Fiber Optic Cable Pipeline Leak Detection Systems for Arctic & Cold Region Applications



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Fiber Optic Cable Pipeline Leak Detection Systems for Arctic & Cold Region Applications Prem Thodi, Mike Paulin, Duane DeGeer & Craig Young INTECSEA November 18-19, 2014

Outline Who we are Experience with Arctic leak detection systems Arctic pipeline leak detection challenges Fiber Optic Cable DTS and DAS Principles of operation Key technology gaps Arctic Leak Detection JIP Summary 2

Introduction Significant undiscovered oil & gas reserves remain in the Arctic Demand for oil and gas will continue to drive Arctic development Unique Arctic environment presents technical challenges Reliable Arctic operational strategies are needed to reduce risk Rapid and reliable leak detection is an important aspect of safe and economic hydrocarbon development in offshore Arctic/cold regions 3

Offshore Arctic Leak Detection Pipeline Leak Detection Systems Conventional flow-based pipeline monitoring systems (mass balance, transient pressure wave, acoustic detection) Airborne and marine surveillance Leak detection procedures under winter sea ice External monitoring systems (FO cables, LEOS, point source monitors) Remote sensing systems (airborne infra-red, radar, satellite, visual, smell) Other systems based on pipeline configuration Preferred Subsea Leak Detection System Features Continuous operation Rapid detection of sub-1% leaks Independent of flow conditions Cost-effective, constructible & installable Minimal false alarms Long (>15 miles) pipeline coverage without intermediate power requirements Installable in Arctic conditions Proven performance in Arctic conditions

Arctic Pipeline Leakage Potential Causes & Consequences Causes Unique Loading Conditions Buried Pipelines High bending strains High differential Temperature Ice gouging, thaw settlement, strudel scour, etc. Pipeline connections, valves, fittings, etc. Structural degradation Corrosion, erosion Fatigue cracking Other issues Span, VIV, buckling, rupture Consequences Safety Environmental Economical Negative reputation Exacerbated by remoteness Structural Degradation - Corrosion 5 Compressive pipe buckle failure

INTECSEA Experience with Leak Detection Systems Beaufort Sea Pipeline Projects: BPXA Northstar (installed 2000) Oil Transmission lines: Mass Balance, Pressure Balance, LEOS Gas transmission lines: Mass balance, Pressure Balance Pioneer Oooguruk (installed 2007) 3 Phase Production flowline: Pressure Balance, PIP annulus monitoring Water injection flowline: Mass Balance, Pressure Balance Gas Injection Flowline: Mass Balance, Pressure Balance Seabed erosion: Distributed temperature sensing (DTS) Eni Nikaitchuq (installed 2009) 3 Phase Production flowline: PIP annulus monitoring, PSL Water injection flowline: Mass Balance, Pressure Balance Gas Injection Flowline: Mass Balance, Pressure Balance Seabed erosion: Distributed temperature sensing (DTS) 6

Arctic Leak Detection Challenges Buried pipelines conveying multiphase flows Seasonal ice cover Installation and maintenance challenges Subsea equipment and power requirements Uncertain minimum thresholds of detection for buried lines Remote maintenance, performance monitoring and control Potential for false alarms Background noise reduction Uncertain operational reliability in Arctic Temperature and slack line issues 7

Fiber Optic Cable Distributed Sensing Systems Distributed Temperature Sensing (DTS) Oil leakage leads to local rise in temperature Gas leakage leads to local cooling Raman band systems Brillouin band systems FOC itself acts as the sensor and data link Distributed Acoustic Sensing (DAS) Acts as a hydrophone Captures acoustic signature (i.e. vibration) generated by leaking fluid Signal/frequency separation Rayleigh band systems No need to contact fluid with FOC sensors 8

Principles of Operation When a short pulse of light is emitted, a proportion of the outgoing signal is scattered back to source due to impurities or defects in fiber microstructure Distributed Temperature Sensing Distributed Acoustic Sensing Raman DTS System Backscatter signal intensitybased system Measures local change in temperature Brillouin DTS System Converts temperature effects on cable into frequency shifts of backscattered light Insensitive to the fiber attenuation changes over time and distance Rayleigh DAS Measures minute strain effects on sensor Strain is caused by acoustic vibrations Acoustic waves modulates the backscattered signal. Cable pick up the acoustic signals, and when a distinguishable signature is detected, an alarm is triggered 9

FOC Distributed Sensing Leak Detection System Components Typical DTS Cable 1. HDPE outer sheath 2. Galfan high strength steel wire 3. Gel-filled metal loose tube SS 316L 4. Bend insensitive optical fibers Typical DAS Cable 1. PA Outer sheath 2. Stainless steel 316 L metal tube 3. Inner interlocking system 4. Multilayer acoustic coupling layer 5. Bend insensitive optical fiber 10

Technology Gaps False alarm reduction Reliability of systems Minimum thresholds of detection Long pipeline application Cable positioning Leak size quantification Technology readiness Few Arctic project applications Northstar Pipeline (BP Alaska) 11 Oooguruk Pipeline (Pioneer Natural Resources)

