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Eni S.p.A.
Exploration & Production Division
COMPANY STANDARD
INTERNAL CORROSION MONITORING
SPECIFICATION
FUNCTIONAL REQUIREMENTS
20556.VAR.COR.FUN
Rev. 0 – February 2008
ENGINEERING COMPANY STANDARD
Documento riservato di proprietà di Eni S.p.A. Divisione Agip. Esso non sarà mostrato a Terzi né utilizzato per scopi diversi da quelli per i quali è stato inviato.
This document is property of Eni S.p.A. Divisione Agip. It shall neither be shown to Third Parties not used for purposes other than those for which it has been sent.
Eni S.p.A.
Exploration & Production Division
20556.VAR.COR.FUN
Rev. 0 February 2008
Page 2 of 14
PREMISE
Rev. 0 February 2008
ISSUE
The documents 20196.VAR.COR.FUN and 20197.VAR.COR.SDS have been withdraws
Eni S.p.A.
Exploration & Production Division
20556.VAR.COR.FUN
Rev. 0 February 2008
Page 3 of 14
TABLE OF CONTENTS
1.
INTRODUCTION
1.1
Scope
1.2
Reference Normative
1.3
ENI Internal Normative
1.4
Definitions
1.4.1
General Definitions
1.4.2
Specific Definitions
1.5
Symbols and abbreviations
1.6
Quality Assurance and Company Inspection
1.7
Special Requirements
2.
2.1
2.2
2.3
HEALTH, SAFETY AND ENVIRONMENTAL REQUIREMENTS
Environmental Conditions
Area Classification
Health, Safety and Environmental Regulations
3.
DESIGN CONDITIONS AND FUNCTIONAL REQUIREMENTS
3.1
Design Conditions
3.2
Test Point Location and Corrosion Monitoring Probes Selection
3.3
Intrusive Probes Assembly
3.3.1
Access Fittings
3.3.2
Access Fitting Location
3.4
Intrusive Probe Retrieval
3.5
Retriever
4.
INSTRUMENTATION ASPECTS
5.
TESTING REQUIREMENTS
6.
DOCUMENTATION
Eni S.p.A.
Exploration & Production Division
20556.VAR.COR.FUN
Rev. 0 February 2008
Page 4 of 14
1. INTRODUCTION
1.1
Scope
This Specification provides the functional requirements for the supply of internal corrosion monitoring
equipment and accessories defined in the Company Standards XXXX “Internal Corrosion
Monitoring”.
The requirements provided by this Specification are intended to be used for the purchase of internal
corrosion monitoring equipment selected in the detail design phase of the Project.
1.2
Reference Normative
ISO 9000 family
International Quality Management Standards
IEC 60079
Electrical Apparatus for Explosive Gas Atmospheres
IEC 60529
Degree of Protection Provided by Enclosures
Directive 94/9/EC
Equipment Intended for Use in Potentially Explosive Atmospheres
(ATEX)
NACE RP0775
Preparation and Installation of Corrosion Coupons and Interpretation
of Test Data in Oil Production Practice
NACE MR0175/ISO 15156
Petroleum and Natural gas industries – Materials for use in H2S
containing environments in oil and gas production
Part 1 General principles for selection of cracking resistant materials
Part 2 Cracking resistant carbon and low alloy steels
Part 3 Cracking resistant CRAs
NORSOK M-001
1.3
Materials Selection
ENI Internal Normative
XXX.XXX.XXX.XXX
Internal Corrosion Monitoring
MOD.COR.MON.001
Data sheet. Monitoring systems
MOD.COR.MON.002
Data sheet. Testing report for monitoring systems
1.4
1.4.1
Definitions
General Definitions
For the purpose of applying this Specification to a contract or purchase order, the word ‘shall’
indicates a mandatory requirement; the word ‘should’ indicates a recommendation; and following
definitions shall apply:
COMPANY
Shall mean Eni E&P or its elected representatives.
CONTRACTOR
Shall mean the company appointed by COMPANY to perform the
EPCI works of a package, and its subcontractors, vendors, agents
and authorised representatives.
Eni S.p.A.
Exploration & Production Division
20556.VAR.COR.FUN
Rev. 0 February 2008
Page 5 of 14
MANUFACTURER
Shall mean the party that manufactures equipment and services to
perform the duties specified by COMPANY or CONTRACTOR.
SUPPLIER
Shall mean the party that supplies equipment and services to
perform the duties specified by COMPANY or CONTRACTOR.
