API 579: a comprehensive fitness-for-service guide Ted L. Anderson•·*, David A. Osageb 'Smtcluml Reliabilil)• Teclmol<>gy, 1898 S Flmirort Cotm. Sui1e 235, Boulder. CO 80301. USA 'M & M Engineering, Sltaker fleiglm. OH. USA Received 4
Augus12000; revised II Decemher 2000; accep1ed 13 Decemher 2000
Abstract This an iclc presents an overv iew of the rcccmly published Amc1ican Pctroleumlnstitutc (API) Recommended Pwctice 579, which covers fitness-for-service assessmem of pressure equi pmem in petrochemical and other industries. Although API 579 covers a wide range of flaws and damage mechanisms, including local metal loss, pitting coiTosion, blisters, weld misal ignmem. and fi re damage, the emphasis of the present arricle is on the assessment of crack-like llaws. The API 579 p rocerlure for evaluating c.-acks incorporates a fai lm·e assessment diagram (FAD) methodology very similar to that in other documents. such as the British Energy R6 approach and the BS 7910 method. The API document contains 1m extensive compendium of K solutions, including a number of new cases generated specifically for AP1579. In the initial release of the document. API bas adopterl ex isting reference stress solutions fo.r the calcul.ation of L, in the FAD procerlure. In a future release, however, API plans to replace these solutions with values based on a more rational definition of reference stress. These revised reference stress solutions will incorporate the effect of weld mismatch. In addition to the Appendices of K and reference stress solutions, API 579 includes awendices that provide guidance on esti mating fracture toughness and we ld residual stress distributions. Over the next few years these appemUces will be enhanced with advances in technology. Recently, API has entered into discussions with the American Society of Mechanica l Engineers (ASME) to convert API 579 into a t APIIASME fitness-for-service guide. © 2001 PubJishcd by Elsevier Science Ltd. Keywords: American Petroleum Institute; Pai lun:: assessment diagram; f:o"Jaw assessment: J'}itness for service; Fracture toughness; Rcfcn::m:c Slress; Residual
stress; Stress imcosity fac1or
1. Background Ex isting US design codes and smndards for pressurized equipment provi de ru.les for the design, fabrication, inspection and testing of new pressure vessels. piping systems. and storage tanks. These code-s do not address the fact that equipment degrades whi le in -service and deficiencies due to degradation or from original fabrication may be found during subsequent inspections. Fitness-for-service (FFS) assessmentS are quantitative engi neering eva.luations, which are performed to demonstrate the structural integrity of an in-service component containing a flaw or damage. The American Perro.leum Institute (APT) Recommended Practice 579 [ l] has been developed to provide guidance for conducting FFS assessments of flaws commonly encountered in the refining and petrochemica l industry which occur in pressure vessels, piping, and tankage. However, the assessment procedures can also be applied to flaws encountered in other industries such as the pu lp and paper industry, " Com:spondingaulhor. Tel.: +1 -303-415-1475; fa.: +J-303-415-1847. E-mail address:
[email protected] (T.L. Anderson).
0308-0 161/001$ - see fron1 mauer © 2001 Published by Elsevier Science Lrd. Pll: S0308-0161(01l000 18-7
fossil fuel util ity industry, and nuclear industry . The guideli nes provided in API 579 can be used to make run-repairreplace decisions to ensure that pressurized equipment contain.ing flaws that has been ident ified during an inspection can continue to be operated safe.ly. API 579 is intended to supplement and augment the requirements in APT 510 [2], APT 570 [3], and API 653 [4): to ensure safety of plant personnel and the publ ic whi le older equipment continues to operate; 10 provide technicall y sound FFS assessment procedures: to e nsure that di:fferent serv ice providers furnish consistent remaining life predictions; and to help optimize maintenance and operation of e)(iSiing facilities to maintain avai.l ability of older plants and enhance long-tenn economic viabili ty. In addition. API 579 will also be used in conjunction with API 580 Recommended Practice For Risk-Based Inspection [5] that is being developed to provide guidel ines for risk asse-ssment, and prioritization for inspection and m ai ntenance planning for pressure-containing equ ipment. The initial impetus to develop an FFS standard that cou ld be referenced from the API inspection codes was provided by a t Industry Project (JlP) istered by the
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T.L Anderson. D.A. Osag' /lntenuuiOiwl Journal of Presmre Vessels and Piping 77 (2000) 953- 963
Material Properties Council (MPC). The driving force behind this development was p lant safety. The methodology provided for in this document, together with the appropriate API inspection code, had to ensure that equipment integrity cou ld be safely maintained when operating equipment with flaws or damage, and could also be used to demonstrate compUaoce with US Occupational Safery and Health istmtion (OSHA) 19 10 Process Safety Management (PSM) Legislation. A review of the existing international FFS standards by the of the MPC JlP was undertaken in 199 1 as the starting point for the development of a new FFS standard. Based on the resu lts of this review, it was detenn ined that a comprehensive FFS standard covering many of the typical ftaw types and damage mechanis ms found in the refining and petrochemical industry did not ex ist. In addition, the existence of many company-based FFS methods, the complexity of the tech nology that no single company c;m solve on its own, and the need to gain acceptance by local jurisdicti ons in the US further indicated the need for a new standard. Therefore, the JJP decided to start the development of the required FFS technology that would be needed to write a comprehensive FFS standard for the refining and petrochemical indus oy. The results of this work were docu-
mented in a MPC FFS TIP Consul tant's Report [6), and this document was subsequently turned over to the API Committee on Refinery Equ ipment (CRE) FFS Task Force charged with development of the FFS standard. In adopted by the API CRE FFS Task Group developing APT 579, an FFS assessment is an engineering analysis of equipment to determine whether it ~s fit for continued service. The equipment may contain flaws, may not meet current design standards, or may be subjected to more severe operating condi tions than the original or current design. The product of a FFS assessment is a decision to operate the equipment as is , alter, repa ir , monitor, or replace; guidance on an inspection interval is also provided. FFS assessments consist of analytical methods to assess flaws and damage and usually require an interdisciplinary approach consisting of the following: • Knowledge of damage mechanisms/material behavior. • Knowledge of past and future operating conditions and interaction with operations personnel. • NDE (flaw location and sizing). • Material properties (environmenta l effe<.:ts). • Stress analysis (often finite element analysis). • Data analysis (engineering reliabil ity models).
