Minimum Design Metal Temperature Results Summary
工程图常见英文
施工图中英文对照词汇表2008-07-28 21:54目录1. 密封元件1.1 法兰、法兰盖1.2 螺栓、螺母1.3 垫片1.3.1 常用1.3.2 高压设备用2. 基础构件3. 梯子平台4. 设备常用零部件4.1 筒体封头4.2 支座4.2.1 鞍座、耳座裙座其它支座4.3 主要零部件5. 换热器专用名词6. 塔专用名词7. 图面节点术语及图面常用语7.1 节点术语7.2 图面常用语8. 技术要求及特性表中常用语9. 常用技术要求的英文译法10. 常用介质11. 其他1 密封元件1.1 法兰、法兰盖1）对焊法兰：WELDING NECK FLANGE2）平焊法兰：SLIP-ON FLANGE3）衬环法兰：CLADDED FLANGE4）突面法兰：RAISED FACE FLANGE (RF FLANGE) 5）凸面法兰：MALE FLANGE (M FLANGE)6）凹面法兰：FEMALE FLANGE (FM FLANGE)7）榫面法兰：TONGUE FLANGE (T FLANGE)8）槽面法兰：GROOVE FLANGE (G FLANGE)9）法兰盖：BLIND FLANGE1.2 螺栓、螺母1）螺栓：BOLT2）双头螺柱：STUD3）螺母：NUT1.3 垫片GASKET1.3.1 常用1）石棉橡胶板：ASBESTOS SHEET (OR GASKET)2）缠绕垫：SPIRAL WOUND GASKET3）橡胶垫：RUBBER GASKET4）金属包垫：METAL JACKETED GASKET5）石墨垫：GRAPHITE GASKET6）聚四氟乙烯：PTFE. GASKET(POLYTETRAFLUOROETHYLENE GASKET) 1.3.2 高压设备用1）铝平垫：ALUMINIUM PLAT GASKET2）透镜垫：LENS RING3）齿形垫：TOOTHED GASKET4）椭圆垫：OVAL RING5）八角垫：OCTAGONAL RING6）Ω垫：“Ω” GASKET7）双锥垫：CONICAL RING GASKET2 基础构件1）地脚螺栓：ANCHOR BOLT2）模板：TEMPLATE3）锚板：ANCHOR PLATE4）基础构件：FOUNDATION COMPONENT5）筋板：RIB3 梯子平台1）梯子：LADDER2）平台：PLATFORM3）钢隔板：GRATING4）槽钢梁：CHANNEL BEAM5）立柱：POST6）扶手：HANDRAIL7）扁钢：PLAT BAR8）踏步：LADDER RUNG9）连接板：CONNECTION PLATE (OR LUG)10）安全门：SAFETY CHAIN (链式) OR BAR11）角钢：ANGLE STEEL4 设备常用零部件4.1 筒体、封头1）椭圆封头：HEAD2）平盖：PLAT COVER3）半球形：HEMISPHERICAL HEAD4）碟形封头：DISHED HEAD5）锥形：CONICAL HEAD6）折边锥形：FLANGED & CONICAL HEAD7）锥段：CONICAL SECTION8）筒体：SHELL9）多层包扎筒体：LAYERED SHELL10）内筒：INNER SHELL11）层板：LAYER PLATE4.2 支座4.2.1 鞍座：SADDLE耳座：SUPPORT LUG (OR BRACKET) 1）垫板：WEAR PLATE (OR PAD)2）底板：BASE PLATE3）筋板：RIB4）腹板：CELIAC PLATE4.2.2 裙座1）筒体：CYLINDER2）盖板：COVER PLATE3）底板：BASE PLATE4）垫板：PAD5）筋板：RIB6）通气孔：VENT HOLE7）进出口：ACCESS OPENING4.2.3 其他支座1）腿座：SUPPORT LEG4.3 主要零部件1）接管：NOZZLE2）管台：NECK3）补强圈：REIN. RING4）加强圈：STIFF. RING5）铭牌：NAME PLATE6）接地板：EARTH LUG7）防冲板：IMPINGEMENT BAFFLE8）防涡流挡板：VORTEX BREAKER9）液位计：LEVEL GAUGE10）视镜：GLASSES11）补强管：REIN. NOZZLE12）筋板：RIB13）弯头：ELBOW14）管：PIPE15）垫板：PAD PLATE16）人孔：MANHOLE17）手孔：HANDHOLE18）组合视镜：COMBINED GLASSES19）内爬梯：INTERNAL LADDER20）内部扶手：INTERNAL HANDRAIL21）垫圈：WASHER22）吊耳：LIFTING LUG23）管轴式吊耳：LIFTING TRUNNIONS24）板式吊耳：PLATE LIFTING LUG25）内件：INTERNALS26）支承圈：SUPPORT RING27）夹、卡子：CLIP28）保温圈：INSULATION SUPPORT RING 29）弯管：BEND PIPE30）防火螺母：FIREPROOF NUT31）角钢：ANGLE STEEL32）管帽：PIPE CAP33）凸缘：PAD34）丝堵：THREADED PLUG35）一般挡板：BAFFLE36）预焊件：PREWELDED PARTS37）管架：PIPE RACK38）安全阀：SAFETY VALVE39）除沫器：DEMISTER40）激冷环：QUENCH RING41）下降管：DOWNCOMER42）溢流管：OVERFLOW NOZZLE43）螺钉：SCREW44）铆钉：RIVET45）锚栓：ANCHOR46）销钉：PIN47）夹具：JIG48）填料箱：PACKING BOX49）填料压盖：PACKING GLAND50）填料：PACKING51）锥顶：CONE ROOF52）拱顶：COVE ROOF53）加热盘管或蛇管：COIL54）壁板：SHELL PLATE55）底板：BASE PLATE56）边缘板：SIDE PLATE57）中幅板：MIDDLE PLATE58）液封槽：LIQUID SEAL59）消防装置：FIREFIGHTING