1.4.2
Specific Definitions
Access fittings
Fittings flanged or welded to a pipeline or a vessel for the installation
of corrosion probes.
Probe for corrosion monitoring in aqueous environments by
microbial growth on exposed coupons. Coupons are eventually
removed and microbial analysis carried out.
Bioprobe
Corrosion Coupon Probe
Probes with metal samples exposed to the fluid inside pipes or
equipment for a prefixed period; the evaluation of the corrosivity is
based on the metal weight loss.
Corrosion Monitoring Test Point – CMP Positions in correspondence to pipelines or equipment
where internal corrosion monitoring is foreseen by means of suitable
probes. It can consists of a pipe spool, flanged on the line to be
monitored, on which the access fittings and the probes are mounted.
Electrical Resistance Probe
Device for measuring the cumulative metal loss by measuring the
electrical resistance of a metallic element (wire, flat sample, tube).
Hydrogen Probe
Device for corrosion monitoring in environments containing H2S,
based on the measure of the hydrogen entrapped in the metal.
Linear Polarization Resistance Electrochemical technique for measuring instantaneous corrosion
rate of a metal in a conductive fluid.
Linear Polarization Resistance Probe Device for corrosion monitoring based on the principle of the
linear polarization resistance.
Probe
General term to indicate a device for internal corrosion monitoring.
Retriever
Device for insertion, substitution or removal of probes from pipes or
equipment without service interruption. They are of mechanical or
hydraulic type.
Water trap
It consists of a small section of pipe, welded or flanged on the lower
side of a pipeline or equipment, where separation and collection of
water from multiphase systems occurs. Inside the water trap,
corrosion monitoring probes are installed.
1.5
Symbols and abbreviations
ATEX
Explosive Atmospheres
CC
Corrosion Coupon
CIE
Corrosion Inhibitor Efficiency
CMP
Corrosion Monitoring Point
CRA
Corrosion Resistant Alloy
Eni S.p.A.
Exploration & Production Division
ER
Electrical Resistance Probe (traditional)
FSM
Field Signature Method
HIC
Hydrogen Induced Cracking
HP
Hydrogen Probe
IP
Ingress Protection classification
LPR
Linear Polarization Resistance Probe
mpy
Unit for corrosion rate: mils per year
UTMAT
Ultrasonic Thickness Transducer Mat
1.6
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Rev. 0 February 2008
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Quality Assurance and Company Inspection
The SUPPLIER shall have in place a quality assurance organization responsible for formulating and
implementing a quality system, which ensures that the requirements of this specification are
achieved.
Unless otherwise stated in a purchase order, the SUPPLIER’s quality system shall be based on ISO
9000 (or COMPANY approved equivalent) and shall be described in a Quality Assurance Manual.
The Quality Manual and Quality Plan shall be submitted to COMPANY with the tender documents.
1.7
Special Requirements
All correspondence, reports, manuals, test reports, certificates shall be in the English language or
shall have authenticated translations accompanying them.
If the requirements of this specification cannot be met, written notification of non-compliance,
including explanations and proposed change, shall be provided at the bid stage by the SUPPLIER for
COMPANY approval.
Eni S.p.A.
Exploration & Production Division
20556.VAR.COR.FUN
Rev. 0 February 2008
Page 7 of 14
2. HEALTH, SAFETY AND ENVIRONMENTAL REQUIREMENTS
2.1
Environmental Conditions
Instrument for external areas shall be suitable to operate in industrial, humid, saline and corrosive
atmospheres, in the ambient minimum and maximum temperature extremes as defined in the basis
of design, including maximum temperature excursions due to solar radiation.
Instrumentation shall be suitable for relative humidity conditions range from 25% up to 100%.
2.2
Area Classification
Electrical and electronic instrumentation for installation in hazardous areas shall in general be
suitable for use in hazardous areas as defined by IEC 60079 ‘Electrical Apparatus for Explosive Gas
Atmospheres’.
Intrinsic safety, EEx (i)a shall be used as the prime method of protection. Deviation from this will
require written permission from the COMPANY. Should permission be given, the allowable
alternative methods of hazardous area protection are listed below in order or preference:
−
Flameproof or explosion proof type EEx(d)
−
Increased safety, type EEx(e)
−
Special protection, type EEx(s).
All electrical systems shall be designed to conform to ATEX requirements. All equipment and
protective system intended for use in potentially explosive atmospheres within the European
Economic Area will have to display the CE marking in accordance with the ATEX Directive 94/9/EC.
ATEX covers equipment and protective system that may be used in areas endangered by potentially
explosive atmospheres created by the presence of flammable gases, vapours, mists or ducts.