Table J Orgcmiza1ion of each .sec1ion in APJ 579 Section subparagraph
Title
Overview
General
The scope and overall requircmcms for an FFS assessment arc provided
Applicability and limilations of
The applicability and limitations for each FFS assessmcnL procedure are clearly indicated; these limitations arc stated in the front of each section for quick reference The data requirements required for the FFS assessment arc clearly outlined; these data requirements include: Original equipmem dc.sign data Maintenance and operationaJ hisrory Required dma/mcasw·erncncs for a r:-r:s assessment Recommendatio ns for inspection technique and sizing requirements
number
2
the FFS assessment procedures
3
Data requiremcnl.S
4
5
Assessmen1 techniques and acceptance Cl'ileJ'ia Remaining life evaloalioo
6
Remedialioo
7
(n .~e rvice
8
Documentation
9
Rcren:nces
moni1oring
10
Tables and iigures
II
l'lxample problems
Detailed assessme nt rules aJ'e provided fOI' three levels of a.<ses$ment: Level I. Level 2, and Level 3. A cUscussion of these assessment levels is cove1·ed in the body of this paper Guidelines for perfonning a 1-emaining life C$timate a1-e provided for the pUI·pose of establishing an inspection Interval in conjunction with the go,·em ing inspection code Guidelines are presemed on methods to mitigate and/or comrol fumre damage. In many cases. changes can be made to the. component or LO rhe operat ing conditions to mitjgate t:he progression of cia mage Guidelines for monitoring damage while the component i:; in-service are provided. these guiclelineo; are useful if a fuJUre damage rate can.not he estima1ed e-a..~>ily or the esLimmed remaining li fe is shon. In-service monitoring is one 1t1ethod wht:reby future ctamage or conditions leading to future damage can be assessed or confidence in Lhe remaining life cslimatc can be increased. Guideli nes for documentation for an assessment are provjded; tbe general rule is - A practitioner should be able to repeat the analysis from the documentari<m withow consulting an imlividual origlnally invol ved in the FFS assessment A comprehensive list of technical references used in lhc development of the FFS assessmcnl procedures is provided: references to codes and standards are provided in this section ·rabies and tlgurcs including logic diagn:unsa.n:: used extensively in each sec1ion to clarjfy assessment rules and procedures
A number of example problems arc provided, which demonstrate tlle application of the FFS assessment procedures
1:1-. Amlcrson, D.A. Os<1ge I lnrern(l(iona/ Journal of Pressure v,ssels tmd Piping 77 (2000) 953-963
Based on this definition , the APT CRE FFS Task Group modified and greatly enhanced the initial efforts of the MPC Jfp to produce the first edition of API 579. The MPC JTP conti.nued tO provide valuable technical contributions throughout this development effort and essentia lJy became the technical development ann of the API Task Group. The MPC FFS JfP is sti ll in ex istence and conti nues to provide FFS technology development while working closely with the needs of the API CRE FFS Task Group. The overall organi zation and assessment procedures in API 579 are reviewed below. This is followed by a more detailed discussion of the API 579 assessmem of cracks.
955
consrructed to the following codes: • • • • • • •
ASME B and PV code, Section Vlll, Division 1 ASME B and PV code, Section VJIT, Divis ion 2 ASME B and PV code, Section I ASME B31.3 Piping code ASME B31.1 Piping code API 650 APT 620.
Guide lines are also provided for applying APL579 to pressure-contai ning equipmeot constructed to other recognized codes and standards, inc luding international and internal corporate standards.