DEVICE 60）排水槽：DRAIN61）夹套筒体：JACKET SHELL62）夹套封头：JACKET ELLIP HEAD63）插入管：SETIN NOZZLE64）复合板：CLAD PLATE65）衬里：LINING66）堆焊层：DEPOSITED LAYER67）高压筒体端部：SHELL END FLANGE68）高压螺栓：HIGH TENSION BOLT5 换热器专用名词1）管束：BUNDLE2）管板：TUBESHEET3）折流板：TRANSVERSE BAFFLE4）弓形折流板：SEGMENTAL BAFFLE5）支持板：SUPPORT PLATE6）换热管：TUBE7）定距管：SPACER8）挡管：DUMMY TUBE9）拉杆：TIE ROD10）防冲板：IMPINGEMENT BAFFLE11）滑道杆：GUIDE ROD (BAR)12）旁路挡板：SEAL STRIP13）分程隔板：PASS PARTITION14）壳体纵向隔板：LONGITUDINAL BAFFLE15）密封条：SEAL STRIP16）U形管：U TUBE17）中间分流挡板：INTERMEDIATE BAFFLE18）浮动管板：FLOATING TUBESHEET19）浮头盖：FLOATING HEAD COVER20）浮头盖法兰：FLOATING HEAD COVER FLANGE21）钩圈：BACKING DEVICE22）平盖管箱：CHANNEL23）凸形封头管箱：CHANNEL24）外头盖：SHELL COVER25）防送支耳：ANTI-LOOSENING LUG26）防松螺栓：ANTI-LOOSENING BOLT27）环首螺钉：EYE BOLT28）顶丝：JACK SCREW29）膨胀节：EXPANSION JOINT30）波纹膨胀节：BELLOWS EXPANSION JOINT31）排污口：DRAIN32）放空口：VENT33）堰板：WEIR34）釜式锥段：CONICAL SECTION35）偏心锥段：ECCENTRIC CONICAL SECTION36）鞍座间调整垫板：SHIM PLATE6 塔专用名词1）塔盘：TRAY2）吊柱：DAVIT3）支持圈：SUPPORT RING4）降液管（板）：DOWNCOMER5）填料：PACKING6）填充物：FILLING7）分布器：DISTRIBUTOR8）再分布器：REDISTRIBUTOR9）泡罩：BUBBLE CAP10）浮阀：FLOATING VALVE11）溢流堰：OVERFLOW WEIR12）受液堰：SEAL PAN13）入口堰：INLET WEIR14）出口堰：OUTLET WEIR15）筛板：SIEVE PLATE16）内件：INTERNALS17）限位板：STOPPER18）拉杆：TIE ROD19）防溅溢流板：DECK20）碎流挡板：STREAM BREAKER21）预焊件：PREWELDED PART22）管架：BRACKET23）栅板：GRATING24）支承块：SUPPORT BLOCK25）就位吊耳：RETAINING LUG7 施工图图面节点术语及图面常用语7.1 节点术语1）壳体纵环焊缝：L&C WELD OF SHELL2）接管与筒体封头焊缝：NOZZLE “A” TO SHELL (HEAD) JOINT 3）接管与法兰焊缝：NOZZLE “A” TO FLANGE JOINT4）带补强圈接管与筒体封头焊缝：NOZZLE WITH REINF . RING TO SHELL(HEAD) JOINT5）管口方位图：NOZZLE ORIENTATION6）××剖面图：SECTION “××”7）××向视图：VIEW “××”8）法兰与筒体焊缝：FLANGE TO SHELL JOINT9）管板凸缘与筒体焊缝：TUBESHEET TO SHELL JOINT10）管支承拉筋详图：RIB DETAIL OF NOZZLE “A”11）搭接焊缝：LAP WELD12）搭接角焊缝：LAP FILLET WELD13）焊后磨平：RUBDOWN AFTER WELDING14）氩弧焊：TIG（TUNGSTEN-INERT-GAS）ARC WELD15）着色检测：PENETRANT EXAMINATION16）磁粉检测：MEGNETIC EXAMINATION17）×××详图：DETAIL OF ×××18）“U”与“U”焊缝：“U” TO “U” WELD JOINT19）“A”向折流板布置图：VIEW “A” BAFFLE ARRANGEMENT20）换热管与管板连接：TUBE TO TUBESHEET JOINT21）强度焊：STRENGTH WELDED22）密封焊：SEAL WELDED23）强度胀：STRENGTH EXPANDED24）贴胀：LIGHT EXPANDED7.2 图面常用语1）装配图：ASS’Y DWG2）部件图：COM’T DWG3）零件图：PARTS DWG4）零部件图：PART & COM’T DWG5）内件图：INTERNALS DWG6）外部构件图：EXTERNALS DWG7）剖面：SECTION8）详图：DETAILS9）俯视图：VERTICAL VIEW10）侧视图：LATERAL VIEW11）固定端：FIXED SIDE12）滑动端：SLIDING SIDE13）镇静钢：KILLED STEEL14）沸腾钢：RIMMED STEEL15）不锈钢：STAINLESS STELL16）双向钢：DUPLEX STEEL17）热轧的：HOT-ROLLED18）冷轧的：COLD-ROLLED19）淬火的：QUENCH20）正火的：NORMALIZE21）退火的：ANNEAL22）回火的：TEMPER23）固溶：SOLUTION24）可拆的：REMOVABLE25）手工电弧焊：SMAW (SHIELDED METAL ARC WELD) 或MMAW (MANUAL METAL ARC WELD) 26）埋弧焊：SUBMERGED ARC WELD27）定位焊：TACK WELD28）点焊：SPOT WELD29）连续焊：CONTINUOUS WELD30）间断焊：INTERMITTENT WELD31）焊后热处理：PWHT (POST WELD HEAT TREATMENT) 32）红丹：RED-LEAD33）镀锌：GALVANIZATION34）酸洗钝化：PICKLING35）泪孔：WEEP HOLE36）半圆孔：SEMICIRCLE37）长圆孔：LONG ROUND HOLE38）对开：OPPOSITE ORIENTED39）削薄过渡：TAPERED TRANSITION40）与封头内壁吻合：AS PER LOCATED INNER SUREFACE OF HEAD41）组焊后加工：MACHINED AFTER WELDING42）法兰密封面待组焊后加工：THE FLANGE SEAL SURFACE SHALL BE MECHINED AFTER WELDING 43）安装就位后点焊：SPOT-WELDED AFTER INSTALLATION44）热处理后加工：MECHINED AFTER PWHT45）（由）制造厂（决定）最终尺寸：FINAL DIMENSION BY MANUFACTURER46）衬里和填充料重量：LINING AND FILLING WEIGHT47）修改版次：REVISION48）标记：MARKED49）管口标高、尺寸和等级：ELEVATION SIZE AND RATING OF NOZZLES8 技术要求及特性表中常用语1）FLUID (OR MEDIUM)：介质2）FLAMMABLE：易燃3）HAZARDOUS：危害性的4）TOXIC：毒性5）LETHAL：致死的6）SPEC. GRAV.：密度（填充物的）7）DEW POINT：露点8）DESIGN PRESSURE：设计压力9）DESIGN TEMPERATURE：设计温度10）OPERATING PRESSURE (TEMPERATURE)：操作压力（温度）11）MAX OPERATING PRESS & TEMPERATURE：最大操作压力（温度）12）JOINT EFFICENCY：焊接接头系数13）CORROSION ALLOWANCE：腐蚀裕度14）INSULATION THICKNESS (WARM/COLD/SOUND)：保温层厚度（暖、冷、声）15）ULTROSONIC EXAMINATION：超声波检测16）RADIOGRAPHIC EXAMINATION：射线检测17）HYDROSTATIC TEST：水压试验18）PHNEUMATIC TEST：气压试验19）LEAKAGE TEST：气密性试验20）KEROSENE LEAKAGE TEST：煤油渗透试验21）AMMONIA GAS LEAKAGE TEST：氨渗透试验22）HEAT TRANSFER AREA：换热面积23）TRIANGULAR PATTERN：三角形排列24）SQUARE PATTERN：正方形排列25）SAFETY VALVE SET PRESSURE：安全阀启跳压力26）RUPTURE DISK BURSTING PRESSURE：爆破膜爆破压力27）NET WEIGHT：净重N.W28）EMPTY WEIGHT：空重 E.W29）WEIGHT WITH WATER：充水重30）TOTAL WEIGHT：总重T.W31）VACUUM：真空32）FULL VACUUM：全真空F.V33）CAPACITY：容积34）MINIMUM DESIGN METAL TEMPERATURE：MDMT最低金属应力温度35）INTERGRANULAR CORROSION TEST：晶间腐蚀试验36）IMPACT TEST：冲击试验37）IMPACT SPECIMEN：冲击试样38）CHARPY IMPACT TEST：夏比冲击试验39）MINIMUM IMPACT ENERGY：最小冲击功40）V-NOTCH：V型切口9 常用技术要求的英文译法1）采用锻件按JB4726 II级为合格：FORGING MATERIAL SHOULD BE APPLIED AND INSPECTED AS II OF JB4726 REQUIREMENTS2）焊接采用电焊，焊条牌号为×××：SMAW SHALL BE APPLIED, AND THE ELECTORDE TYPE IS ×××3）补充技术要求：SUPPLEMENT TECHNICAL REQUIREMENTS4）未注明角焊缝焊角高度按较薄板厚度：UNLESS OTHERWISE SPECIFIED, THE FILLET WELD LEG SIZE SHALL BE EQUAL TO THE THICKNESS OF THE THINNER PLATE TO BE WELDED ON.5）板材以正火状态供货：THE STEEL PLATE (可填具体材料) SHALL BE SUPPLIED AS NORMALIZED CONDITION6）除图中注明外，焊接接头型式及尺寸按HG20583-1998中规定，法兰的焊接按相应法兰标准规定：UNLESS OTHERWISE SPECIFIED IN THIS HEREIN DWG, THE WELD TYPES AND DIMENSIONS SHALL BE AS PER STIPULATED IN HG20583-1998, AND PIPE(OR NECK) TO FLANGE JOINTS AS PER RELEVANT FLANGE STANDARDS REGULATIONS7）未注圆角为Rx：UNLESS OTHERWISE SPECIFIED, THE ROUND RADIUS IS Rx8）未注倒角为××：UNLESS OTHERWISE SPECIFIED, THE DIMENSION OF CHAMPER IS ××9）“A”与“B”配钻：“A” SHALL BE DRILLED WITH “B” TOGETHER10）“A”与“B”对中：SAME AXIES FOR “A” AND “B”11）含××半圆孔：×× SEMICIRCLE HOLES COUNTED10 常用介质1）HYDROGEN：氢气2）OXYGEN：氧气3）NITROGEN：氮气4）CARBON OXIDE：一氧化碳5）CARBON DIOXIDE：二氧化碳6）HYDROGEN