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压力管道培训之材料8管道施工及验收规范(Materialsfor
pressurepipingtraining-8pipingconstructionand
acceptancespecification)
Pressurepipingtrainingmaterials8pipingconstructionand
acceptancespecification.Txtmenshouldbegratefultowomen
whoaremorethan20yearsoldwiththeirownside.Because20
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Pressurepipingmaterialpart
Eighthchapters
Codeforconstructionandacceptanceofpipelines
Firstpages,9pages
8codeforpipingconstructionandacceptance
8.1codeforcomprehensiveconstructionandacceptance8.2
classificationofpipelines(grades)pipingclassification
8.2.1SH3501-2002pipelineclassification-8.2.2HG20225-95
pipelineclassification-8.2.3GB50235-97
8.3requirementsforradiographicinspectionofweldedjoints
Requirementsforradiographicinspectionof8.3.1SH3501-2002
weldedjoints-Requirementsforradiographicinspectionof
8.3.2HG20225-1995weldedjoints-Requirementsfor
radiographicinspectionof8.3.3GB50235-97weldedjoints-
8.3.4,SH3501,HG,20225,GB50235comparison,
8.4pipingpressureandsealingtest
8.4.1pipes;liquidtests;pressureandgastests;pressure
pipes;liquidtests;pressureandgastests;pressure;8.4.2;
sealingtests
Eightpointfive
Scopeofapplicationofconstructionacceptancespecification
Pressurepipingmaterialpart
Eighthchapters
Codeforconstructionandacceptanceofpipelines
Secondpages,9pages
8specificationforconstructionandacceptanceof8.1
comprehensivespecificationforconstructionandacceptanceof
GB50235-97-GB50236-98-industrialmetalpipeline
engineeringconstructionandacceptanceoffieldequipment,
fieldequipment,industrialpipeweldingengineering
constructionandacceptancespecification
SH3501-2002petroleumchemicaltoxicandcombustiblemedium
pipingengineeringcodeforconstructionandacceptanceofoil
-toxicchemical,qualityinspectionandassessmentofHG
20225-95chemicalmetalpipeconstructionandacceptance
specification-FJJ211-86-GB50184-93jacketedpipe
constructionandacceptancespecificationforindustrialmetal
pipelineengineeringstandard
SH/T3517-2001petrochemicaltechnicalstandardfor
constructionofsteelpipelineengineeringGBJ126-89-
SY/T0420-97-HGJ229-91-industrialequipmentandpipeline
insulationengineeringconstructionandacceptance
specificationofburiedsteelpipelinesofpetroleumasphalt
coatingtechnologystandardofindustrialequipment,
industrialequipment,codeforconstructionandacceptanceof
pipelineanti-corrosionengineering
SH3022-1999paintofpetrochemicalequipmentandpipeanti-
Technicalspecification-TechnicalSpecificationfor
corrosion-SH3010-2000petrochemicalequipmentandpiping
insulationCCJ28-89-CJJ/T81-98CJJ33-89-cityheating
networkconstructionandacceptanceofurbanburiedheating
pipetechnicalspecificationforgastransmissionand
distributionengineeringconstructionandacceptance
specification
8.2pipelineclassification(class)classification(in
pipelineconstructionandAcceptanceCodesindifferentmedium,
differentoperatingconditionsofthepipelineinspection
requirementsaredifferent.Intheconstructionandacceptance
specification,differentmedium,differentoperating
conditionsofthepipelineinspectionrequirementsare
different.8.2.1SH3501-2002-SH3501pipelinepipeline
classificationSHA,SHB,SHC,SHDfourgrades.
Pressurepipingmaterialpart
Eighthchapters
Codeforconstructionandacceptanceofpipelines
Thirdpages,9pages
Table8-1pipelevelSHA1.,2.,3.,1.,2.,3.,1,,2.
