.367

331 270.55

7 781 889.00

Turning point 17 end

172.014

334 569.78

7 781 291.10

5000

Turning point 17 start

170.513

336 064.64

7 781 247.48

Turning point 16 end

161.779

344 735.18

7 782 301.29

5000

Turning point 16 start

160.053

346 449.42

7 782 212.82

Crossing at Fibre Optic Cable 2

149.765

356 480.22

7 779 928.02

 

Crossing at Fibre Optic Cable 1

136.415

369 496.62

7 776 961.00

 

Turning point 15 end

119.068

386 410.79

7 773 105.84

5000

Turning point 15 start

117.922

387 488.61

7 772 726.29

Turning point 14 end

110.923

393 781.99

7 769 662.09

5000

Turning point 14 start

108.633

395 995.19

7 769 157.61

Turning point 13 end

101.63

402 998.05

7 769 191.78

5000

Turning point 13 start

100.73

403 893.75

7 769 115.33

Turning point 12 end

77.867

426 406.60

7 765 131.24

5000

Turning point 12 start

77.104

427 144.73

7 764 941.63

Crossing at Reindeer pipeline

74.919

429 213.26

7 764 239.04

 

Turning point 11 end

51.649

451 245.18

7 756 747.90

5000

Turning point 11 start

51.153

451 721.82

7 756 611.80

Turning point 10 end

38.629

463 920.25

7 753 774.35

5000

Turning point 10 start

35.758

466 383.90

7 752 377.92

Boundary of the offshore area of Western Australia with State Waters

32.036

468 969.16

7 749 700.58

 

 

  1.       The SCARBOROUGH EXPORT TRUNKLINE ROUTE map is deleted and replaced with the map at Attachment 1.

 

  1.       The SPECIFICATIONS of the Licence remains unchanged.

 

SPECIFICATIONS

 

Design and Construction

 

The offshore pipeline must be designed and constructed in accordance with Offshore Standard DNVGL-ST-Fl0l – Submarine Pipeline Systems (Offshore Pipeline), which is incorporated in its entirety in Australian Standard AS2885.4 – Pipelines, Gas and Liquid Petroleum (Part 4: Submarine Pipelines). Specifically, the design and construction phase of the pipeline must comply with DNVGL-ST-Fl0l.

 

Basis of Design

 

The pipeline design is based on the following parameters:

Item

Item Description

Details and units

1

Outside diameter (OD) of pipe

Section

OD [mm]

Nominal OD [in]

KP 32.036 to 33.1

925.4

36

KP 33.1 to 200

924.8

KP 200 to 204

814.6

32

KP 204 to 213

838.0

KP 213 to 324

827.6

KP 324 to 433.053

823.2

Buckle Arrestors

890.0

Structures Piping Header

838.0

Tee Branch

406.4

16

Spool line pipe

826.8

32

Spool bends

837.8

2

Wall thickness of pipe (all materials)

Section

Thickness [mm]

KP 32.036 to 33.1

30.7

KP 33.1 to 200

30.4

KP 200 to 204

27.3

KP 204 to 213

39.0

KP 213 to 324

33.8

KP 324 to 433.053

31.6

Buckle Arrestors

65.0

Structures Piping Header

39.0

Tee Branch

30.0

Spool line pipe

33.4

Spool bends

38.9

3

Length

Approximate length in Commonwealth waters:

401 km (KP 32.036 – KP 433.053)

4

Design Life

Minimum 25 years

5

Pipeline Material

Carbon Steel

6

Pipeline Steel Grade

DNVGL-ST-F101 Grade 450 DFU

7

Protective coating

External corrosion coating is either 3.5 mm three layer polypropylene or 6.0 mm bituminous enamel with concrete weight coating (40 mm – 110 mm).

Tie-in spool between the riser base manifold and pipeline end termination has ultra-high build epoxy external coating.

8

Corrosion allowances

Internal: 1.0 mm

External: None (0 mm)

9

Pipeline Specification

DNVGL-ST-F101: SAWL 450 DFU

10

Minimum yield strength of pipe steel

450 MPa

11

Maximum Allowable Operating Pressure

23 MPa(a) at platform export discharge at 30 m above mean sea level

12

Design Capacity

1,750 MMscf/d

13

Inlet and outlet facilities

Inlet: Riser base manifold

Outlet: N/A (Pipeline transitions into state waters)

14

Fitting, valve and flange specifications

Fittings

-          32-inch x 16-inch reducing tee (3 off), DNVGL-ST-F101, ASME VIII, DNVGL-RP-0034.

-          36-inch x 32-inch concentric transition forging (1 off), DNVGL-ST-F101, DNVGL-RP-0034.

Diverless Connectors

-          32-inch horizontal connector (2 off), DNVGL-ST-F101, API 6A/ISO 10423, API 17D/ISO 13628-4.

-          16-inch horizontal connector (1 off), DNVGL-ST-F101, API 6A/ISO 10423, API 17D/ISO 13628-4

Valves

-          32-inch ROV operated subsea valve for PLET (1 off), DNVGL-ST-F101, ISO 14723.

-          16-inch ROV operated subsea valve for Tee (2 off), DNVGL-ST-F101, ISO 14723

-          Small bore bleed assemblies (2 off), DNVGL-ST-F101, ISO 14723

15

Compressor stations

No compressor stations

16

Maximum Design Temperature

60.0 °C

17

Minimum Design Temperature

-10 °C

18

Characteristics of substance proposed to be conveyed

Dry gas

19

General plans and descriptions of pump stations, tank stations or valve stations and their equipment

The riser base manifold collects export gas via three flexible risers. A 32-inch tie-in spool connects the riser base manifold to the pipeline end termination.

The pipeline end termination is on the end of the 32-inch section at KP 433.053.

Between the pipeline end termination and KP 200 the pipeline has two hot tap tee assemblies and a single in-line tee assembly.

At KP 200, the pipeline transitions to 36-inch diameter.

Between KP 200 and the state water boundary at KP 32.036 there are no facilities.

20

General plans and description of pigging facilities

Temporary subsea pig launcher/receiver connected to the Export Riser Base Manifold using a diverless connector and a permanent pig receiver onshore at the Pluto LNG plant site.

21

Cathodic Protection

A sacrificial cathodic protection system consisting of full bracelet anodes (Al-Zn-In Alloy) that are strapped and electrically connected to the pipeline.

Anode spacing varies between 73.2 m and 292.8 m with an approximate total quantity of 3,129 anodes.

Cathodic protection of structures consists of sacrificial stand off anodes (Al-Zn-In Alloy) installed on the structure members. The tie-in spool will be protected by anodes placed on the riser base manifold structure.

22

Hydrate Management

Dehydrating and hydrocarbon dew-pointing the export gas.

 

 

ATTACHMENT 1

SCARBOROUGH EXPORT TRUNKLINE ROUTE

Interactions

Authorises

All Versions

Sourced from the Federal Register of Legislation at 26 August 2026. For the latest information on Australian Government law please go to https://www.legislation.gov.au.