A0T8Z2 - BRC Ring Border Manual
A0T8Z2 - BRC Ring Border Manual
Pipeline
Operating & Maintenance
Manual
Pipeline Operating &
Maintenance Manual
Revision: 2.0 December 2005
TABLE OF CONTENTS
Revision List ..........................................................................................................ii
1.0 Introduction
1.1. Purpose ..................................................................................................... 1
1.2. Scope......................................................................................................... 1
1.3. Document Control and Revision ................................................................ 2
1.4. Roles and Responsibilities......................................................................... 2
2.0 Pipeline Inventory, Records and Maps ................................................................. 3
2.1. Introduction ................................................................................................ 3
2.2. Pipeline Inventory Management ................................................................ 3
3.0 Pipeline Operating & Maintenance ....................................................................... 4
3.1. Pipeline Commissioning............................................................................. 4
3.2. Pipeline Suspension .................................................................................. 4
3.3. Pipeline Deactivation ................................................................................. 5
3.4. Pipeline Abandonment............................................................................... 5
3.5. Leak Detection........................................................................................... 5
3.6. Signage...................................................................................................... 6
3.7. Incident Reporting...................................................................................... 6
3.8. Ground Disturbance................................................................................... 6
3.9. Pipeline Repairs......................................................................................... 6
3.10. Isolation Valve Maintenance ...................................................................... 7
3.11. Pressure Protection Device Maintenance .................................................. 7
3.12. ROW Surveillance ..................................................................................... 7
3.13. Internal Corrosion Control.......................................................................... 8
3.14. External Corrosion Control......................................................................... 8
3.15. Pipeline Monitoring & Inspection................................................................ 8
3.16. Pressure Testing........................................................................................ 9
Appendices
A General Attachments
A.1 Pipeline Commissioning Procedure
A.1.1 Start-up and Shut-down of Lined Pipelines
A.2 Pipeline Decommissioning Procedure
A.3 Site Specific (i.e. liner vents – omit if not applicable)
B Site Specific Attachments
B.1 Pipeline Flow Schematic
B.2 Pipeline Inventory Summary
B.2.1 Active Pipeline Summary
B.2.2 Inactive Pipeline Status Log
B.2.3 Ring Border – NEB Pipeline Summary
B.3 Protective Device Summary
B.3.1 Isolation Valve Summary
B.3.2 Pressure Protection Device Summary
B.4 Integrity Management Plan
B.4.1 Chemical Inhibition Program
B.4.2 Pipeline Assessment Report
B.5 Operations & Maintenance Task List
REVISION INDEX
Burlington
Rev. # Date Sections Revised
Approval
0 Dec 2003 Initial draft AWH
1.0 Oct 2005 All – EUB pipeline Regs Update AWH
2.0 Dec 2005 All – AB and BC manuals combined AWH
Added Pipeline Decommissioning form
2.1 Jan 2006 AWH
to Appendix A2
1.0 INTRODUCTION
1.1 PURPOSE
The purpose of this Manual is to provide direction and understanding of responsibility to
Burlington’s operations personnel regarding pipeline operation and maintenance. The
Manual is to be used in conjunction with the most recent editions of Burlington’s
Environment, Health & Safety Handbook and the North Region Emergency Response
Plan.
It is the intention of this Manual to in part describe the procedures required to maintain
the integrity of the facilities for as long as it is in operation. Any reviews and revisions to
this Manual will be initiated by Operations leadership or engineering personnel, as
dictated by significant changes in production parameters, results of condition monitoring
or other such items that are addressed within. As a minimum, the corrosion protection
and monitoring of this system shall be reviewed and adjusted at a frequency of not less
than 5 years.
This document satisfies the Alberta Pipeline Regulation’s, Section 7, BC OGC Pipeline
Regulation section 6(d), and the NEB Onshore Pipeline Regulation’s, Part 6 paragraph
27, requirement for an Operations and Maintenance manual.
The Manual contains and/or provides references to Burlington procedures for various
operating activities.
A summary of operating and maintenance tasks is provided in a table in Appendix B.4 of
this Manual.