SULFIDE (H2S)：硫化氢7）AMMONIA (NH3)：氨8）METHANOL：甲醇9）INERT GAS：惰性气10）LPG(LIQUEFIED PETROLEUM GAS)：液化石油气11）SOUR GAS：酸性12）ALKALIZATION WATER(ALKALIZED WATER)脱盐水：13）SYNGAS (OR SYNTHESIS GAS)：合成气14）SHIFTED GAS：变换气15）RECYCLE GAS：循环气16）POLYMETER：聚合物17）DIESEL：柴油18）METHANE：甲烷19）RESIDUE OIL：渣油20）CRUDE OIL：原油11 其他1）LIST OF ATT. DOC. NO. ：附表号2）ORIENT. OF NOZ. DOC. NO. ：管口方位文件号3）PROJ. NO. ：项目号4）PROCESS DATA SHEET：工艺数据表5）PERSONNEL PROT：人员保护6）FIRE PROOFING：防火LAHH 高高液位报警口LAH 高液位报警口NLL 正常液位LAL 低液位报警LALL 低低液位报警。
PVElite help guide updated-design constraints
Design Constraints Tab
UG-100 - ASME UG-100 pneumatic test. The test pressure is 1.1 times (1.25 for pre-99 addenda) the maximum allowable working pressure for the entire vessel, multiplied by the lowest ratio of the stress value Sa for the test temperature to the stress value S for the design temperature. The stress ratio mentioned above includes bolt allowable stresses for flanges that are designed according to Appendix 2. This will usually result in a ratio of 1. See ASME Interpretation VIII-1-83-260 for more information. Click Tools > Configuration to turn off this option, resulting in a ratio greater than one in cases where the operating and ambient stresses for the vessel parts are not the same. AT-300 - ASME AT-300, Division 2, based on vessel design pressure. The hydrotest pressure is 1.25 times the design pressure to be marked on the vessel, multiplied by the lowest ratio of the stress intensity value Sm for the test temperature to the stress intensity value Sm for the design temperature. This type of hydrotest is normally used for non-carbon steel vessels where the allowable stress changes with temperature starting even at a somewhat low temperature. AT-301 - ASME AT-301, Division 2, based on calculated pressure. A hydrostatic test based on a calculated pressure may be used by agreement between the user and the manufacturer. The hydrostatic test pressure at the top of the vessel is the minimum of the test pressures calculated by multiplying the basis for calculated test pressure for each element by 1.25 and reducing this value by the hydrostatic head on that element. No Hydro - No hydrotest pressure. User Entered Pressure 1.43 * MAWP (PED)
ASME TABLE KK FORM U-DR-1
Owner:
Operator:
Country of Installation:
State/Province of Installation:
City of Installation:
Classification
Category
Exposure
Category
Topographic
Factor
Elevation
Seismic Loading:ASCE7□
UBC□IBC□
Other□None□
Soil Profile Classification:
PWHT:
PerCode□ProcessRequired□
Deg@
Due to:Process□Other□
Ambient Temperature□
Corrosion Allowance:
Shell
Heads
Nozzles
Jacket
Coil
Supports
Internals
Corrosive
Service?