SH3501-2002pipelineclassification-
SHBSHCSHD
Thescopeofutmosthazardmediumpipeline(exceptbenzene
pipeline)toxicityofpropylenehighhazardmediumfine,
phosgene,carbondisulfideandhydrogenfluoridemedium
pressurepipelineisgreaterthanorequalto10.OMPa
transportingtoxic,combustiblemediumpipingfortoxicityof
benzenepipingtoxicityofextremelyharmfulmediumforhigh
hazardmediumpipeline(acrylonitrile.Phosgene,carbon
disulfideandhydrogenfluoridegroupA,b)pipelineexcepta
combustiblegasandaliquidhydrocarbon,akindofB,
ClassBflammableliquidmediumpipinghasamoderatetoxicity,
slightlyharmfultomedium,piping,typeB,classBflammable
liquidmedium,piping
Cryogenicpipewithtemperaturelowerthan-29
8.2.2HG20225-95pipelineclassification-HG20225-95divides
thepipeintofourgradesA,B,C,D--table8-2--
Conveyingnoncombustiblemediumcombustibleortoxicmedium
pipelinepipelinelevelABCDformediumrangetransportof
highlytoxicandnon-toxicnoncombustiblemediumpiping
conveyingmedium,mediumpressurepipelinedesignPnoless
thanIMPa,andthedesignofpipelinetemperatureof-29to186
DEGC
HG20225-95pipelineclassification-
8.2.3GB50235-97cancelledpipelineclassification,according
tothedesigntemperature,designpressureandmediumclass
distinction1)designisdividedinto:ttemperaturemorethan
400DEGC,-29=t<400C,t<-29;2)thedesignpressureis
dividedinto:P=10.OMPa(lessthan42),P<10.0MPa,4P<10.0
MPa,P<4.0MPa,3)medium:highlytoxic,toxicandcombustible
medium,non-toxic,noncombustiblemedium(GB5044)
Note:the''occupationofGB5044mediumtoxicexposuretotoxic
substancesintheIratingof"harmdegreeofthemedium;toxic
mediumaccordingtotheGB5044''occupationofexposuretotoxic
substancesclassification"inIIandthefollowingdamage
medium;combustiblemediumaccordingtotheGB50160"codefor
fireprotectiondesignofpetrochemicalenterprises7'
classification
8.3radiographicinspectionrequirementsforweldedjoints一
Requirementsforradiographicinspectionof8.3.1SH3501-2002
welds-
Pressurepipingmaterialpart
Eighthchapters
Codeforconstructionandacceptanceofpipelines
Fourthpages,9pages
Table8-3
Pipelinelevel
RequirementsforradiographicinspectionofSH3501-2002welded
joints
ThedesignofPMPatransmissionmediumpressure(table)any
pressureP=10,4=P<10.0P<10.0P<4.0P<10.0P<4.0P<10.0
P<4.04P<10.0arbitrarypressuredesigntemperaturedetection
IIIIII%qualifiedforIIIIIIIIIIIIIIIIII
SHA
Utmosthazardmedium(exceptbenzene)anddegreeoftoxicity
ofpropylenehighhazardmediumfine,phosgene,carbon
disulfideandhydrogenfluoridealltoxicandcombustible
mediumalltoxicandcombustiblemediumutmosthazardmedium
benzenetoxicity,highhazardmedium(acrylonitrile,phosgene,
carbondisulfideandhydrogenfluorideexcept)aClassAand
classaclassBflammableliquidhydrocarbon,gasandaBclass,
aclassBflammableliquidtoxicitylevelismoderate,mildand
mediumhazardclassB,classCcombustiblemediumtoxic,
combustiblemedium
B
AnytemperatureanytemperatureT=400-29=t<400t=400,
-29=t<400t=400,t=400,-29=t<400t=400T<-29
10010010020201010,10055100
SHB
SHCSHD
TheSH3501consideredthecharacteristicsofpetrochemical
industryofhypertoxicandcombustiblemediumpipingmade
detailedprovisions.Noncombustible,jointX-raydetection
requirementsforapprovalinaccordancewiththerequirements
ofGB50235non-toxicmediumwelding.
