外文翻译----离心泵在化工生产的应用

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化工常用英语词汇

化工常用英语词汇

化工专业英语词汇化学专业课程中英文对照一、化工装置常用词汇一概论introduction方案建议书proposal可行性研究feasibility study方案设计 concept design工艺设计 process design基础设计 basic design详细设计 detail design开工会议 kick-off meeting审核会议 review meeting外商投资 foreign investment中外合资 joint venture中外合营 joint venture补偿贸易compensation trade合同合同附件 contract卖方 vendor买方 buyer顾客 client承包商contractor工程公司 company供应范围 scope of supply生产范围 production scope生产能力 production capacity项目 project界区 battery limit装置 plant公用工程utilities工艺流程图 process flow diagram工艺流程方块图 process block diagram管道及仪表流程图 piping and instrument drawing物料及热量平衡图 mass & heat balance diagram蒸汽及冷凝水平衡图 steam & condensate balance diagram设备布置图 equipment layout设备表 equipment list成品产品 productfinal product副产品 by-product原料raw-material设计基础数据 basic data for design技术数据 technical data数据表 data sheet设计文件 design document设计规定 design regulation现场服务 site service项目变更 project change用户变更 client change消耗定额 consumption quota技术转让technical transfer技术知识 technical know-how technical knowledge技术保证technical guarantee咨询服务 consultative services技术服务 technical services工作地点 location施工现场 construction field报价 quotation标书 bidding book公司利润 company profit固定价合同 fixed price contract固定单价合同 fixed unit price contract成本加酬金合同 cost plus award fee contract定金 mobilization银行保证书bank guarantee letter保留金 retention所得税 income taxes特别承包人税 special contractor's taxes城市和市政税 city and municipal taxes工作手册 work manual工作流程图 work flow diagram质量保证程序 QA/QC procedures采购计划 procurement plan施工计划construction plan施工进度construction schedule项目实施计划project execution plan项目协调程序 project coordination procedure项目总进度计划 project master schedule设计网络计划 engineering network logic项目质量保证 project quality assurance项目质量控制project quality control采购procurement 采购周期procurement period会签 the squad check计算书 calculation sheets询价 inquiry检验inspection运输transportation开车start up / commission验收inspection & acceptance校核 check审核 review审定 approve版次 version部门 department专业specialty项目号 project number图号 drawing number目录 contents序言 foreword章chapter节section项itemMR material requisitionSPEC engineering specificationDATA SHEET技术表technical data sheetTBA技术评标technical bid analysisPDP preliminary design packagePM 项目经理 project managerLDE专业负责人lead discipline engineerMRQ材料询价单 Material requisition for quotationMRP材料采购单material requisition for purchaseBEP基础工程设计包basic engineering packageP&ID管道及仪表流程图 piping and instrument drawingdiagramPFD process flow diagramNNF normally no flowFO failure openFC failure closeC/S/A civil/structure/architectureDDP详细设计阶段 detail design phase二、工艺流程连续过程 continuous process间歇过程 batch process工艺叙述 process description工艺特点 process feature操作 operation反应 reaction副反应 side reaction絮凝 flocculation浮洗 flotation倾析 decantation催化反应 catalytical reaction萃取 extraction中和 neutralization水解 hydrolysis过滤 filtration干燥drying还原 reduction氧化 oxidation氢化 hydrogenation分解 decomposition离解dissociation合成 synthetics吸收 absorption吸附 adsorption解吸 desorption结晶crystallization溶解 solution调节 modulate控制 control悬浮 suspension循环circulation再生 regeneration再活化 reactivation沥取 leaching破碎 