压力管道培训之材料8管道施工及验收规范_第1页
压力管道培训之材料8管道施工及验收规范_第2页
压力管道培训之材料8管道施工及验收规范_第3页
压力管道培训之材料8管道施工及验收规范_第4页
压力管道培训之材料8管道施工及验收规范_第5页
已阅读5页,还剩10页未读 继续免费阅读

下载本文档

版权说明:本文档由用户提供并上传,收益归属内容提供方,若内容存在侵权,请进行举报或认领

文档简介

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

yearsoldisthelowestpointinaman,slife,nomoney,no

career;and20yearsold,butitisthemostbrilliantwoman,s

lifeseason.Aslongasthehoedancewell,whichcornercan

notdig?Thisarticleiscontributedbywangkui0574

DOCdocumentsmayexperiencepoorbrowsingontheWAPside.It

isrecommendedthatyoufirstselectTXT,ordownloadthesource

filetothelocalview.

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

温馨提示

  • 1. 本站所有资源如无特殊说明,都需要本地电脑安装OFFICE2007和PDF阅读器。图纸软件为CAD,CAXA,PROE,UG,SolidWorks等.压缩文件请下载最新的WinRAR软件解压。
  • 2. 本站的文档不包含任何第三方提供的附件图纸等,如果需要附件,请联系上传者。文件的所有权益归上传用户所有。
  • 3. 本站RAR压缩包中若带图纸,网页内容里面会有图纸预览,若没有图纸预览就没有图纸。
  • 4. 未经权益所有人同意不得将文件中的内容挪作商业或盈利用途。
  • 5. 人人文库网仅提供信息存储空间,仅对用户上传内容的表现方式做保护处理,对用户上传分享的文档内容本身不做任何修改或编辑,并不能对任何下载内容负责。
  • 6. 下载文件中如有侵权或不适当内容,请与我们联系,我们立即纠正。
  • 7. 本站不保证下载资源的准确性、安全性和完整性, 同时也不承担用户因使用这些下载资源对自己和他人造成任何形式的伤害或损失。

评论

0/150

提交评论