2. Overview of API 579
2.2. Organization
2.1. Applicable codes
APT 579 is a highly srructured document designed to faci litate use by practitioners and to facilitate future enhancements and modifications by the API CRE FFS Task Group. Section I of the document covers: introduction and scope; responsibil ities of the owner-, inspector, and engineer; qualification requirements for the inspector and engineer; and references to other codes and standards. An outline of the overall FFS assessment methodology that is
API 579 provides guidelines for perfonning FFS assessments that can be useJ in conjunctio n with the APT Inspection codes (APT510, API 570 and API 653) to determine the su itability for continued operation. The assessmem proceuures in this recommended practice could be used for FFS assessments and/or rerati ng of components designed and Table 2 Overview o f flaw anct dmnage assessment procedures
Flaw or damage mechanism
Overview
3
Brittle fract w·c
Asscssmcn1 procedures an: provided to evaluate t.h c resistance to briulc rr.!Ctun: of in-service l'arbon and low aJI()y s teel prcssw·c vessels, piping. and storage tanks. C riteria arc pruvided to
4
General meta l loss
Section in API 579
evaluaLe nonnaJ op-cra1ing, swn-up. upset, and shutdown condi1ions Assessment procedures are provided to evaluate general <.'O JTOsion. Thkkncs.o; dma used ror the assessment can be cilhcr point thk:kness n:adings ur detailed thickness profiles. A methodology is pro·vided w guide the practitioner to the local tnt:tal loss assessmcnL procedures based on the type a nd variability o f th ickness data rc:cmded during an inspection
5
Local metal loss
6
Pitdng corrosion
7
Blisters and lamina1ions
8
\ Veld misaJignmenL a nd shell di~ton ions
9
Crack-like f1aws
10
High tcm p~ralure oper..ttion and creep
II
Fire damage
Assessmem techniques Ul'e provided to evaluate single and networks of Local Thin Al'eas (LTAs), and groove-like Raws in p1·essurized components. Detruled thickness profiles al'e required for Lhe assessment. The assessment p1·ocedures ca.n also be utitized to evalume blisters Assessment procedures al'e provided to e'•alume 'videly sca11ered pi uing. localized piuing. piuing which occurs wit.hjn a region of local me1a lloss. a nd a re.g ion of localized me.t al loss located within a region of widely scaue recl pitting. The. assessment procedures can aJso be utilized to evaluate a network of clo~el y spaced hlis Le.n::. The asse$-~mem procedures ut ilize L,he. methodology devel oped for Local meta l loss Asseso;ment procedure~ are provided to evaluate e ither isolated. or nelwork.s of blisters ;md laminations. The assessme.ot guideljnes include prO\' isions for blisters located at weld ts and srruclur.tl disconlinuities such as s heJI transit ions, Sl i[ening rings. and nozzles Asses.sment procedures are provided to evaluate s tresses resuhing rrom geometric disconl inuiljes in shell type ~tructurcs including weld misa lignment and shcJI disto11ions (e.g. ou t~of~ roundness, bulges, and dents) Assessment procedures are provided to e valuate c rack-Like (l aws. Re(·(nnmc.ndations for evaluating cr.lck gruwrb including enviroomentaJ concerns an= a lso covered A.;sessment proccdl.lft!S a rc provided 10 derennine the remaining life of a component operating in the c reep regime. T'he remaining li fe procedures are limited to the initiation of a c rack Assessment prot..'Gd ures arc provided to evaluate equipment s ubjcct lO fire damage. A
methodology is p•·o,•ided ro rank and screen components for evaluation based on the hem exposure expetienced during the 6re. The assessmem ptocedures of the other secLions of this publication a re util!ized to eval uate component damage
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T.L Anderson. D.A. Osag' / lntenuuiOiwl Journal of Presmre Vessels and Piping 77 (2000) 953- 963
common to all assessmen t procedures included in API 579 lS provided in Section 2 of the documcm. The organ ization of Section 2 is shown in Table I. This same organization is utilized in aU subsequent sections that contain FFS assessment procedures. Starting with Section 3, a catalogue of FFS assessment procedures organized by damage mechanism is provided in API 579. A complete listing of the flaw and damage assessment procedures currently covered is shown in Table 2. These damage mechanisms can be grouped at a higher level to foT111 a degradation class (see Fig. I). This higher level of organization is useful in that it provides insight into how the assessmem procedures of different sections may be combined to address complex flaws in a componen1. As
shown in Fig. I, several flaw types and d;unage mechanisms may need to be evaluated 10 detem1ine the FFS of a component. Each section in API 579 referenced within a degrada· tion class includes guidance on how to perform an assessment when multiple damage mechanisms are present. When assessment procedures are developed for a new damage mechan ism, they wi II be added a.s a self-contained section to maintain the strucmre of API 579. Currently, new sections are being developed to address hydrogen induced cracking (HIC) and stress-oriented hydrogen induced cracking (SOHlC) damage. local hot spots, assessment procedures for riveted components, and creep c rack growth. A series of append.ices are provided which contam tech nical information that can be use with all sections of API
Stress Analysis
Flaw Dimensions
!
I
Stress Intensity Factor Solution, K1
Material Toughness,
~.
:
Kr =
Kl
K~AT
Failure Assessment Diagram Envelope Brittle Fracture
Unacceptable Region
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0
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Mixed Mode· Brittle Fracture And Plastic Collapse
Assessment/ Point
(f) (f)
l1J
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z
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(!)
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1
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LOAD RATIO
cr,.,
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Reference Stress Solution, "ret
l Flaw Dimensions
.