2.3
Health, Safety and Environmental Regulations
The SUPPLIER shall be responsible for ensuring that goods and services supplied meet all
applicable regulations on health, safety and environmental issues.
The equipment shall be designed to operate safely and satisfactorily at all expected combinations of
process, utilities, climates and environmental conditions including those at start-up, shutdown, partial
load operation, and emergency cases while retaining the overall system security, reliability and
availability.
Eni S.p.A.
Exploration & Production Division
20556.VAR.COR.FUN
Rev. 0 February 2008
Page 8 of 14
3. DESIGN CONDITIONS AND FUNCTIONAL REQUIREMENTS
3.1
Design Conditions
Unless to be installed into an environmentally controlled area, all corrosion monitoring system
equipment (instrumentation, probes etc.) shall be suitable to operate at the ambient conditions as
defined in paragraph 2.1.
The design life of the corrosion monitoring system shall match the design life of the structure to
monitor.
Weight loss corrosion coupons and intrusive corrosion sensors subjected to consumption shall
guarantee the maximum lifespan obtainable without compromising the functionality and the specified
requirements of the probe, as sensitivity, response time etc. As a minimum, the design life of the
sensor should be equal to 2 years, and consistent with the inter-period between shutdowns if sensor
retrieving under pressure is not allowed.
In presence of toxic/lethal fluid, the retrieval of intrusive probes from live lines shall not be permitted.
Retrieval of probes and coupons shall be undertaken only after depressurisation and possibly
purging.
For safety reasons, the installation of intrusive probes on piping systems designed for pressure
above class #900 psi is to be carefully considered and possibly excluded to avoid leakage of toxic
fluid from critical high-pressure systems. The installation of intrusive probes on piping systems
designed for pressure above class #2000 psi is not recommended.
The SUPPLIER shall review and confirm suitability of the corrosion monitoring devices and
accessories with respect of the following environmental factors and aspects:
− minimum and maximum design temperature;
− minimum and maximum design pressures;
− formation of condensates;
− presence of corrosive species or pollutants;
− formation of moulds;
− electrical hazard;
− mechanical stress and vibrations during operation;
− electro-magnetic influence;
− explosion and fire hazard.
The SUPPLIER of corrosion monitoring system equipment shall also provide details of in-built safety
features to avoid leakage as well as any venting requirements.
The SUPPLIER of probes shall recommend element types for the indicated sensitivity and design life
as specified in this document.
3.2
Test Point Location and Corrosion Monitoring Probes Selection
The basic guidelines for the design of internal corrosion monitoring system are provided by Company
Standards XXX “Internal Corrosion Monitoring”. This Standard provides criteria for the selection of
the location of the corrosion monitoring test point “CMP”, a description of the different types of the
available probes and criteria for the probes to install at each CMP and their method of installation.
3.3
Intrusive Probes Assembly
The assembly of intrusive probe consists of the following components:
Eni S.p.A.
Exploration & Production Division
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−
−
−
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20556.VAR.COR.FUN
Rev. 0 February 2008
Page 9 of 14
access fitting,
probe,
solid plug (corrosion coupon) and hollow plug (ER probes),
cap,
probe holder,
electronic equipment,
spare parts.
Functional requirements for the above components are herein specified.
3.3.1
Access Fittings
Intrusive monitoring probes and coupons shall be installed by means of two-inch high-pressure
access fittings at the pre-selected locations (CMPs). For piping design pressure lower than 150 psig
(piping class rating #150 psi) the use of high-pressure access fittings may be waived. For highpressure piping (piping class rating above #2000 psi) the use of intrusive probes to be installed
through access fittings is to be avoided.
Access fittings may be flareweld or flanged and may be normal or tee-type. For systems containing
toxic or lethal fluids or for high pressures system (above #900), the tee-type shall not be used.
Flanged type access fittings shall be ANSI flange RJ or RF, non-tee type. Two-inch weld-o-flange
shall match, as a minimum, rating and material of the parent pipe. Blind flanges shall be used where
preliminary installation of access fittings is initially foreseen to allow a subsequent upgrading of the
CMPs.
Access fitting material (weld-o-flange assembly) shall conform to the requirements of the project
piping specification as a minimum. If dissimilar materials were considered in flanged assembly,
galvanic corrosion shall be avoided by using electrical insulation kits.
The welding of access fittings onto any equipment shall comply with the requirements of the
applicable Project documents and Codes. Welding of different materials should be avoided.