crushing煅烧caloination沉降sedimentation沉淀precipitation气化gasification冷冻refrigeration固化、结晶solidification包装package升华sublimation燃烧combustion引烧 ignition蒸馏 distillation碳化 carbonization压缩 compression三、化学物质及特性固体 solid液体 liquid气体 gas化合物 compound混合物 mixture 粉 powder片状粉未 flake小粒 granule结晶 crystal乳化物 emulsion氧化物oxidizing agent还原剂 reducing agent有机物 organic material真空 vacuum母液master liquor富液 rich liquor贫液 lean liquor萃出物 extract萃余物 raffinate絮凝剂 flocculants冷冻盐水 brine酸度 acidity浓度 concentration碱度 alkalinity 溶解度 solubility凝固点 solidificalion point沸点 boiling point熔点 melting point 蒸发率 evaporation rate粘度 viscosity吸水的 water absorbenta无水的 anhydrousa 外观 appearance无色的 colorlessa透明的 transparenta半透明的 translucent密度density比重 specific gravity催化剂 catalyst燃烧 combustion引燃 ignition自然点self-ignition temperature可燃气体 combustible gas可燃液体 inflammable liquid易燃液体volatile liquid爆炸混合物explosive mixture爆炸性环境explosive atmosphereenvironment爆炸极限 explosive concentration limit废水 waste water废液waste liquid废气 off-gas噪声 noise pollution成分 composition挠度 deflection力和力矩 force and moment弯矩 bending moment应力-应变曲线 stress-strain diagram百分比 percentage环境温度 ambient temperature工作温度 operating设计温度 design temperaturepressure相对湿度 RH=relative humidity油渣、淤泥 sludge杂质 impurity 四、化工设备泵 pump轴流泵 axial flow pump真空泵 vacuum pump屏蔽泵 canned pump 柱塞泵 plunger pump涡轮泵 turbine pump涡流泵 vortex pump离心泵 centrifugal pump 喷射泵 jet pump转子泵 rotary pump管道泵 inline pump双作用往复泵 double action reciprocating pump计量泵 metering pump深井泵 deep well pump齿轮泵 gear pump手摇泵 handwobble pump螺杆泵 screw spiral pump潜水泵 submersible pump斜转子泵inclined rotor pump封闭式电磁泵 hermetically sealed magnetic drive pump气升泵air-lift-pump轴承 bearing叶轮 impeller虹吸管 siphon高压容器 high pressure vessel焚化炉 incinerator火焰清除器 flame arrester工业炉 furnace烧嘴 burner锅炉boiler回转窑 rotary kiln加热器 heater电加热器 electric heater冷却器 cooler冷凝器 condenser换热器 heat exchanger反应器 reactor蒸馏釜 still搅拌器 agitator混合器 mixer静态混合器 static mixers管道混合器 line mixers混合槽 mixing tanks破碎机 crusher磨碎机 grinder研磨机 pulverizer球磨机 ballmill过滤器 filter分离器separator干燥器 drier翅片 fins烟囱 stack火炬 flare筛子 screen煅烧窑 calciner 倾析器 decanter蒸发器 evaporator再沸器reboiler萃取器 extractor离心机centrifuger吸附收器 adsorber结晶器 crystallizer电解槽 electrolyzer电除尘器electric precipitator洗涤器 scrubber消石灰器 slaker料仓 bin料斗 hopper加料器feeder增稠器 thickener澄清器 clarifier分级器 classifier浮洗器 flocculator废液池 sump喷射器 ejector喷头 sprayer成套设备 package unit仪器设备 apparatus附属设备 accessory旋转式压缩机 rotary compressor往复式压缩机 reciprocating compressor 水环式压缩机 nash compressor螺杆式压缩机 helical screw compressor离心式压缩机centrifugal compressor多级压缩机 mutiple stages compressor固定床反应器 fixed bed reactor流化床反应器 fluidized bed reactor管式反应器 tubular reactor列管式换热器tubular heat exchanger螺旋板式换热器 spiral plate heat exchanger萃取塔 extraction column板式塔 plate column填料塔 packed column洗涤塔 scrubber吸收塔 absorber冷却塔 cooling tower精馏塔 fractionating tower汽提塔 stripper再生塔 regenerator 造粒塔 prill tower塔附件 tower accessories液体分配布器 liquid distributor填料支持板 support plate定距管 spacer降液管 downcomer升气管 chimney顶底层塔盘 top bottom tray挡板 baffle抽出口 draw nozzle溢流堰 weir泡罩 bubble cap筛板 sieve plate浮阀 float valve除沫器 demister pad塔裙座 skirt椭圆封头 elliptical head 高位槽 head tank中间槽 intermediate tank加料槽 