1.2 SCOPE
This Manual contains guidelines and procedures for the integrity management of existing
pipelines within the scope of the following provincial jurisdictions:
• British Columbia Oil and Gas Commission (OGC)
• Canadian Standards Association CSA Z662
• Alberta Energy and Utilities Board (AEUB)
• National Energy Board
The specified Burlington owned pipelines included in the scope of this manual are listed
in Appendix B.2.
Excluded from the Manual are:
• Unlicensed pipelines on lease, and
• Unlicensed buried utility lines for sanitary service and fresh water.
This Manual does not specifically address the quality control requirements for the design
and construction of pipelines.
Documentation of these activities must be kept on file and available upon request. Refer
to audit requirements Directive 56 Schedule 1.The BC Oil and Gas Commission will not
grant leave to abandon a pipeline, unless the line is removed in its entirety and the land
restored. (OGC Pipeline Information Bulletin No. 31, January 23, 1997)
Pipelines are to be maintained at a Deactivated level (refer to section 3.4).
3.5 Leak Detection
Operating companies are required to make periodic line balance measurements for
system integrity. Where existing technology for measuring and balancing multiphase
systems is limited or impractical, alternative techniques should be used. Installed
devices or operating practices, or both, are to be capable of early detection of leaks.
(CSA Z662 Clause 10.2.6)
Leak detection of pipelines in the facility can be achieved through several methods.
Methods that should be considered include, but are not limited to the following:
¾ Production accounting material balances.
¾ Visual inspection of Right of Ways (ROW Surveillance),
¾ Investigation of 3rd party reports,
¾ Changes in chart recorder data,
¾ Low pressure alarms,
¾ Over the line flame ionisation surveys.
Personnel responsible for interpreting and responding to the leak detection system shall
be knowledgeable of the leak detection methods and the pipeline system.
Records of all leak detection activity must be maintained and made available to the
Regulator upon request.
3.6 Incident Reporting
In the event of a leak or break in a pipeline where product is released, operations will
take immediate steps to stop the source of release and contain and clean up the spill.
Following initial response, the operator will notify the BRCL site supervisor, and follow
the incident reporting guidelines as established in the “Environment, Health & Safety
Handbook; Incident Notification and Reporting”.
The OGC is to be notified (in the form or manner directed by the chief inspecting
engineer) of the occurrence of; (a) spillage of oil or gas or solids, (b) malfunction of or
damage to the pipeline, or (c) incidents likely to cause or contribute to spillage. The
cause, effect and remedy of these events are to be subsequently reported. (OGC
Pipeline Regulation section 22(1) and (2))
Please see Oil and Gas Commission web page (www.ogc.gov.bc.ca) for guidance with
reporting to the OGC and necessary Notification and Report forms.
3.7 Signage
Pipeline identification in the form of appropriate signage is required and shall be installed
and maintained at facility leases, road and railway rights-of-way, utility corridors,
subdivision developments, irrigation systems, and water crossings. (OGC Pipeline
Regulation section 18 and CSA Z662 Clause 10.2.8 and Alberta Pipeline Regulation
section 23)
Signs must conform to the size and content requirements as outlined in the Alberta
Pipeline Regulation section 68(2)(b), Schedule 1.
Sour pipeline facilities require signs warning of the possible presence of H2S and
advising about protective gear requirements. (OGC Sour Pipeline Regulation section
6(3))
Operations are responsible for the monitoring of sign condition and replacement should
they be removed, defaced or become illegible.
Operations will perform an annual survey of all signs to ensure they are in accordance
with the requirements of the regulations.
3.8 Ground Disturbance
All ground disturbance activities are to be carried out by qualified personnel in
accordance with the procedures outlined in the Environment, Health & Safety Handbook.
3.9 Pipeline Repairs
Pipeline repairs are an engineering function and as such shall be carried out using
approved procedures. Repairs shall follow engineered repair procedures in accordance
to current edition of CSA Z662.
In BC, prior to the commencement of an extension, alteration or repair of any pipeline or
a pressure component used or to be used in any pipeline, Burlington must file with the
chief inspecting engineer, in duplicate, all the pertinent data, specifications and
documented or other information he/she may require. Within 30 days of the completion
of the extension, alteration or repair a certificate, certifying that all work done and
materials used were in accordance with the data and specifications submitted, is to be
filed with the chief inspecting engineer. (OGC Pipeline Regulation section 11)
Failed sections of pipe shall be replaced with a section similar or equivalent to that of the
existing pipe. The wall thickness of the replacement section shall be equal or greater
(within transition limits) than that of the failed section.