Int.
Ext.
Int.
Ext.
Int.
Ext.
Other Loading per UG-22:
Temp.Gradients□Deflagration□
Diff.Thermal Exp.□
Insulated:Yes□No□
By Manufacturer□By Others□
TypeThickness
External
应用PVElite 应注意的问题
PVElite简介及应用PVElite 软件是由美国COADE 工程软件公司编制的，基本包含了设备设计中中常用计算，涉及十几个国外标准规范，输入的数据多，多项选择的参数比较多，需要设计人在计算时在多个选项中做出明确选择，而且这类参数对计算结果影响较大，为便于大家正确理解和使用该软件，熟悉软件计算书，特将主要内容概括如下。
1．软件使用的标准规范1.1基本元件计算规范ASME VIII Division 1，2002修订版。
PD5500,2000版，仅限于管板、接管根部局部应力计算。
TEMA, Tublar Exchanger Manufacture’s Association,1999年第8版，仅限管板计算。
WRC 107,Welding Research Council Bulletin 1979版。
WRC 297,Welding Research Council Bulletin 1984版。
API 579，Local Thinning and General Metal Loss Level 1 and 2 evaluation。
1.2风载计算规范ASCE 7，American Society of Civil Engineers Standard 7 (formerly ANSI A58.1)，1993版。
ASCE 7，American Society of Civil Engineers Standard 7 (formerly ANSI A58.1)，1995版。
UBC，Uniform Building Code，1994版。
NBC，National Building Code of Canada，1990版。
IS-875，India's wind design code ，1987版。
USER DEFINED，自定义风载数据。
1.3地震载荷计算规范ASCE 7，American Society of Civil Engineers Standard 7 (formerly ANSI A58.1)，1993版。
第二章 压力容器基本知识
第二章压力容器基本知识第一节压力容器类别划分【学习目标】学习TSG R0004-2009《固定式压力容器安全技术监察规程》，掌握压力容器类别划分原则。
学习HG20660-2000《压力容器中化学介质毒性危害和爆炸危害程度分类》，了解常见的化学介质毒性危害和爆炸危害程度分类。
一、压力容器类别划分TSG R0004-2009《固定式压力容器安全技术监察规程》1.7条款规定：根据危险程度，本规程适用范围内的压力容器划分为三类，以利于进行分类监督管理。
压力容器类别划分与三个因素有关：介质特性（组别）、设计压力（MPa）、容积（L）。
压力容器类别划分的意义是有利于压力容器的分类监督和管理，如压力容器设计许可证、压力容器制造许可证等都与压力容器类别有关。
A1 压力容器类别划分A1.1 介质分组压力容器的介质分为以下两组：（1）第一组介质，毒性程度为极度危害、高度危害的化学介质，易爆介质，液化气体。
（2）第二组介质，除第一组以外的介质。
A1.2 介质危害性介质危害性指压力容器在生产过程中因事故致使介质与人体大量接触，发生爆炸或者因经常泄漏引起职业性慢性危害的严重程度，用介质毒性程度和爆炸危害程度表示。
A1.2.3 介质毒性危害程度和爆炸危害程度的确定按照HG20660-2000《压力容器中化学介质毒性危害和爆炸危害程度分类》确定。
A1.3 压力容器类别划分方法A1.3.1 基本划分压力容器类别的划分应当根据介质特性，按照以下要求选择类别划分图，再根据设计压力p（单位MPa）和容积V（单位L），标出坐标点，确定压力容器类别：（1）第一组介质，压力容器类别的划分见图A-1；（2）第二组介质，压力容器类别的划分见图A-2。
A1.3.2 多腔压力容器类别划分按照类别高的压力腔作为该容器的类别并且按照该类别进行使用管理。
A1.3.3 同腔多种介质压力容器类别划分一个压力腔内有多种介质时，按照组别高的介质划分类别。
A1.3.4 介质含量极小的压力容器类别划分当某一危害性物质在介质中含量极小时，应当根据其危害程度及其含量综合考虑，按照压力容器设计单位决定的介质组别划分类别。
PVelite培训教程（可编辑）
PVelite培训教程PV Elite 培训手册PVElite 培训手册二零零五年五月三十日PV Elite 培训手册目录1 概述. 51.1 Pvelite特性51.2 主要功能. 51.2.1 Shell&Head 壳体、封头51.2.2 Nozzle 管口 51.2.3 Conical Section 锥壳. 51.2.4 Flanges 法兰. 51.2.5 Floating Head 浮头. 51.2.6 TEMA 和 PD5500 管板. 61.2.7 WRC107 和 WRC297 61.2.8 Thin joints 薄膨胀节 61.2.9 Thick joints 厚膨胀节. 61.2.10 ASME 管板61.2.11 Rectangular Vessels 矩形容器. 61.2.12 Horizontal Vessels 卧式容器61.2.13 Vertical Vessels 立式容器 62 操作界面 73 容器数据. 133.1 Design Constraints 设计参数 133.2 ASME Steel Stack163.3 Design Modification 设计修改163.4 Load Case 工况组合. 163.4.1 Load 载荷. 163.4.2 Load Case 工况组合 183.4.3 与工况有关的其它要求 183.5 Nozzle Design Options 管口设计选项:193.6 风、地震数据. 193.6.1 风载荷. 193.6.2 地震数据. 254 元件参数. 334.1 元件基本参数: 334.2 元件附加参数. 344.2.1 Cylindrical 圆筒344.2.2 Elliptical 椭圆形封头 344.2.3 Torispherical 碟形封头. 354.2.4 Spherical Head 半球形封头. 354.2.5 Conical Head or Shell Segment 锥形封头或锥形过渡段 35 4.2.6 Welded Flat 焊接平盖. 364.2.7 Flange Analysis 法兰分析36第 2 页共 145 页 PV Elite 培训手册4.2.8 Skirt Support with base ring 裙座(带螺栓底座环). 