feed tank补给槽 make-up tank计量槽 measuring tank电解槽 cell溜槽 chute收集槽 collecting tank液滴分离器knockout drum稀释罐 thinning tank缓冲罐 surge drum回流罐 reflux drum闪蒸罐 flash drum浮顶罐 floating roof tank内浮顶罐 covered floating roof tank球罐 spheroid气柜 gas holder湿式气柜 wet gas-holder干式气柜 dry gas-holder螺旋式气柜 helical gas-holder星型放料器,旋转阀 rotary valve抽滤器 mutche filter压滤器 filter press 压滤机 pressure filter板框压滤器 plate-and-fram filter press转鼓过滤器 rotary drum filter带式过滤器 belt filter翻盘式过滤器袋滤器 bag filter旋风分离器 cyclone separator盘式干燥箱 compartment tray drier真空干燥器 vacuum drier隧道式干燥器tunnel drier回转干燥器 rotary drier穿流循环干燥器 through circulation drier喷雾干燥器 spray drier气流干燥器 pneumatic conveyor drier圆盘式加料器 dish feeder螺旋式加料器 screw feeder颚式破碎机 jaw crusher回转破碎机 gyratory crusher滚洞破碎机roll crusher锤式破碎机 hammer crusher冲击破碎机 rotor impact breaker气流喷射粉碎机 jet pulverizer棍磨机 rod mill雷蒙机 raymond mill锤磨机 hammer mill辊磨机roller mill振动筛 vibrating screen回转筛 rotary screen风机 fan罗茨鼓风机 root's blower起重机 crane桥式起重机 bridge crane电动葫芦 motor hoist发电机 generator 电动机 motor 汽轮机 steam turbine五、管道工程 piping engineering1 阀门 valve阀杆 stem内螺纹阀杆 inside screw阀座 valve seat body seat阀座环、密封圈 sealing ring阀芯包括密封圈,杆等 trim阀盘 disc阀体 body阀盖 bonnet手轮 hand wheel手柄 hand level handle压盖 gland闸阀 gate valve平行双闸板 double disc parallel seat楔形单闸板 split wedge截止阀 globe valve节流阀 throttle valve针阀 needle valve角阀角式截止阀 angle valveY型阀截止阀 Y-valveY-body globe valve球阀 ball valve三通球阀 3-way ball valve蝶阀 butterfly valve对夹式薄片型 wafer type偏心阀板蝶阀 offset disc eccentric butterfly valve 斜阀盘蝶阀 canted disc butterfly valve连杆式蝶阀 link butterfly valve止回式蝶阀 combined non-return butterfly valve柱塞阀 piston type valve旋塞阀 plug valve三通旋塞阀 three-way plug valve四通旋塞阀 four-way plug valve旋塞 cock衬套旋塞 sleeve cock隔膜阀 diaphragm valve橡胶衬里隔膜阀 rubber lined diaphragm valve直通式隔膜阀 straight way diaphragm valve夹紧式胶管阀 pinch valve止回阀 check valve升降式止回阀 lift check valve旋启式止回阀 swing check valve落球式止回阀 ball check valve弹簧球式止回阀 spring ball check valve底阀 foot valve切断式止回阀 stop check valve活塞式止回阀 piston check valve翻板止回阀 flap check valve蝶式止回阀 butterfly check valve安全泄气阀 safetySV安全泄放阀 relief valveRV安全泄压阀 safety relief valve杠杆重锤式 lever and weight type罐底排污阀 flush-bottom tank valve波纹管密封阀 bellow sealed valve电磁阀 solenoid operated valve电动阀 electricallyelectric-motoroperated valve 气动阀 pneumatic operated valve低温用阀 cryogenic service valve蒸汽疏水阀 steam trap机械式疏水阀 mechanical trap浮桶式疏水阀 open top bucket trap浮球式疏水阀 float trap倒吊桶式疏水阀 inverted bucket trap自由浮球式疏水阀 loose float trap恒温式疏水阀 thermostatic trap压力平衡式恒温疏水阀 balanced pressure thermostatic trap 热动力式疏水阀 thermodynamic trap脉冲式蒸汽疏水阀 impulse steam trap放汽阀自动放汽阀 automatic air vent valve换向阀 diverting reversing valve呼吸阀 breather valve减压阀 pressure reducing valve控制阀 control valve执行机构 actuator差压调节阀 differential pressure regulating valve切断阀 block shut-off, stop valve调节阀 regulating valve快开阀 quick opening valve快闭阀 quick closing valve隔断阀 isolating valve三通阀 three way valve夹套阀 jacketed valve非旋转式阀 non-rotary valve2管子,管件,法兰管子 pipe按标准制造的配管用管tube不按标准规格制造的其它用管钢管 steel pipe铸铁管 cast iron pipe衬里管 lined pipe复合管 clad pipe碳钢管 carbon steel.pipe合金钢管 alloy steel pipe不锈钢管 stainless steel.pipe奥氏体不锈钢管 austenitic