Detailed drawings of the repair including precise locations are to be prepared and filed in
the pipeline file. All pressure test data and OGC submissions must also be maintained in
a pipeline file.
3.10 Isolation Valve Maintenance
Pipeline valves that might be required during and emergency shall be inspected and
partially operated at least once per calendar year, with a maximum interval of 18 months
• Establish appropriate pressure test limits so that the pressure test will not
adversely affect the integrity of the pipeline.
Before the testing of any pipeline, copies of all test procedures are to be submitted to the
Inspecting Engineer of the commission. (OGC Pipeline Regulation section 19(11))
Any leak occurring during a pressure test shall be reported to the OGC.
All pertinent data surrounding a pressure test must be recorded and made available to
the OGC.
Pressure tests shall be documented to adequately support the success of the tests.
Records of pressure tests that qualify piping for service, shall be retained in the
pipeline’s file throughout its useful life, and shall contain at least the following
information: (CSA Z662 Clause 8.6.1 and 8.6.2.4)
• Time and date of test,
• Pipe specifications,
• Elevation profile and location of test section where applicable,
• Pressure test medium used,
• Test pressure at lowest elevation,
• Test duration,
• Pressure and temperature recording charts, where applicable,
• Pressure volume chart where applicable, and
• Location of any leaks or failures and description of repair action taken.
APPENDIX A.1
Pipeline Commissioning
Procedure
APPENDIX A.2
Pipeline Decommissioning
Procedure
dd / mm / yyyy
Pipeline Data Shut-in Date: ___/___/_____ EUB License: __________________ - ____
Location (LSD): From - - - W M To - - - W M
The following three modes of decommissioning are consistent with the regulatory requirements.
Mode 1 – Suspension: A planned or unplanned period of inactivity (< 12 months), after which the
line will be returned to its original service. Ensure the following items are addressed, then date when complete:
Required Completed
Documentation (dd/mm/yyyy)
1 Purge, displace or pig production fluids to prevent hydrates, freezing, wax Daily Report
plugging, or corrosion depending on the nature of the fluids. / /
2 If the suspension is expected to be greater than 10 days for sour lines or Chemical supplier’s
30 days for sweet lines, batch inhibit as per the POMM. Batch Report / /
3 Isolate and reduce pressure (Leave positive pressure ~100 kPa). Daily Report
/ /
4 Lock-out and tag all connecting valves. Daily report / /
5 Document and file in the pipeline operation and maintenance records. Inactive pipeline log / /
Mode 2 – Discontinue: A planned shut down of normal pipeline operations usually because the
pipeline is no longer required for its original function. The line is normally considered an asset to be used for some
other function at a future unspecified date. Ensure the following items are addressed, then date when complete:
Required Completed
Documentation (dd/mm/yyyy)
1 Isolate and reduce pressure. Daily Report
/ /
2 Physically disconnect the line from all energy sources (operating facilities Daily Report
or pipelines). / /
3 Vent the pipeline to atmosphere or separator and flare with consideration Daily Report
given to H2S and EUB G60 requirements. Watch LEL levels and ignition
sources if venting to atmosphere.