42 4.3 容器详细参数. 464.3.1 附件基本数据:474.3.2 Ring 加强圈. 474.3.3 Nozzle 管口. 514.3.4 Lung 支耳. 654.3.5 Saddles 鞍座 664.3.6 Trays 塔盘. 714.3.7 Leg 支腿. 714.3.8 Packing 填料 744.3.9 Liquid 介质754.3.10 Insulation 保温 774.3.11 Lining 衬里784.3.12 Platform784.3.13 Weight 重量. 794.3.14 外载. 805 换热器. 825.1 Tubesheet Type and Design Code 管板型式和设计标准 82 5.2 Tubesheet Properties 管板参数845.3 Tube Data 换热管参数. 875.4 Expension Joint Data 膨胀节数据905.5 Load Cases 载荷组合(工况) 935.6 Floating Tubesheet 浮动管板 945.7 Floating Head 浮头盖. 955.8 钩圈参数956 Analyze 分析977 输入有关的部分 ASME条文说明 987.1 UG-45接管径部厚度. 987.2 标准管壁的昀小壁厚987.3 补强件的强度. 987.4 开孔补强998 术语定义1009 附录规范公式和规则应用举例1039.1 内压容器 1039.1.1 具有焊接接头的容器筒体和封头焊接接头系数规则应用103 9.2 承受附加载荷的受内压壳体的厚度计算. 1099.3 外压容器.1149.4 外压作用下客器允许的昀大不圆度.1179.5 外压圆柱形壳体周向加强圈的设计.1189.6 凸面受压的成型封头所需厚度..119第 3 页共 145 页 PV Elite 培训手册9.7 开孔和补强1229.7.1 焊接连接1229.8 管孔带 1379.9 应用 UCS-66 规程确定昀低许用昀小设计金属温度( MDMT)的例子 138第 4 页共 145 页 PV Elite 培训手册1 概述1.1 Pvelite特性PVelite 计算软件是基于国家标准,如:ASME 锅炉压力容器标准,或工业标准,如:卧式容器 Zick 分析方法。
术语-1,编制说明,081023
GB/T ××××.1—200X 压力容器术语基本术语（征求意见稿）编制说明1编制依据压力容器是化工、炼油、制药等行业的主要设备，是国务院颁布的《特种设备安全监察条例》中监管的七种特种设备之一。
为了压力容器的安全运行，全国锅炉压力容器标准化管理委员会制定了诸如GB150《钢制压力容器》等多项与压力容器相关的标准。
为了规范压力容器行业中的专业术语，早在上个世纪80年代就开始着手制定压力容器名词术语标准，但由于多方面原因，未能得以颁布。
近些年由于压力容器行业的蓬勃发展，压力容器的设计者、制造者、使用者和检验者都迫切需要一本规范的压力容器名词术语标准来方便互相之间的交流，同时也用于规范其他资料的编制，所以全国锅炉压力容器标准化委员会（TC262）向国家标准化管理委员会提出申请编制《压力容器名词术语》标准，并于2000年由国家标准化委员会审查确定列入《2000年制修订国家标准项目计划》，项目编号20000331-T-469。
2 GB/T ××××—200×《压力容器术语》拟包括如下8个部分：GB/T××××·1—200×压力容器术语基本术语GB/T××××·2—200×压力容器术语技术、质量管理GB/T××××·3—200×压力容器术语压力容器结构GB/T××××·4—200×压力容器术语材料GB/T××××·5—200×压力容器术语设计GB/T××××·6—200×压力容器术语制造GB/T××××·7—200×压力容器术语涂覆、运输包装GB/T××××·8—200×压力容器术语安全附件3 GB/T ××××.1—2008 压力容器术语基本术语本标准第1部分共有主词条19个，另附有派生词条17个，共计36个。
ASME压力测试程序
ASME压力测试程序Pressure Testing Procedure 压 力 测 试 程 序Prepared by Date _____________编 制： 日期：Approved by _________________ Date ____________批 准： 日期：Accepted by _________________ Date ____________认 可： 日期：Zhenjiang JinMenIndustrial Co., Ltd ASME Procedures JM/ASME Pressure TestingProcedure Rev. No.: Page ：2 of2.2 that all low-pressure filling lines and other appurtenances that shall not be subjected tothe test pressure have been disconnected.应清洗被检测的容器中的原理油、油脂、油漆和其它脏物。
在测试中，容器的外表面应保持干燥和整洁。
应检验测试设备确保它是不漏水的，所有低压填充线和其它附属物在测试中不应被连接。
3 Hydrostatic Pressure Test 水压试验3.1 For internal pressurized vessels, hydrostatic pressure tests shall be applied by raising thepressure gradually to the maximum allowable working pressure (MAWP) as shown on the manufacturer’s data report to be stamped on the pressure vessel and hold for a few minutes in order to verify whether there is leakage. Then the pressure shall be raised to the testing pressure which at every point in the vessel is at least equal to 1.3 times the MAWP to be marked on the vessel multiplied by the lowest ratio of the stress value S at the test temperature on the vessel to the stress value S at the design temperature. All loading that may exist during pressure test shall be considered. The testing pressure shall be indicated on the drawings.水压试验应应用内部承压，通过渐渐地升压直至到最大需用工作压力（MAWP ），生产制造商用钢印标识在压力容器上的数据报告有标明了最大需用工作压力。