stainless steel pipe铁合金钢管 ferritic alloy steel pipe轧制钢管 wrought-steel pipe锻铁管 wrought-iron pipe无缝钢管 seamlessSMLS steel pipe焊接钢管 welded steel pipe电阻焊钢管 electric-resistance-welded steel pipe电熔弧焊钢板卷管 electric-fusionarc-welded steel-plate pipe 螺旋焊接钢管 spiral welded steel pipe镀锌钢管 galvanized steel pipe排污阀 blowdown valve集液排放阀 drip valve排液阀 drain valve放空阀 vent valve卸载阀 unloading valve排出阀 discharge valve吸入阀 suction valve取样阀 sampling valve手动阀 hand operatedmanually-operated valve水龙头 bibb;bib;faucet抽出液阀小阀 bleed valve旁路阀 by-pass valve软管阀 hose valve混合阀 mixing valve破真空阀 vacuum breaker冲洗阀 flush valve根部阀 root primary, header valve水煤气钢管 water-gas steel pipe塑料管 plastic pipe玻璃管 glass tube橡胶管 rubber tube壁厚 wall thicknessWT壁厚系列号 schedule number.加厚的,加强的 extra heavy strong双倍加厚的,双倍加强的 double extra heavy strong 弯头 elbow异径弯头 reducing elbow长半径弯头 long radius elbow短半径弯头 short radius elbow长半径180°弯头 long radius return短半径180°弯头 short radius return三通 tee异径三通 reducing tee等径三通 straight tee带支座三通 base tee45°斜三通45°lateralY型三通 true"Y"四通 cross异径管 reducer同心异径管 concentric reducer偏心异径管 eccentric reducer管接头 coupling;full coupling活接头 union短管 nipple预制弯管 fabricated pipe bendU型弯管 "U"bend法兰端 flanged end万向接头 universal joint对焊的 butt weldedBW螺纹的 threadedTHD承插焊的 socket weldedSW法兰 flangeFLG整体管法兰 integral pipe flange钢管法兰 steel pipe flange螺纹法兰 threaded flange滑套法兰 slip-on flange平焊法兰 slip-on-welding flange承插焊法兰 socket welding flange松套法兰 lap joint flangeLJF对焊法兰 weld neck flangeWNF法兰盖 blind flange;blind异径法兰 reducing flange压力级 pressure ratingclass突面 raised faceRF凸面 male face凹面 female face全平面;满平面 flat face;full faceFF3.管道特殊件 piping speciality粗滤器 strainer过滤器 filter临时过滤器 temporary strainercone type Y型过滤器 Y-type strainerT型过滤器 T-type strainer永久过滤器 permanent filter洗眼器及淋浴器 eye washer and shower 视镜 sight glass阻火器 flame arrester喷咀;喷头 spray nozzle喷射器 ejector取样冷却器 sample cooler消音器 silencer膨胀节 expansion joint波纹膨胀节 bellow补偿器 compensator软管接头 hose connectionHC快速接头 quick coupling金属软管 metal hose橡胶管 rubber hose挠性管 flexible tube特殊法兰 special flange漏斗 funnel8字盲板 spectacle figure 8 blind爆破板 rupture disk4,其它材料碳素钢 carbon steel .不锈钢 stainless steel.铸铁 cast iron.铝 aluminum铜,紫铜 copper钛 titanium抗拉强度 tensile strength 非金属材料 non-metallic material塑料 plastic陶瓷 ceramic搪瓷 porcelain enamel 玻璃 glass橡胶 rubber垫片 gasketGSKT平垫片 flat gasket填料 packing型钢shaped steel角钢 angle steel槽钢 channel工字钢 I-beam宽缘工字钢或H钢 wide flanged beam扁钢 flat bar圆钢 round steel; rod钢带 strap steel网络钢板 checkered plate材料表 bill of materialBOM材料统计 material take-offMTO散装材料 bulk material综合管道材料表 consolidated piping material summary sheetCPMSS汇总表summary sheet 5.设备布置及管道设计中心线 center line装置边界 boundary limitBL 区界area limit设备布置equipment arrangement layout;plot plan标高,立面elevationEL支撑点 point of supportPOS工厂北向 plant north方位 orientation危险区hazardous area classification净正吸入压头net positive suction head绝对标高absolute elevation坐标 coordinate管道研究 piping study管道布置平面 piping arrangement planPAP管道布置 piping assembly; layout详图 detail"X"视图 view"X""A-A" 剖视 section "A-A"轴测图 isometric drawing索引图 key plan管道及仪表流程图 piping and instrument diagramP&ID管口表 list of nozzles地上管道 above ground piping地下管道 