Material Yield Stress,
I Stress Analysis
F'ig. I. Schemal ic overview of the FAD prn<:
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1:1-. Amlcrson, D.A. Os<1ge I lnrern(l(iona/ Journal of Pressure v,ssels tmd Piping 77 (2000) 953- 963
957
Table J API 579 appendices Appendix Tio le Thickness. MAWP and membrane srress equations ror a FFS assessment
B
c D
Su·ess analysis overview for a FFS assessment Compendimu of SLTess intensity factor solut.ions
Compendium of reference stress solutions
Overview
Equations for the thicklless. MAWP. and membrane stress are given foo· onos1of lhe common pressurized components. These equ~1tions are provided to assist intenlational practitioners who may no1 have access 10 ohe ASfVlE code and who need 10 deoennine if ohe local design code is simi lao·10 ohe ASME code for which ohe FFS as,;essoneno procedures were primarily designed for Recomonendaoions for ~1ress analysis oechoiques thai can he used 10 peri'ol'm an FFS assessmeno are provided including guidelines for finite element analysis A <.·ornpendium of snes.s intensity f~tctor .soJutions for common pressur:ized components (i.e. cyl_inders. spheres. nozzle. etc.) are given. These solu1ions are used for 1he-assessme.nt of crack like naws . The solutions presented represent Lhe latest technology and have been re~derived using the finile e.lement method in conj unction wil·h weight functions A compendium of refe.rencc stress solutions for common pressurized components (i.e. cylinders,
spheres. no.u.lc, e tc.) arc gi ven. These solutions are used fo r the assessment of crack ~ like llaws
E
Residual stresses in a FFS evaluation
F
Material propc11ies for a FFS assessment
G
Deterioo·aolon and failuo·e modes
H
Valiclaoion
I
Glossary o f 1em1.s and definit ion ~ Technical inqui(ies
J
Procedures to estimate the thmugh~wall residual stress fidel" for dilfercnt weld ge<>mctries are provided; this infonnation is required ror the assessment of crack like Haws Material proper! ies required for all FFS assessments arc provided including: Sutngoh par.nnerers (yield and tensile su·css) Physical properties (i.e. Young's Modulus, e1c.) f'ra.clw·e (Oughness Dma for fariguc crack. growth cakulaLions Pao igue cur l'es (lnioiao.ion) Mareria.l data for co:ee1> analysis including remai ning life and creep cr•ck growoh An overview of tlle types of naws and damage mechanisms thai can occur is pl'ovided. concem rating on service-induced degl'adation mechanisms. This appendix only provides an abridge-d Q\'erview on damage mechanisms; API 57 1 is cun·ently beiog developed to provide a definitive reference for damage mechanisms ohm can be used wioh API 579 and A PI 580 A.n overview of the smd ies use.d to valjdate the gene.ral and local nJet~llloss, and the crack-like llaw a.c;sessmenL procedures are provided DeHnilions for common used throughout the sect ions and appendj ce~ of API 579 are g iven Guidelines for .submiuing a le-ehnical inquiry tn AP·r are provided. Techn ical inquires will be forwarded 10 1he API CRE FFS task grour for resoluoioo
579, which cover FFS assessment procedures. The maj ori ty of the information in the appendices covers stress analysis tech niques, material property data, and other pe11ine111 information that is required when performing a FFS assessment. An overview of the appendices is provided i.n Table 3. 2.3. Assessmem me!hodology
The API 579 FFS assessment methodology used for aU damage type_~ is provided in Table 4. The organization of each section of APT 579 that covers an assessment procedure is consistent with this methodology. This consistent approach to the treatment of damage and the associated FFS assessment procedures fac ilitates use of the document in thai, if a pmctiti oner is fami liar with one section of the document, it is not difficult ro utilize another section because of the commoo structure. This assessment methodology has proven to be robust for all flaw and damage types that have bee n incorporated into API 579. Because of this success, when new sections are added to APT 579, the template used for the development will be based on this assessment methodology. 2.4. Assessmem levels Three levels of assessment are provided in API 579 for
each flaw and damage type. A logic diagram is included in each section tO illustrate how these assessment levels arc interrelated. As an example, the logic diagram for evaluating crack-like flaws is shown in Fig. 2. In general, each assessment level provides a balance between conservatism, the amount of information required for the evaluation. the skill of the practitioner perform ing the assessment, and the complexity of analysis be ing performed. Level I is the most conservative, but is easiest to use. Practi tioners usually proceed sequentially from a Level l to a Level 3 assessment (unless otherwise directed by the assessment techniques) if the current assessment level does not provide an acceptable result or a clear course of action cannot be determined. A general overview of each assessment level and its intended use are described below. • Level 1 - The assessment procedures included in this level are imended to provide conservative screening criteria that c;m be utilized with a minimum amount of inspection or component information. The Level I assessment procedures may be used by ei ther pl ant inspection or engineering personnel. • Level 2 - The assessment procedures included in this level are intended to provide a more detai led evaluation that produces results that are less conservative than those
958
T.L Anderson. D.A. Osag' / lntenuuiOiwl Journal of Presmre Vessels and Piping 77 (2000) 953- 963
Table 4
API 579 FFS asses;men1 melhoctology for al l damage 1ypes Srep l.kscriplion Flaw tmd tltunage mechw1ism ldentijicmion - The first step in a FFS asses.~ment is to identify the tlaw type and cause of damage. FFS assessments should not be pcrfonned unless the c~use of the damage can be identified. The o riginal design and fab1ication practices. materials of construction.