- 1、下载文档前请自行甄别文档内容的完整性，平台不提供额外的编辑、内容补充、找答案等附加服务。
- 2、"仅部分预览"的文档,不可在线预览部分如存在完整性等问题,可反馈申请退款(可完整预览的文档不适用该条件!)。
- 3、如文档侵犯您的权益，请联系客服反馈,我们会尽快为您处理(人工客服工作时间：9:00-18:30)。
Minimum Design Metal Temperature Results Summary :Curve Basic Reduced UG-20(f) Thickness Gov E*Description MDMT MDMT MDMT ratio ThkNotes F F F in.---------------------------------------------------------------------------- [10] B -20 -20 1.000 0.250 1.000[7] B -20 -20 1.000 0.250 1.000[8] B -20 -20 1.000 0.250 1.000[10] B -20 -20 1.000 0.250 1.000[7] B -20 -20 1.000 0.250 1.000[8] B -20 -21 0.992 0.250 1.000[10] B -20 -20 1.000 0.250 1.000[7] B -20 -20 1.000 0.250 1.000[9] B -20 -24 0.963 0.250 1.000[9] B -20 -24 0.963 0.250 1.000---------------------------------------------------------------------------- Required Minimum Design Metal Temperature -20 FWarmest Computed Minimum Design Metal Temperature -20 FNotes:[ ! ] - This was an impact tested material.[ 1] - Governing Nozzle Weld.[ 4] - ANSI Flange MDMT Calcs; Thickness ratio per UCS-66(b)(1)(c).[ 5] - ANSI Flange MDMT Calcs; Thickness ratio per UCS-66(b)(1)(b).[ 6] - MDMT Calculations at the Shell/Head Joint.[ 7] - MDMT Calculations for the Straight Flange.[ 8] - Cylinder/Cone/Flange Junction MDMT.[ 9] - Calculations in the Spherical Portion of the Head.[10] - Calculations in the Knuckle Portion of the Head.[11] - Calculated (Body Flange) Flange MDMT.[12] - Calculated Flat Head MDMT per UCS-66(3)UG-84(b)(2) was not considered.UCS-66(g) was not considered.UCS-66(i) was not considered.Notes:Impact test temps were not entered in and not considered in the analysis.UCS-66(i) applies to impact tested materials not by specification andUCS-66(g) applies to materials impact tested per UG-84.1 General Note (c).The Basic MDMT includes the (30F) PWHT credit if applicable.PV Elite is a trademark of Intergraph CADWorx & Analysis Solutions, Inc. 2012Design Code: ASME Code Section VIII Division 1, 2010, 2011aDiameter Spec : 96.000 in. IDVessel Design Length, Tangent to Tangent 14.50 ft.Distance of Bottom Tangent above Grade 0.00 ft.Distance of Base above Grade 0.00 ft.Specified Datum Line Distance 14.50 ft.Shell Material Specification SA-516 70Nozzle Material Specification SA-106 BInternal Design Temperature 200 FInternal Design Pressure 100.000 psigExternal Design Temperature 200 FExternal Design Pressure 15.000 psigMaximum Allowable Working Pressure 51.460 psigExternal Max. Allowable Working Pressure 2.149 psigHydrostatic Test Pressure 0.000 psigRequired Minimum Design Metal Temperature -20 FWarmest Computed Minimum Design Metal Temperature -20 FWind Design Code ASCE-93Earthquake Design Code UBC-94 Element Pressures and MAWP: psigElement Desc | Design Pres. | External | M.A.W.P | Corrosion| + Stat. head | Pressure | | Allowance--------------------------------------------------------------------- Ellipse 