under ground piping管线号 line number总管 header; manifold旁路 by pass常开 normally open常闭 normally closed取样接口 sampling connection伴热管tracing pipe蒸汽伴热 steam tracing热水伴热 hot-water tracing电伴热 electrical tracing夹套管 jacketed line全夹套管 full jacketed比例 scale图 figure草图sketch图例 legend符号 symbol件号 part n普通化学 General Chemistry分析化学 Analytical Chemistry 有机化学 Organic Chemistry 物理化学 Physical Chemistry 谱学导论 Introducton of Spectroscopy 无机化学 Inorganic Chemistry 普通化学和分析化学实验 Experiments of General and Analytical Chemistry 现在基础化学 The Principle of Mordern Chemistry 现在基础化学实验 Experiments of Modern Fundamental Chemistry 有机化学实验 Experiments of Organic Chemistry 仪器分析和物理化学实验Experiments of Instrumental Analysis and Physical Chemistry 合成化学实验Experiments of Synthetic Chemistry 现代化学专题 Topic of Modern Chemistry 化学综合实验 Experiments of Comprehensive Chemistry化工原理 Principle of Chemical Engineering 化工原理实验 Experiments of Chemical Engineering 应用化学实验 Experiments of Applied Chemistry 无机合成化学 Synthetic Inorganic Chemistry近代分析化学Modern Analytical Chemistry 分离分析化学Separation Analytical Chemistry有机化合物波谱鉴定 Spectrum Identification of Organic Compounds 有机合成及反应机理 Organic Synthesis and Mechanics 化学进展 Progress in Chemistry 化学反应工程Chemical Reaction Engineering 应用电化学 Applied Electrochemistry工业催化 Industrial Catalysis 环境化学 Environmental Chemistry 环境监测 Environmental Monitoring化学科技英语 Scientific English for Chemistry 数理方法在化学中的应用 Mathematical Statistics for Chemistry 化工制图 Chemical Engineering Cartography 计算机与化学测量实验 Computer and Chemical Measurement 化学信息学 Chemoinformatics or Chemical Informatics 应用化学专题 Special Topics in Applied Chemistry。

化工装置词汇

化工装置词汇

化工装置词汇化工装置词汇一、化学专业课程中英文对照普通化学 General Chemistry分析化学 Analytical Chemistry有机化学 Organic Chemistry物理化学 Physical Chemistry谱学导论 Introducton of Spectroscopy无机化学 Inorganic Chemistry普通化学和分析化学实验Experiments of General and Analytical Chemistry现在基础化学 The Principle of Mordern Chemistry现在基础化学实验Experiments of Modern Fundamental Chemistry有机化学实验 Experiments of Organic Chemistry仪器分析和物理化学实验 Experiments of Instrumental Analysis and PhysicalChemistry合成化学实验 Experiments of Synthetic Chemistry现代化学专题 Topic of Modern Chemistry化学综合实验 Experiments of Comprehensive Chemistry化工原理 Principle of Chemical Engineering化工原理实验 Experiments of Chemical Engineering应用化学实验 Experiments of Applied Chemistry无机合成化学 Synthetic Inorganic Chemistry近代分析化学 Modern Analytical Chemistry分离分析化学 Separation Analytical Chemistry有机化合物波谱鉴定Spectrum Identification of Organic Compounds有机合成及反应机理 Organic Synthesis and Mechanics化学进展 Progress in Chemistry化学反应工程 Chemical Reaction Engineering应用电化学 Applied Electrochemistry工业催化 Industrial Catalysis环境化学 Environmental Chemistry环境监测 Environmental Monitoring化学科技英语 Scientific English for Chemistry数理方法在化学中的应用Mathematical Statistics for Chemistry化工制图 Chemical Engineering Cartography计算机与化学测量实验 Computer and Chemical Measurement 化学信息学 Chemoinformatics or Chemical Informatics应用化学专题 Special Topics in Applied Chemistry化工装置常用词汇1一概论 introduction方案(建议书) proposal可行性研究 feasibility study方案设计 concept design工艺设计 process design基础设计 basic design详细设计 detail design开工会议 kick-off meeting审核会议 review