2
3
service his tory, and environmental conditions can be used to a.~>Certain Lhe likely cause of the damage. Once the naw type is idcntilicd, the appropriate section of Lhis document t:an be sele<:led for the assessment Applicabili(y and limitations of the FFS clsscs.ymem procetfures - The applicability and limitations of the asse5Smenl procedure arc described in each seCti(>n 1 and a de<.:ision (>n whether 10 proceed with an assessment can be made Data requin•mems - The data required for FF·s assessments depend on Lhe naw t)'pc or damage mechanism being c\•aluated. Dma requirements may include: original equipment design data~ information pcnaining to maintenance and operational history; expected fu1Urc service~ and data specific to the
FFS as.sessmem such as llaw size. s1a1e of stress in lhe componem ar lhe loca1ion of 1be Oaw. and material properties. Da1a requiremen1s common 10 all
FFS assessm_e nt procedures are covet'ed in Sectio1t J. Data reqWrements specific 4
lO;;. damage
mechanism or flaw type. are covered in lhe seclion
comai.ning the con·esponding assessmem p.1·ocedU1'es Asse,n~me.nt teclmiques and acceptance trittria - Assessment techniqu-es and acceptance criteria al'e provided in each $ection. If multiple damage mechanisms al'e p1·e sem. more than one ~ Lion may have to he used for the evalua1.ion
5
6 7
8
An es1ima1e of 1he 1·emaining life or limi1ing Oaw size should be made. The remaining life is eslablished using !he PFS
Remainillg life evaluurioll -
assessmem procedures with an eslima1e of furore damage nne (i.e. con·osion allowance). T he remaining life can be used in conjunction with nn inspection code to establish an inspec1ion interval Remedimion - Remediation 1nerhods are provided in each sec1ion based on the damage mechanjsm or naw type.. _In some cases. remediation techniques may be used 10 control fu ture damage associated with naw growth and/or material degradat ion In-service monitoring - M.e Lhocts fo r in-service monitoring Hre provide d in each sectic.)n based on the damage mechanism or tlaw type . hH;ervice monitoring may be U.""-d for Lhosc case5 where, a remaining life and inspeclion interval cannot be adequately established because of the complexilies associated damage mechanis m and service environment Dnrwnenration - The documentation of an FFS asse5Stnenl s hould incl ude a record of all data and decisions made in e ach of the previous steps to qualify lbe component for continued operation . Documcnlat ion requircmenL~ t•ommon to all FFS assessment procedures arc given in Section 2 of API 579. Spcdfk <.locumentalion requjremems for a particular damage medt:anism or naw type are covered in Lhc sec.:tion conLaining the con·csponding assessment procedures
from a Level l assessment. In a Level 2 assessment, inspection information similar to that required for a Level I assessment are required; however, more detailed calculations are used in the evaluation. Level 2 assessments are typically conducted by plant engineers or enginee ring special.ists experienced and knowledgeable in performing FFS assessments. • Level 3 - The assessmen t procedures included in th.is level are intended to provide the most detai led evaluation 1.2
that produces results that are less conservative than those from a Level 2 assessment. In a Level 3 assessment the most deta iled inspection and component information is typically required, and the recommended analysis is based on numerical techniques such as the finite clement method. The Level 3 assessment procedures are primarily intended to be used by engineering specialists experienced and knowledgeable in perfon ning FFS evaluations.
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7:1_ Andersu, , D.A. O.wge I lnrern(lfiOn(l/ Journ"l of Pressure V<ssels """Piping 77 (2(}0()) 953- 'MJ
2.5. Remaining life and rerating The FFS assessment procedures in API 579 cover both the present in tegrity of the component gi ven •• current stare of damage and the projected remaining life. Tf the results of a FFS assessment indicate that the equipment is suitable for the current opemting conditions. the equipment can continue to be oper.ned at these conditions. if a suitable inspection program is established. If !he resultS of the FFS assessment indicate that the equipment is not suitable for the current opemting conditions, calculat ion methods are provided in API 579 to rerate the component. For pressurized components (e.g. pressure vessels and piping) these calculation methods can be used to find a reduced maximum allowable working pressure and/or coincident temperature. For tank components (i.e. shell courses) the ca lculation methods can be used to determine u reduced Maximum Fill Height. The remuining life calcu lation in APT 579 is not intended to prov ide a precise est imate of the actual time to failure. Alternatively, the remui ning life calcu lation is used to establish an approprime inspection interval in conjunction with the governing inspection code and/or inservice monitoring plan, or the need for remediation.
2.6. Relations/tip to other FFS swndards As previously di scussed. of the MPC FFS JTP reviewed existing interm1tional FFS standards to detern1ine !he suitability for use in the refining and petrochemical industry. Although a ~ingle comprehensive standard did not exist. technology contained in these international standards was identified that could be utilized for certain flaw types. Where possible. parts of these methodologies were incorporaled into API 579. and in many cases they were significantly enhanced. In some cases. where the technology was not directly incorpomted. the APT CRE FFS Task Group felt that
3. Overview of API 579 crack-like flaw assessm ent Section 9 of API 579 covers the assessment of cr;1cks and other planar flaws. As is the case with other prominent procedures. such as R6 and OS 79 10, the failure assessment diagr.tm (FAD) methodology fom1s the basis of the flaw evaluation. Fig. l illustrates the FAD concept. The toughness ratio, K.- and the load mtio. /..,. for the structure of interest are plotted on the diagmm. The FAD curve represents the
predicted failure locus. If the assessment point f;•lls within the curve, it is considered acceptable. The roughness mtio is computed from the following expression:
K, = Kf + 4>K~R
(I)
K mao
where Kf is the applied stress intensity factor due to primary loads. K~R is the stress intensity factor due to secondary and residual stress. Krna~ is the fmcture toughnes . and 4> is a plasticity adjustment factor on K15 R. Note that the above fonnulation, whkh was recently suggested by Ainsworth et al. [ 12], differs somewhat from that in the current versions of R6 and BS 79 10, which for secondary and residual stress plasticity effects through the p factor. which is added ro K,. Eq. (I). which has a multiplying factor on KfR . is a more rigorous formu lation . Both the p and cl> formulations were derived from the same analyses. However, the p factor fomlUiation implies a toughness dependence on plastic zone formation, wh ich has no theoretica l bas is. T he more correct form forK, in Eq. ( I) will most likely appear in furure revisions of R6 and BS 7910. The load ratio in API 579 is def'ined ;._.;
L,
= u,.r .