100.000 15.000 51.460 0.1250Cylinder 100.000 15.000 51.867 0.1250Ellipse 100.000 15.000 51.460 0.1250Cylinder 0.000 0.000 51.867 0.1250Ellipse 100.000 15.000 51.460 0.1250Sphere 100.000 15.000 103.842 0.1250Sphere 100.000 15.000 103.842 0.1250Element "To" Elev Length Element Thk R e q d T h k Joint Eff Type ft. ft. in. Int. Ext. Long Circ-----------------------------------------------------------------------Ellipse -14.33 0.167 0.250 <<< 0.365 0.375 1.00 1.00Cylinder -10.33 4.000 0.250 <<< 0.366 0.392 1.00 1.00Ellipse -10.17 0.167 0.250 <<< 0.365 0.375 1.00 1.00Skirt -10.17 5.000 0.250 No Calc No Calc 1.00 1.00Cylinder -5.17 5.000 0.250 0.188 No Calc 1.00 1.00Ellipse -5.00 0.167 0.250 <<< 0.365 0.375 1.00 1.00Sphere -5.00 0.001 0.250 <<< 0.245 0.264 1.00 1.00Sphere -5.00 0.001 0.250 <<< 0.245 0.264 1.00 1.00Element thicknesses are shown as Nominal if specified, otherwise are MinimumWind/Earthquake Shear, Bending| | Distance to| Cumulative |Earthquake | Wind | Earthquake |From| To | Support| Wind Shear | Shear | Bending | Bending || | ft. | lb. | lb. | ft.lb. | ft.lb. |--------------------------------------------------------------------------- 10| 20| 0.75259 | ... | ... | ... | ... |20| 30| 2.83333 | 114.217 | ... | 162.104 | ... |30| 40| 4.91667 | 374.716 | ... | 1139.97 | ... |40| 50| 2.50000 | 1253.46 | ... | 6533.79 | ... |50| 60| 7.50000 | 542.269 | ... | 2283.86 | ... |60| 70| 10.0833 | 216.645 | ... | 386.574 | ... |70| 80| 10.1672 | 205.791 | ... | 351.371 | ... |80| 90| 11.8736 | 205.726 | ... | 351.165 | ... |Abs Max of the all of the Stress Ratio's : 0.8039Total Wind Shear on Support 1253. lb.Note: Wind and Earthquake moments include the effects of user definedforces and moments if any exist in the job and were specifiedto act (compute loads and stresses) during these cases. Alsoincluded are moment effects due to eccentric weights if any arepresent in the input.Weights:Fabricated - Bare W/O Removable Internals 8178.6 lbmShop Test - Fabricated + Water ( Full ) 67250.6 lbmShipping - Fab. + Rem. Intls.+ Shipping App. 8178.6 lbm Erected - Fab. + Rem. Intls.+ Insul. (etc) 8178.6 lbm Empty - Fab. + Intls. + Details + Wghts. 8178.6 lbm Operating - Empty + Operating Liquid (No CA) 8178.6 lbm Field Test - Empty Weight + Water (Full) 67250.6 lbmPV Elite is a trademark of Intergraph CADWorx & Analysis Solutions, Inc. 2012Problems/Failures Summary : Step: 24 12:34p Sep 1,2014Listed below are the known problem areas for the current design. Ifone or more of the design flags are turned on, please re-run the analysis.Some of these issues may be resolved when using updated input values.** Warning: Insufficient Element Thickness due to Internal Pressure !** Warning: Insufficient Element Thickness due to External Pressure !** Warning: One or more Nozzles failed Code Requirements !Please review all reports carefully!PV Elite is a trademark of Intergraph CADWorx & Analysis Solutions, Inc. 2012。