Note: Confirm that communication with other pipelines does
not exist by monitoring pressure while venting. / /
4 If the pipeline does not have a pig launcher and receiver, install temporary Daily Report /
ones. Use a good cleaning pig (Consult pig supplier on appropriate style of contractor’s work report
pig.) and pig the pipeline with nitrogen, air(2) or fresh water(2). Capture all
fluids on the receiving end into a temporary tank until the pig is
recovered. Additional pig runs may be required to ensure the pipeline is
clean (1). / /
5 Purge the line with an inert and non-corrosive fluid (check only one): Daily report/
Inert gas (N2) contractor’s work report
Air with a filming inhibitor(2)
Fresh water with O2 scavenger and inhibitor(2)
Leave a positive pressure of approximately 100 kPa on the pipeline to
prevent air from entering. / /
6 Check all risers to ensure that all energy sources are disconnected or Daily report/
blinded. Install ½” or 1” ball valves to serve as test ports. contractor’s work report
Attach tags on all disconnected or blinded risers that provide the following
information:
Pipeline licensee
Licence and line number
Location(s) of other end points
Discontinuation date
Media left inside the pipeline
/ /
7 Maintain cathodic protection on pipeline. Annual CP survey
Reports / /
8 Complete and submit required G55 documents and submit to the EUB EUB Base map
within 90 days of completion (3). Guide 56 Schedule 1 / /
Guide 56 Schedule 3
Guide 56 Schedule 3.1
9 Compile all required documentation in a pipeline discontinuation report Discontinuation report
and file in the pipeline operation and maintenance records. Inactive pipeline log / /
Mode 3 – Abandon: A planned shutdown of pipeline operations usually because the pipeline is no
longer required or no longer able to function. The line is normally no longer considered an asset and no future
application is foreseeable. Ensure the following items are addressed, then date when complete:
Required Completed
Documentation (dd/mm/yyyy)
1 Isolate and reduce pressure. Daily Report
/ /
2 Physically disconnect the line from all energy sources (operating facilities Daily Report
or pipelines). / /
3 Vent the pipeline to atmosphere or separator and flare with consideration Daily Report
given to H2S and EUB G60 requirements. Watch LEL levels and ignition
sources if venting to atmosphere.
Note: Confirm that communication with other pipelines does not
exist by monitoring pressure while venting. / /
4 If the pipeline does not have a pig launcher and receiver, install temporary Daily Report /
ones. Use a good cleaning pig (Consult pig supplier on appropriate style of contractor’s work report
pig.) and pig the pipeline with nitrogen, air or fresh water. Capture all
fluids on the receiving end into a temporary tank until the pig is recovered.
Additional pig runs may be required to ensure the pipeline is clean (1). / /
5 Purge the line with nitrogen, air or fresh water (check only one): Daily report/
Inert gas (N2) contractor’s work report
Air
Fresh water
/ /
6 Cut all risers off below surface at pipeline level and cap, except when it is Daily report/
located within the boundaries of a facility that will continue to have other contractor’s work report
equipment operating.
Pipeline licensee
Licence and line number
Location(s) of other end points
Abandonment date
Media left inside the pipeline
/ /
7 Remove all cathodic protection. CP survey report / /
8 Complete and submit required G55 documents and submit to the EUB EUB Base map
within 90 days of completion (3). Guide 56 Schedule 1
Guide 56 Schedule 3
Guide 56 Schedule 3.1 / /
9 Compile all required documentation in a pipeline abandonment report and Abandonment report
file in the pipeline operation and maintenance records. Inactive pipeline log / /
(1) A detailed cleaning procedure, developed with the assistance of a chemical supplier, may be required to
thoroughly clean the pipeline.
(2) The use compressed air or fresh water for decommissioning a pipeline requires that a batch inhibitor be
applied between two batching pigs as a last step before the final purge. Consult with a chemical supplier for
assistance on designing an appropriate batch treatment.
(3) Assistance in this matter is available through the EHS group, specifically the Pipeline Engineering Integrity
Team (Allan Hobbins 780-539-3007, Northern Materials Engineering, 780-469-1164).
APPENDIX A.3
Premise These guidelines are intended to provide direction on how to prevent corrosion
damage in pipelines that are being brought into service or being temporarily
removed from service. This is not intended to include routine maintenance batch
inhibition treatments that are part of the corrosion mitigation program for the
pipeline.
It has been proven that a coating of a suitable corrosion inhibitor applied to a
pipeline before initial production will dramatically reduce the likelihood of corrosion
caused by detrimental flow conditions and the lack of protective scales, which may
exist during start-up. To this end it is expected that a batch treatment be applied
to a pipeline for the following situations:
• All new pipelines will be batch inhibited as one of the final steps in the
construction process,
• Sour lines that are to be shut-in for longer than 10 days, as part of the
shut-in activities,
• Sour lines that have been shut in for longer than 3 months or that have
not been previously batch treated immediately prior to start-up,
• Sweet lines that are to shut-in for longer than 3 months or that may
contain significant concentrations of methanol (i.e. >10% concentration
in the water), as part of the shut-in activities,
• Sweet lines that have been shut-in for longer than 1 year immediately
prior to start-up.