(2)
Uys
where u ref is the reference srress ;md u 1, is the yield strength. Eq. (2) is identical to the 4 definition in R6 and BS 7910. However. API 579 proposes an alternative definition of the reference stress. as discussed later in this article. The main cr.tck-Jike flaw assessment in API 579 is Level 2, which uses !he following FAD equmion:
K,
= fl -
for L, ::::
0.14(4)2](0.3
+ 0.7 expf -
0.65(1...,)6 ])
(3)
4im:uJ·
which is !he same as the R6 Option I FAD, as well as !he one of the available Level 2 FAD expressions in BS 7910. This FAD has a cut-off at~"'"''' which is defined as
Lr(max)
= -I ( 2
I
u,. )'
+ -
(4)
U y,,.
where u,,, is the tensile strength. Fig. 2 shows a plot ofEq. (3) with typical cut-offs for various steels. Level2 util izes partial s afety factors (PSFs) on toughness, flaw size and stress. whereby the can select a t:1rget reliability and perfom1 a deterministic analysi s. If. after adjusting the input va lues by the PSFs. the assessment point lies inside the FAD. one can conclude that the actual probability of fai lure is less than the target value. The PSFs tabulated in Section 9 of API 579 were generated as part of tbe MPC FFS project (13]. The API 579 Level 3 assessment is a more advance analysis !hat gives the a subsmntial ••mount of flexibility. The
960
TL Anderson. D.A. Osa..~• I lnttrmuiontll Journal of Pr.ssure Vns<& am/ Piping 77 (2000) 953-963
available options for a Level 3 assessment include: • Method A - Level 2 assessment with -generated partial safety factors or a probabilistic analysis. • Method B - Material-specific FAD. similar to R6 Option 2. • Me thod C - J -based FAD obtained from clastic - pl;tstic finite element analysis, si milar to R6 Option 3. • Method D - Ductil e teari11g assessment. • Method E - Use a recognized assessment procedure. such as R6 orBS 7910. The Level I as e~sment is very simple screening evaluation that can be perfonned by a qualified inspector. Level I consists of a series of allowable flaw size curves. These curves were gcner.ucd using the Level 2 assessment with conservative input assumptions. l'ote that the APT 579 Level I asscssmcm of cracks is completely diffcrcnr than the BS 7910 Level I iiSSessment. The Iauer is u pseudo FAD ana lysis that is intended to mai ntain backward compatibility wi th the 1980 vc1·sion of the BS PD 6493 procedure. Unlike Level I of BS 79 10, the APT 579 Level I assessment requires almost no calcu lations.
tion. which can be used to infer K for an arbitrary throughwall stress field. The procedure for generating weight functions from the uniform and linear crack face pressures is outlined in Appendix C of APT 579. The range of dimensional paramerers for the cylinder 01nd sphere analyses is as follows:
• R;lt = 3, 5, 10. 20. 60, 100, oo. • all = 0.2, 0.4, 0.6. 0.8.
• cia= 0.5, I. 2, 4. 8, 16. 32. where R, is the inside hell radius. 1 is the wall thickness. a is the depth of the surface flaw. and 2c is the surface flaw length. Fig. 3 is a plot o f typical resultS from the recent analyses. Uniform crack face pressure was applied. giving a stress intensity solution of the following form:
(5) where p is the crack face pressure, G0 is a dimension less geometry fuctor, and Q is the flaw shape parameter:
a
Q =I+ 1.464 ( ~
)1.65
(6)
4. New K solu tions in API 579 Appendix C contains an extensive library of stress imensity solutio ns for cracked bodies. Many of these solutions were obtained from the published literature as well as other assessment procedures, including BS 7910. New K solutions were also generated for inclusion in APl579. Tn particular, a comprehensive set of solutions for c racks in cyli ndrical and spherical shells was recently developed [14]. Th is study involved over 2400 finite clemem runs. Of course. there were a number or existing solut ions for cylinders and spheres. bm these tended to cover a limited mnge of radius/thickness and flaw aspect ratios. ln a study commissioned by the MPC FFS project [14), the following geometries and Haw orientations were considered: • • • • • •
Internal axial surface flaws in a cylinder. External axial surface flaws in a cy linder. Interna l circumferential sUJ:face flaws in a cylinder. Ex ternal c ircumferential surface flaws in a cyl inder. Interna l meridiana! surface flaws in a sphere. External meridiana! surface flaws in a sphere. Three load cases were analyzed:
• Uniform crack f01ce pressure. • Linearly varying crack face pressure. • Global bending moment (circwnfcrcntial cr.tck.~ in cyl inders). The first 2 load cases can be used to derive a weight func-
Note that there is a significant R/1 efl'ect on the nondimcnsional stress intensity factor, G0• Consequently. using a K solution for a surt'<~ce cmck in a flat plate when assessing a curved shell could lead to significam errors. The K solurion libmry in APT 579 will be expanded as new cases become avai Iable. Currently. solutions for cy linders with R/1 = I arc being computed. ln the ncar future. K solutions for cracks at structural discontinuities such as noz2eles and stiffening rings wi ll be generated.