8.3.2
RequirementsforradiographicinspectionofHG20225-1995
weldedjoints一
Table8-4-
Requirementsforradiographicinspectionofweldedjointsof
HG20225-1995-Requirementsforradiographicinspectionof
weldedjoints
Designpressure(P)(MPa)(table)anypressuredesign
temperature(T)Carbitraryt=400t<400t=400t<400t=400
T<400t=400t<400t=400T<400t=400T<400t=400186<t<400
-29=t=1865III10III510020IIIIIII10II20detection
ofII%oftheproportionof100100qualifiedgradeIIII
PipelinecategoryA(highlytoxic)BlB2B3B4ClC2C(non
flammablenon-toxic)C3C4C5D(nonflammablenon-toxic)
P=10,4=P<10.04=P<10.01=P<4.01
B(flammable,toxic)
Note:(1)whenthedesigntemperatureist<-29degrees,no
matterwhichlevelofpipeline,shouldbe100%inspection,
IIlevelqualified;(2)oxygenpipelineinspectionbyclassB
pipeline
Pressurepipingmaterialpart
Eighthchapters
Codeforconstructionandacceptanceofpipelines
Fifthpages,9pages
8.3.3
RequirementsforradiographicinspectionofGB50235-97welded
joints-table8-5requirementsforradiographicinspectionof
GB50235-97weldedjoints-
Serialnumber123456
Themediumthatcarrieshighlytoxicfluids,alltoxicand
combustiblemedia,nonflammablefluids,non-toxicfluids,
pipes,cryogenicpipes,nonflammablefluids,non-toxicfluids,
pipes,otherpipes
DesignpressureMPa(table)anypressureP=10,4=P<10.0P
=10,P=1,anypressure
Designtemperatureofarbitrarytemperatureatanytemperature
T=400,t=400T<-29t=400
Detect%
Qualificationlevel
Onehundred
II
05III
8.3.4SH3501,HG20225,GB50235,a.thesamepointweredetected
onthefollowing100%raypipe;1)toxicmedium;2)of
hypertoxicandcombustiblemediumPismorethan10atany
temperature
4=P<10.0,t=400,C3)nonflammable,non-toxicmediumP>
10,4)B.SH35011lowtemperaturepipeline)ontheflammable
highhazardmediumbythemediaisdividedintotwotypes:
benzenetoxicity,highhazardmedium(acrylonitrile,phosgene,
carbondisulfideandhydrogenfluorideandexcluded)aclass
ofliquefiedhydrocarbonP<10.0linedetectionratewas20%;
theclassA,classBflammablegasandaBclass,aclassB
flammableliquid-29=t<400CandP<4.0t=400,t=400t<-29
pipeshotcc
Pressurepipingmaterialpart
Eighthchapters
Codeforconstructionandacceptanceofpipelines
Sixthpages,9pages
P<10.02)
-29=t<400CandP<4.0
T=400,thepipelineX-raydetectionratewas10%;
Thedegreeoftoxicitywasmoderate,mildandmediumhazardB
classB,classCP<10.0-29combustiblemediumislessthanor
equaltot<400DEGCandP<4.0t=400,thepipelineX-ray
detectionratewas5%;
3)ofnonflammable,non-toxicmediumpipingnotprovidedfor
HG20225ofcombustibleandpoisonousmediumaccordingtothe
operatingconditionsaredividedinto3kindsof0P<10.0t<400
and1P<4.0t=4001
Pressurepipingmaterialpart
Eighthchapters
Codeforconstructionandacceptanceofpipelines
Seventhpages,9pages
Thepressureof1.15times,andnotlessthanthetestpressure
equipmentpipelinedesignpressure,withtheconsentofthe
constructionunit,canbetestedaccordingtothetestpressure
ofequipment;3)whenthedesigntemperatureofthepipeline
ishigherthanthetesttemperature,thetestpressureshall
becalculatedasfollows:Ps=1.5P[]l/[]2insigmasigma;Ps
testpressure(11MPa;P,g)11designpressure(gauge),MPa;