3.3.2
Access Fitting Location
In selecting the exact location of the access fitting at the pre-selected CMP’s location, adequate
clearance shall be guaranteed to allow comfortable and safe operations of maintenance, periodical
probe replacement or manual data retrieving. At this purposes, adequate horizontal and vertical
clearance shall be foreseen in the design phase (typically, clearance to accommodate the probe
retriever shall be verified). The Supplier shall provide all relevant information on detailed datasheets
to permit the verification that all clearances constraints are satisfied.
When more than one access fitting are installed at a CMP, the inter-axial distance between two
fittings shall not be lower than 500 mm.
To minimise the effect of flow rate and flow regime on corrosivity, the access fittings should be
located at a minimum distance of 7 pipe diameters downstream-of and a minimum of 3 pipe
diameters upstream-of any changes in flow caused by bends, reducers, valves etc.
To avoid debris accumulation leading to galling at the threads, a top of the line installation is
preferable, unless the specific need of bottom of the line installation is dictated by preferential
corrosion in this area (typically in oil systems where water stratification at the bottom is expected). In
the latter case the Supplier shall provide evidence that a specific design of the probe assembly or a
specific retrieval procedure can prevent this problem.
Access fittings orientation shall be vertical, unless the specific purpose and location of the probe
dictates a different orientation.
Eni S.p.A.
Exploration & Production Division
3.4
20556.VAR.COR.FUN
Rev. 0 February 2008
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Intrusive Probe Retrieval
Weight loss corrosion coupons require periodic retrieval at scheduled frequency (typically 6 months)
for replacement and corrosion rate measurements. is designed to be carried out by means of
appropriate extractor tools. Other intrusive probes may also require occasional probe retrieval in
case of sensor malfunction or consumption. This operation is carried out with a proper extractor tool
(or retriever) described in paragraph 3.5.
The retrieval of intrusive probes from live lines may represent a safety hazard and shall be carefully
evaluated as discussed in paragraph 3.1. If the retrieval operation involves risk for personnel
associated to the release of lethal or toxic fluid and/or the high system pressure, retrieval under
pressure shall not be permitted and the installation of block and bleed valves is required to allow
local depressurization and avoid major shutdown to accomplish this operation. After depressurization
local purging may also be required depending on the level of toxicity of the fluid. These operational
procedures shall be clearly stated in the Operation Manual of the corrosion monitoring system.
Probe assembly, access fittings, clearances etc. should be designed to allow the retrieval of intrusive
probes with the same extractor tool.
All intrusive probes shall be checked during each scheduled plant shutdown, and replaced where
necessary
3.5
Extractor Tool (or Retriever)
Commercially available extractor tools (or retrievers) allow the insertion and the extraction of
coupons and other intrusive probes on “live lines” under pressure. This operation may be therefore
carried out with no necessary need for shutdown. Market available tools permit to operate with
temperatures up to 120°C and pressures up to 600 bar.
However, as discussed in paragraphs 3.1 and 3.4, safety considerations may dictate that this
operation be preceded by depressurisation and possibly decontamination (purging).
Two types of retriever are accepted:
− mechanical;
− hydraulic.
In a mechanical retriever, the counter pressure to extract the probe is effected by a threaded
mechanical seal. In a hydraulic extractor, the counter pressure is provided by a hydraulic system.
Hydraulic extractor has smaller dimensions and weight and is usually more reliable. From a safety
perspective, hydraulic system has to be preferred because it allows remote control in the most critical
phases (extraction and installing).
The materials used for the extractor and valve, both internal and external, shall be suitable to resist
corrosion from process fluids and to warehouse storage conditions.
In the presence of H2S-containing fluids (sour service), the materials that may be exposed to the
contact with sour fluid shall be compliant with the requirements of ISO 15156 / NACE MR0175 with
respect to both material requirements and environmental application limits.
The materials of each component shall be submitted to Company for review and approval.
The threads of access nozzles, the extractor service valve and the extractor itself, must be
trapezoidal, for rapid connection operations.
The extractor tool should be equally capable of retrieving corrosion coupons and other intrusive
probes in use in the field.
Eni S.p.A.
Exploration & Production Division
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Rev. 0 February 2008
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Adequate maintenance shall be periodically provided to all moving parts of the retriever.
Eni S.p.A.
Exploration & Production Division
20556.VAR.COR.FUN
Rev. 0 February 2008
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4. INSTRUMENTATION ASPECTS
The supply of corrosion monitoring system shall include all instrumentation required for manual or
remote (on-line) data retrieving, data interpretation and data storage, maintenance, probe retrieval
(retriever or extractor tool), spare parts etc.