5. Fra cture toughness estimation Appendix F of API 579 eomains information on material properties. including 10ughness. This appeodix does not contain a database of toughness values, however. Rather. it provides correlations and estimation methods. For ferritic steels, there are lower-bound correlations of toughness to Charpy transition temperature. These correlations were adapted from Sections lTl and Xl of the ASME boiler und pressure vessel code. For static loading in the <~bsence of dissolved hydrogen. the lower-bound toughness correla tion is as follows:
K1c
= 36.5 + 3.084 exp[0.036(T- T,cr + 56))
(MP-a../iii.
(7a)
oq.
K1c = 33.2
+ 2.806 cxpt0.02(T- T,.r +
100)] (7b)
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1:1-. Amlcrson, D.A. Os<1ge I lnrern(l(iona/ Journal of Pressure v,ssels tmd Piping 77 (2000) 953- 963
2.5
·-
· -
.... _____ _
2
C)
0
..- . -
---6.
...
:· . - .. t.
----- ----------------e
1.5 Uniform Crack Face Pressure alt • 0.6 cJa s "12
= +=
Cylinder-Circumferential-lntemal - - ·~ - - Cyllnder-Circumferential-Extemal Cylincler-Axial-lntemal • Cylincler-Axial-Extemal ---.!.-- Sphere-Meridianal-lntemal .u Sphere-Meridianai-Extemal
0.5
0
0.05
0.1
0.25
0.2
0.15
0.3
0.35
t/R.I Fig. 3. Nondimensiona.l stress intensity factot· at the deepest point of a surface crack (
= 7rl2) as a funct ion of thickness/radius mtio in cylinders and spheres.
where Trer is the 20 J ( 15 ft-lb) tr-ansition temperature in the case of carbon steels. For dynamic loading or for hydrogen charged steels, the foll owing lower-bound correlati on can be used: 1
Km
= 29.5 +
1.344 exp[0.0260(T-
7~.r
+ 89)) (8a)
0
(MPaJffi, C),
K1R = 26.8 + 1.223 exp[0.0144(T-
7~cr
+ 160)) (8b)
(ksi.Jin.. 0 F}. An upper-shelf cut-off must be imposed on the above expressions. For older, high-su lfur steels. a cut-off of 11 0 MPaJffi (100 ksi.Jin.) is recommended. For newer, low-sulfur steels, a cut-off of 220 MPa.JiTI (200 ksi.Jin.) may be assu med. For probabil istic fracture analyses of steel structures, API 579 endorses the use of the fracture toughness Master Curve, as implemented in ASTM Standard E 1921-97 l l5]. The Master Curve quantifies the temperature dependence of steels in the transition range, as well as the statistical d istri bution of toughness at a given temperature. The lat.ter is characterized by a three-parameter We ibull di stri -
bution with two of the three parameters specified: F
=I-
K)c - 18.2 ) F = I - exp [ -8 ( Ko _ _ 18 2
4
]
4 ] (lllJll,
.
MPaJffi), (9a)
.
~
(m., ks1v111.),
(9b)
where F is the cumulative probability. 8 the specimen thickness (crack front length), and K0 is the Weibullmean toughness, wh.ich corresponds to the 63rd perceotile value. The temperature dependence of the median (50th percentile) toughness is given by KJc{median)
= 30 +
KJc{rncdiun1
= 27 + 64 exp[0.0106(T - To)] (ksi.Jin., "F),
70 exp[O.OI90(T- To)] (MPaJffi, "C), ( lOa)
( lOb) where To is the index transition temperature material for the material of interest. It corresponds to the temperature at which the median tOughness for a 25 mm ( l in.) th ick specimen is I00 MPaJiil (9 1 ks i.Jin.). The median and Wei bull mean are related as follows:
Ko= 1 The rationale for using a dynamic cra.ck iliTcst fracture toughness com> lalion for hydrogen charged steels is as follows: If dissoh•e d hydrogen is present, it may degrade the material's ahility to resisl brittle fracture i ni t ia~ tion. Once mpid crack propagation begins, however, lhc hydrogen can no longer inlluencc the 111atcrial behavior. Therefore, the cr•ck arre~t toughness should be a reasonable lower-bound estitnate of the mate1iaPs ability to resist unstable crack propagation.
[ B (K~c0-- 2020)
exp - - -2;,.4
Ko=
K Jc(mcdi.m) -
[ln(2)]0.25
20
+20
Kk(median) - 18.2 [In (2)]025
+ L8.2
(MPaJiU),
(ksiJin.).
( !Ia)
{II b)
By combining Eqs. (9a), (9b), (lOa), ( lOb) and ( II a), ( lib), we see that once T0 is known , the toughness in the transition
TL Anderson. D.A. Osa..~• I lnttrmuiontll Journal of Pr.ssure Vns<& am/ Piping 77 (2000) 953-963
962
region is completely described. ASTM E 1921 -98 outlines the procedure for determining To from fmcrure 10ughness test ing in the transition region. When fracture 10ughness testing is not feasible. To can be esti mated from the 27 J (20 ft-lb) rransition temperature:
To= T21 J
(12a)
18°C.
-
To = T2o 11 ·1~ - 32.4oF.
( 12b)
The above correlation has a standard deviation of approx imate! y I5°C (2'PF).