[Sigma]111testtemperaturematerialallowablestress,MPa;
[Sigma12-designtemperaturematerialallowablestress,when
MPa.]l/[[sigmaSigma12isgreaterthan6.5,6.5.whenPsattest
temperatureproducestressexceedingtheyieldstrength,the
maximumtestpressurePstonotexceedtheyieldstrengthwhen
thepressureexceedsthemaximum;yieldstrength;4)onthe
greatdifferenceofthepipelineshouldbeincludedinthe
staticpressuretestmediumpressuretest.Thetestpressure
ofliquidpipelineshouldbethehighestThepressureis
accurate,butthelowpressurepipingcomponentsshallnot
exceedthebearingcapacity;5)ofpipelinesubjectedto
externalpressure,thetestpressureshouldbedesignedwithin
1.5timesthepressuredifference,andnotlessthan0.2MPa;
6)todeterminethehighpressurecasingpipeclamptestshould
betheinternalorexternaldesignpressure.Testtubeclamp
casingshouldbeaccordingtotheprovisionsofarticle(1).
ThetestpressureofB.gas.1)undertheinternalpressureof
thesteelandnonferrousmetalpipepressuretestpressure
shallbe1.15timesthedesignpressure,testpressurevacuum
pipeshouldbe0.2MPa.2)whendesignofpressurepipelineis
greaterthan0.6MPa,theremustbespecifiedinthedesign
documentorbythedesignunittoavailablepressurefor
pressuretest.
Pressurepipingmaterialpart
Eighthchapters
Codeforconstructionandacceptanceofpipelines
Eighthpages,9pages
TheprovisionsofSH35011)forvacuumpiping0.2MPa;2)the
pressureofthehydraulicpressuretestfor1.5times;3)the
pressureoftheairpressuretestfor1.15timesthedesign.
4)pipelinepressuretest,testtemperature,stressvalueshall
complywiththefollowingprovisions:whenthedesign
temperatureishigherthanthetesttemperature,testpressure
pipingshal1becalculatedaccordingtothefollowing:Pt=KP0
[]1/[sigmaSigma]2typePt11testpressureMPa;[11o]1test
temperaturetheallowablestress,MPa[11;Sigma]2design
temperatureundertheallowablestress,MPa;K-coefficient,
liquidpressuretest1.5;gaspressuretestthestressvalue
of1.15.liquidpressuretest,shallnotexceed90%oftheyield
pointofthematerialundertesttemperature;airpressuretest
shallnotexceed%yieldpointofmaterialundertest
temperaturewhenthestressvalueshallnotexceedtheyield
pointofthematerialundertesttemperature80%.Morethan
materialtesttemperatureyieldHG20225andGB50235pointCJJ
33-89%isbasicallythesameastheprovisionsofthe1)gas
pipelinestrengthtestpressureshallbe1.5timesthedesign
pressure,steelpipeshallnotbelessthan0.3MPa;thecast
ironpipeshallnotbelessthan0.05MPa;2)strengthtest
pressureregulatoratbothendsoftheauxiliaryequipmentand
pipingshallbe1.5timesofthedesignpressuresealtest;
8.4.2C.shouldbeGB50235:pipelineleakagetestfor
transportingtoxicfluid,toxicfluid,mustbecarriedout
for.SHAlevelpipelinecombustiblefluidpipelineSH3501:
accordingtotherequirementsofdesigndocuments,SHBpipeline
accordingtothenatureofmediadecision
Pressurepipingmaterialpart
Eighthchapters
Codeforconstructionandacceptanceofpipelines
Ninthpages,9pages
HG20225:GB50235B.GB50235:testmediumshouldbeusedinair,
whenspecifiedinthedesigndocumentbyothermedia,according
tothedesignrequirementsofmediumSH3501:shouldadoptthe
ai
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