In circumstances where there are no pigging facilities the alternative is to utilize an
inhibitor with a strong vapour phase component in it. An application procedure will
have to be developed for each situation by Operations, the supplier and EH&S
Safety Engineering.
Inhibitors The following is a list of the currently approved batch inhibitors that are to be
utilized as part of this procedure:
• Champion Technologies Cortron RU-196 mixed 1:1 with clean diesel,
• Baker Petrolite CRO 345 mixed 1:2 with clean diesel,
• Brenntag T-8537 mixed 1:1 with clean diesel.
Selection of the inhibitor from the above list should be based primarily upon
matching suppliers with any current mitigation program in the facility but
consideration may also be given to availability and pricing.
Batch Size In order to achieve the recommended 3 mil (0.003”) inhibitor film the following
formula is used to calculate the volume of inhibitor required:
2.8L x Line Size (cm) x Line Length (km)
• Lead Pig: Super pig; shore 90 material, containing a cup, 2 disks, and
a cup. Diameter should be 4 to 5% above pipeline I.D.
• Trailing Pig: Super pig; shore 80 material, containing a cup, 2 notched
disks and a filming disk. Diameter should be 2 to 3% above pipeline
I.D.
• Pig Sizing: Even though both pigs are in the system at the same time
and under the same operating conditions; the second pig must actually
travel faster than the first pig in order to displace or squeeze the
inhibitor back over it. The second pig will actually begin to catch the
first pig. If this does not take place the two pigs and chemical simply
travel through the system as a single unit transporting the chemical
instead of leaving it on the circumference of the line.
• Although it will vary with shore hardness, super pigs are supposed to
be 60% collapsible.
• Attention needs to be paid to pig sizing versus line I.D. for both new
and used pigs. A batch inhibitor pig should be replaced if it is worn to
less than 1% oversize of the pipe internal diameter.
• Pig diameter can be measured with:
a. Callipers or ruler across centreline.
b. Tape measure
c. Pushing the pig through a permanently mounted pipe sample
located near the pig sender
Supplier Pipe-tech Corporation Ltd of Calgary is the preferred supplier of specialty pigs.
Pipe-tech sells a complete line of batching pigs; you must supply pipeline OD
and ID as well as pig sender style when ordering pigs. Ask for filming pigs,
one lead and one filmer per set (see picture below). Pipe-tech can be reached
at 1-887-287-3558.
APPENDIX B.1
APPENDIX B.2
APPENDIX B.3
APPENDIX B.4
APPENDIX B.5
Pipeline
Operations & Maintenance
Task List
TIMING /
REF. ROUTINE ACTIVITY RESPONSIBILITY REPORT TO: COMMENTS
FREQUENCY
Do by exception only as part of travel
3.6 Leak Surveillance Operations Routine Incident Report
routine to wells.
Complete during routine well-site visits
3.13 ROW Surveillance Operations Annual BRCL and by appropriate air or ground vehicle
for sections not visible from road/lease.
App At least
Pipeline Pigging Operations Log Entry
G.4 Monthly
Cathodic Protection Adjustive Operations /
3.15 Probe Annual Include all pipeline risers, test stations.
Survey EH&S
Cathodic Protection Rectifier
3.14 Operations Monthly Probe
Readings
3.2 / Ensure Shut-in Pipelines are
Suspended as per 1st Quarter
App Operations Log
Procedures 2003
A.2
Semi-annual No valves in list. All manual valves due
3.11 Isolation Valve Maintenance Operations Log Entry
(<6 months) annually.
TIMING /
REF. ROUTINE ACTIVITY RESPONSIBILITY REPORT TO: COMMENTS
FREQUENCY
Operations occurrence
Facilities / Each
3.10 Pipeline Repairs occurrence EH&S / OGC
Operations
Annual (or as
Operations
2.2 License Data Updates changes EH&S
Engineering
occur)
BRCL
2.2 Pipeline Status Review Operations Annual
(Pipeline Manual)
App Assess production and work- Operations /
Ongoing EH&S
G.4 over changes Engineering
Compliance Report of Task
Operations Monthly
Activities
Review Pipeline Operating
Operations / EH&S Annual
Manual and update