6. Refer ence strcs.~ and weld mismatch Appendix D of API 579 contains reference stress solutions for a variety of cracked bodies. Fo r the most part, these solutions were adopted directly from R6 and BS 79 10 and are bascu on lim it loau solutions. The authors believe that the current uefinition of refe re nce stress based o n li mit load is inappropriate and should be replaced in the long run. When rigorous c lastic- plastic J solution~ for cr;1cked bodies are plolted in of FADs. the resulting curves exhibit a strong geometry dependence when 4 is compute
~
( 13)
K, = v ---:~·
This is ploned against the load ratio. a.~ defined in Eq. (2). The potential geometry dependence of the FAD curve arises in the uefinition ofreference stress. A self-consistent defini tion of 1 can be derived from the R6 Option 2 FAD equation , wh ich is material-specific but is assumed to be geometry-independent. Setting L, = 1 in this expression leads to
u,.
- J-
I
_ £) -l = I+ 0.002£ +-I ( I + _0._002
}
CT) S
2
( 14)
fF) >
The above expression a.~sumes that u 1, is the 0.2% offset yield strength. The reference stress is linearly relate
H CTnuminal •
( 15)
where H is inferred from the nominal stress at
4 = I:
H = _ _u..!).:. • --
( 16)
Unomina:JIL,- 1 .
Thus. the refcrenuc stress is chosen in such a way that the Optj~n 2 FAD will nearly match a rigorous elastic-plastic J analysis. That is. give n the above definition of reference srress, Option 2 unci Option 3 FADs will be virtua lly identical. The forgoing begs the question: if an elastic- plastic J analysis is ncquircd to determi ne 4- wh
7. Residual stress distributions for FFS assessment One of the key assumptions in fracture assessments of welded structures is the residual stress distribution. Earlier assessment procedures. uch as PO 6493 (both the 1980 and 1991 versions). made the very conservative assumption of yield-magnituue membrane residual stresses in as wclue
1:1.. Arukmm. V.A. Osu,qe l lfllenwtionfll Jounwl of Pressure Vessels und f>ipi11g 77 (2000) 9SJ- 96J
project will ;tddress the following issues: • Confirmation of some of the parametric distributions in Appendix E. • A c lear criterion for electing 'bending' and 'self-equilibrating' type· of residual stress distributions in pipe/ vessel welds. • Development o f improved residual stress distributions for fillet welds at comer ts. nozzle welds. and repai r welds. • Tncorpomti on of local post-weld heat treatment e lfects.
963
as requ ired by the standards committee. Discussions are already in progress. and suggest ions have been made to have the new standards com mittee meet ings in conjunction with PVRC. This would help to create a focal point for FFS technology development in that the PVRC COE and MPC FFS JlP have previously met at this time. In addition. the of the standard~ committee could directly interface with of these groups to define technology needs and help arrange for appropriate fu nding levels.
References Appendix E will continually be expanded and revised as new results become available.
[I) API. Re<:onunended practice for litnc«·for·<el\ ice. API 579. \Vashington, DC: American Peunleum Jn,.l itule, 2000. 121 API. Pressure ves.~>el inspec1ion code: mainlenance in~peclion.
8. API and ASME FFS activities T he American Society of Mechanical Engineers (ASME) has formed a new main comm ittee, the Post ConsmJCtion Mai.n Committee. with a charter to develop codes and standards for in-service pressure containing equ ipment covering all industries. Curre ntly. standards development activity is underway in the areas of Risk-Based Inspection (RBI) and repair methods (e.g. leak seal ing. boxes, patches. etc.). Tn the area of FFS. API and ASME are working to create a new standards comminee that will tly produce a s ingle FFS standard in the US thai c;m be used for pressure containing equipment. It is envis ioned that once the negotiations and opemti ng procedures for the new committee srrucrure arc complete. API 579 will form the basis of the t APIJASME stand;trd that will be produced by this committee. The inili
rerating. repair and alteration. API 51 0. Vl u.;.hinglOn. DC: American Petroleum Institute. 1999. [3] API. Piping inspection code: in
[5) API. Recommended practice i'o•· risk· bascd inspcctitlll. API 580 (in development). \Vashing1on, DC: American Petroleum fno,; tilutc. PI'OCctlure~ rur operating pre~ surc vessels, tank.-;, and piping in renncl'y und chemical .~rvicc. FFS-26. New York. NY: The Material> Pt"l>pct·tic< Council. Ocwlx:r, 1995. British Energy. Assessment of the integrity of <tructure< containmg defects. Britislt Energy R-6. 1999. BSI. Guide on method< for O'<e"lng the acceptahiluy of flaw< 10 sttuc1ures. BS 7910. Briti
. t93J. l'alo Aho. CA: EPRI. 1981. Ainsworth RA. Sharples JK. Smith SO. EfTccts of rc:'
l
16l MPC. F'itncss-ror-servic.:c cvaluutiun
(7]
[81 (91 110]
1111 I t2]
[ 13]
2000. [ 14) Anderson TL, ·n-.orwaltl GV. Revelle 0 .1 . Strc« intcn
surface cracks and bw·ied t racks in cylinders, sphere~. and nmplmes. Presented at the 2000 ASME l'ressu1'C Vessel and Piping Conference,
Seattle. July. 2()()(). [ 15] ASTM E 192 J -97 St:111dard 1<.>1 method for detct'lllination of reference 1emperatu1'e. T0 • liJt fe•·ritic steels In the trnn