Transmitters and other electronic items shall be suitable for use in hazardous areas as defined by
IEC 60079 ‘Electrical Apparatus for Explosive Gas Atmospheres’.
The protection level of mechanical instruments and field junction boxes shall have the appropriate IP,
as per IEC 60529, for the specific exposure in accordance with the appropriate Project
documentation. The electrical certification shall be EEx (e). Junction Box enclosure material shall be
stainless steel or GRP.
Electronic instrument method of protection shall be selected in accordance with the appropriate
Project documentation.
All instruments shall be accessible for operation and maintenance and where necessary platforms
and stairs shall be supplied with package skid. Instruments shall be located as near to the point of
measurement as practicable and mounted on instrument stands or brackets.
Instrumentation and cables, primary connection, pneumatic connection, electrical connection, bulk
instrument types and materials for impulse line and for air network shall be in according to the
applicable Project documentation.
Instrumentation shall be suitably protected from the environment. Heated enclosures, heat tracing
and insulation shall be applied as appropriate. Heaters and heat tracing shall be of the self-regulating
type with sufficient rating to be able to heat impulse lines and instrument bodies to the minimum
operating temperature from the minimum ambient temperature.
Adequate electronic instruments are required to measure the signal and to determine the corrosion
rate.
Portable instruments shall be able to operate:
− at the minimum and maximum design ambient temperature
− at a relative humidity of 100%
− at the applicable IP and explosion proof classification.
Eni S.p.A.
Exploration & Production Division
20556.VAR.COR.FUN
Rev. 0 February 2008
Page 13 of 14
5. TESTING REQUIREMENTS
Probes
Each apparatus containing electrical or electronic components shall be subjected to testing as
follows:
− electrical test: it will be switched on for 24 hours consecutively and shall not overheat in any part;
− functional test: on properly prepared samples, the equipment must operate properly in all
possible conditions (in minimum and maximum conditions as regards the signal or the measured
value) both immediately it is switched on and after 24 hours continuous operation
Apparatus that does not pass the specified tests shall be rejected.
Each probe shall be subjected to testing as follows:
− electrical test: all electrical contacts will be verified. On hydraulically tested probes, the electric
isolations of sensors will also be checked (electrodes for linear polarisation probes; calibrated
wire for electrical probes) at the beginning and after 24 hours exposure.
− functional test: the probes subjected to hydraulic test must be subjected to functional tests at the
beginning and end of the electrical testing.
The probes that do not pass the specified tests shall be rejected.
Probe Housing and access fitting
Each component of the monitoring system shall be tested by the Supplier according to the following
procedures.
Mechanical parts (certification and traceability)
Mechanical parts forming the access fitting and all the related accessories shall be subjected to the
following check:
− identification of serial numbers: for each mechanical component (access nozzle, extractor and
the relevant service valve, probes) it shall be verified that each part has a permanent label with
the corresponding catalogue number;
− certification: each part identified with a code number shall be supplied with a certificate of
chemical analysis and mechanical properties, carried out by the supplier of the materials or a
recognised laboratory;
− positive material identification: components manufactured from special materials shall be
subjected to positive material identification as per Project procedures.
Hydraulic Test
Probes shall be subjected to hydraulic test for at least two consecutive hours at a test pressure of
150% the maximum design pressure. The test must be carried out with an aqueous solution coloured
with appropriate red or fluorescent colouring. The test result will be considered positive if no leak of
solution is observed and the pressure remains constant (accepted variation: 1%). The testing
frequency on the probes shall be, as a minimum, each type of probe (solid or hollow) and then a
minimum of 10% of the total for each type supplied.
Eni S.p.A.
Exploration & Production Division
20556.VAR.COR.FUN
Rev. 0 February 2008
Page 14 of 14
6. DOCUMENTATION
The Supplier shall submit a complete set of technical documentation, which shall include also
catalogues and technical bulletins, with the indication of codes for each part of the system.
Each part identified with a code number must be supplied with a certificate of chemical analysis and
mechanical properties, carried out by the Supplier of materials or a recognised laboratory.
For electrical resistance probes, technical documentation indicating reference hydrodynamic
conditions shall be provided for the adjustment of the probe.
Quality Assurance manual and Quality Certificate are required.
The Supplier shall provide all information and technical bulletin relevant to:
− acquisition data system,
− elaboration data system,
− personnel training,
− installation, extraction and cleaning operation of probes,
− analysis and interpretations of results,
− probe length for specified fitting stand-off.
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