meeting外商投资 foreign investment中外合资 joint venture中外合营 joint venture补偿贸易 compensation trade合同合同附件 contract卖方 vendor买方 buyer顾客 client承包商 contractor工程公司 company供应范围 scope of supply生产范围 production scope生产能力 production capacity项目 project界区 battery limit装置 plant公用工程 utilities工艺流程图 process flow diagram工艺流程方块图 process block diagram管道及仪表流程图 piping and instrument drawing物料及热量平衡图 mass & heat balance diagram蒸汽及冷凝水平衡图 steam & condensate balance diagram 设备布置图 equipment layout设备表 equipment list成品(产品) product(final product)副产品 by-product原料 raw-material设计基础数据 basic data for design技术数据 technical data数据表 data sheet设计文件 design document设计规定 design regulation现场服务 site service项目变更 project change用户变更 client change消耗定额 consumption quota技术转让 technical transfer技术知识 technical know-how牋牋牋牋technical knowledge技术保证 technical guarantee咨询服务 consultative services技术服务 technical services工作地点 location施工现场 construction field报价 quotation标书 bidding book公司利润 company profit固定价合同 fixed price contract固定单价合同 fixed unit price contract成本加酬金合同 cost plus award fee contract 定金 mobilization银行保证书 bank guarantee letter保留金 retention所得税 income taxes特别承包人税 special contractor's taxes城市和市政税 city and municipal taxes工作手册 work manual工作流程图 work flow diagram质量保证程序 QA/QC procedures采购计划 procurement plan施工计划 construction plan施工进度 construction schedule项目实施计划 project execution plan项目协调程序 project coordination procedure 项目总进度计划 project master schedule设计网络计划 engineering network logic项目质量保证 project quality assurance项目质量控制 project quality control采购 procurement采购周期 procurement period会签 the squad check计算书 calculation sheets询价 inquiry检验 inspection运输 transportation开车 start up / commission验收 inspection & acceptance校核 check审核 review审定 approve版次 version部门 department专业 specialty项目号 project number图号 drawing number目录 contents序言 foreword章 chapter节 section项 itemMR material requisitionSPEC engineering specificationDATA SHEET(技术表) technical data sheet TBA(技术评标) technical bid analysis PDP preliminary design packagePM (项目经理) project managerLDE(专业负责人 lead discipline engineerMRQ(材料询价单) Material requisition for quotationMRP(材料采购单) material requisition for purchaseBEP(基础工程设计包) basic engineering packageP&ID(管道及仪表流程图) piping and instrument drawing(diagram)PFD process flow diagramNNF normally no flowFO failure openFC failure closeC/S/A civil/structure/architectureDDP(详细设计阶段) detail design phase二. 工艺流程连续过程continuous process间歇过程batch process工艺叙述process description工艺特点process feature操作operation反应reaction副反应side reaction絮凝flocculation浮洗flotation倾析decantation催化反应catalytical reaction萃取extraction中和neutralization水解hydrolysis过滤filtration干燥drying还原reduction氧化oxidation氢化hydrogenation分解decomposition离解dissociation合成synthetics吸收absorption吸附adsorption解吸desorption结晶crystallization溶解solution调节modulate控制control悬浮suspension循环circulation再生regeneration再活化reactivation沥取leaching破碎crushing煅烧caloination沉降sedimentation沉淀precipitation气化gasification冷冻refrigeration固化、结晶solidification 包装package升华sublimation燃烧combustion引烧ignition蒸馏distillation碳化carbonization压缩compression三、化学物质及特性固体solid液体liquid气体gas化合物compound混合物mixture粉powder片状粉未flake小粒granule结晶crystal乳化物emulsion氧化物oxidizing