INTECSEA JIP Testing of Fiber Optic Cable Distributed Sensing Leak Detection Systems for Arctic and Cold Region Applications Managed by Petroleum Research Newfoundland Labrador (PRNL) Not-for-profit corporation that funds and facilitates collaborative R&D on behalf of Newfoundland and Labrador s offshore oil and gas industry. Lead by INTECSEA Governmental and Industry funding Phased Development Phase 1: finishing 2014 Phase 2: 2015-2016 (planned)

Introduction & Background No comprehensive full scale testing has been reported in the public domain for FOC subsea Arctic applications Purpose of this JIP is to help close the technology gap General Test Setup 13

JIP Objectives Test detectability limits Determine minimum thresholds of detection (leak rate and response time) Help advance the technology readiness level Simulate cold-region environmental testing Identify/quantify false alarm rate Phase 1 Objectives Planning, design and costing to establish the basis of the testing program (in Phase 2) Develop experiment setup, test matrix and procedure, Phase 2 test organization and execution plan, Cost and schedule This will allow Phase 2 to proceed with greater confidence in the execution, cost and schedule associated with the FOC LDS experiment program 14

Phase 1 Objectives Design Test Tank Design Overall Experimental Setup Planning Test Procedure Execution Plan Cost Develop Cost and Schedule for Phase 2 Phase 2 Testing

Definition of Physical Test Outline desired test parameters Particular consideration is given to testing of a long FOC length (40km), moderate test pipe length (20m) and a low ambient temperature (4 C / 1 C) Parameters Pipeline Length Water Depth (max/min) Pipeline OD Value 2m 20m 100m / 1500m (simulated) 12 (324mm) Concrete Weight Coating Thickness 25.4mm (1 ) Fluid Type (oil/gas) Pipeline Design Pressure Water and Nitrogen 5800psig Pipeline Operating Temperature 0 to 50 C Ambient Temperature Burial 4 C (with potential of testing 1 C) Non-buried and 1m burial cases 16

Test Hierarchy & Procedure Testing hierarchy: Liquid Temp Pressure Leak Size Gas Pressure Temp Leak Size 17 Test procedure: Installation of test setup Insulation/isolation Soil preparation Test matrix (varying pressure, temperature, leak size) Test procedure, monitoring and control equipment HSE considerations

Test Facility Selection 18 Study was completed on potential test facilities/space selections. Study Methodology: Facility identification (within JIP project area) Selection criteria (size, cost, boundary effects) Identify required modifications (i.e. insulation to minimize boundary effects) Facility ranking Identified 2 facilities Facility 1: Requires purpose built tank (allows testing of 2m long pipeline segment) Facility 2: Existing tank (allows testing of 18-19m long pipeline segment)

Test Tank Tank sizing based on the following: Acoustic boundaries requirements Leak simulation (i.e. appropriate sizing of pressure rated tubing) Burial / non-burial test conditions Required instrumentation and control based on fluid type Proposed system is able to control: Pressure Flowrate Temperature Leak size CFD Model - Acoustic Contours of Pipeline Leak 19

Test Facility Selection C-CORE Requires purpose built tank Can test 2m long test pipe Foxtrap Existing tank Can test 18-19m long pipe 20

FOC Vendor Screening Study Vendor Identification 14 vendors were identified Outlined Required System Criteria Water depth, fluid type, pipeline length, etc. Literature Review Through internet search and past project experience Questionnaire provided to vendors Level I Screening Determine relevancy to JIP Level II Screening Investigation of system performance 21

FOC Positioning & Geotech Study 22 Determine optimal positions to ensure baseline for detection performance can be achieved, as well as detection envelopes can be established Positioning based on: Leak conditions Buried/non-buried, gas/water leak Vendor recommendations Testbed Geotechnical Evaluation Identify appropriate soil material, density and saturation requirements, and soil placement/replacement strategy Identify testbed material as representative of Arctic and cold region soil conditions Identify potential local vendors

Phase 2 Objectives Conduct detailed engineering and procurement Execute the leak detection test program Determine detectability and detection envelope of selected/leading DTS as well as DAS systems Further prove the technology (and enhance TRL or reduce TRC) for Arctic and cold region applications Perform system installation, maintenance and repair requirement assessment Evaluate system reliability and false alarm rate Recommend proven systems (DTS/DAS) for field test and/or pilot project implementation 23

Novelties Long cable (up to 40 km) Low ambient temperature (as low as 4 C / 1 C) Large test tank (20m x 10m x 2.5m) Accommodation of boundary conditions Buried pipeline Integrated (DTS/DAS) leak testing Small chronic leak detection capability testing Replicate coated conditions Concrete vs. bare pipe 24

Contacts Prem Thodi: Premkumar.Thodi@intecsea.com Mike Paulin: Mike.Paulin@intecsea.com Duane DeGeer: Duane.DeGeer@intecsea.com Craig Young: Craig.Young@intecsea.com