agent 还原剂reducing agent有机物organic material 真空vacuum母液master liquor富液rich liquor贫液lean liquor萃出物extract萃余物raffinate絮凝剂flocculants冷冻盐水brine酸度acidity浓度concentration碱度alkalinity溶解度solubility凝固点solidificalion point 沸点boiling point熔点melting point蒸发率evaporation rate粘度viscosity吸水的water absorbent(a)无水的anhydrous(a)外观appearance无色的colorless(a)透明的transparent(a)半透明的translucent密度density比重specific gravity催化剂catalyst燃烧combustion引燃ignition自然点self-ignition temperature可燃气体combustible gas可燃液体inflammable liquid易燃液体volatile liquid爆炸混合物explosive mixture爆炸性环境explosive atmosphere(environment) 爆炸极限explosive concentration limit废水waste water废液waste liquid废气off-gas噪声noise pollution成分composition挠度deflection力和力矩force and moment弯矩bending moment应力-应变曲线stress-strain diagram百分比percentage环境温度ambient temperature工作温度operating设计温度design temperature(pressure)相对湿度RH=relative humidity油渣、淤泥sludge杂质impurity四、化工设备泵pump轴流泵axial flow pump真空泵vacuum pump屏蔽泵canned pump柱塞泵plunger pump涡轮泵turbine pump涡流泵vortex pump离心泵centrifugal pump喷射泵jet pump转子泵rotary pump管道泵inline pump双作用往复泵double action reciprocating pump计量泵metering pump深井泵deep well pump齿轮泵gear pump手摇泵hand(wobble) pump螺杆泵screw (spiral) pump潜水泵submersible pump斜转子泵inclined rotor pump封闭式电磁泵hermetically sealed magnetic drive pump 气升泵air-lift-pump轴承bearing叶轮impeller虹吸管siphon高压容器high pressure vessel 焚化炉incinerator火焰清除器flame arrester工业炉furnace烧嘴burner锅炉boiler回转窑rotary kiln加热器heater电加热器electric heater冷却器cooler冷凝器condenser换热器heat exchanger反应器reactor蒸馏釜still搅拌器agitator混合器mixer静态混合器static mixers管道混合器line mixers混合槽mixing tanks破碎机crusher磨碎机grinder研磨机pulverizer球磨机ballmill过滤器filter分离器separator干燥器drier翅片fins烟囱stack火炬flare筛子screen煅烧窑calciner倾析器decanter蒸发器evaporator再沸器reboiler萃取器extractor离心机centrifuger吸附(收)器adsorber结晶器crystallizer电解槽electrolyzer电除尘器electric precipitator洗涤器scrubber消石灰器slaker料仓bin料斗hopper加料器feeder增稠器thickener澄清器clarifier分级器classifier浮洗器flocculator废液池sump喷射器ejector喷头sprayer成套设备package unit仪器设备apparatus附属设备accessory旋转式压缩机rotary compressor往复式压缩机reciprocating compressor水环式压缩机nash compressor螺杆式压缩机helical screw compressor离心式压缩机centrifugal compressor多级压缩机mutiple stages compressor固定床反应器fixed bed reactor流化床反应器fluidized bed reactor管式反应器tubular reactor列管式换热器tubular heat exchanger螺旋板式换热器spiral plate heat exchanger 萃取塔extraction column板式塔plate column填料塔packed column洗涤塔scrubber吸收塔absorber冷却塔cooling tower精馏塔fractionating tower汽提塔stripper再生塔regenerator造粒塔prill tower塔附件tower accessories液体分配(布)器liquid distributor填料支持板support plate定距管spacer降液管downcomer升气管chimney顶(底)层塔盘top (bottom) tray挡板baffle抽出口draw nozzle溢流堰weir泡罩bubble cap筛板sieve plate浮阀float valve除沫器demister pad塔裙座skirt椭圆封头elliptical head高位槽head tank中间槽intermediate tank加料槽feed tank补给槽make-up tank计量槽measuring tank电解槽cell溜槽chute收集槽collecting tank液滴分离器knockout drum稀释罐thinning tank缓冲罐surge drum回流罐reflux drum闪蒸罐flash drum浮顶罐floating roof tank内浮顶罐covered floating roof tank 球罐spheroid气柜gas holder湿式气柜wet gas-holder干式气柜dry gas-holder螺旋式气柜helical gas-holder星型放料器,旋转阀rotary valve抽滤器mutche filter压滤器filter press压滤机pressure filter板框压滤器plate-and-fram filter press转鼓过滤器rotary drum filter带式过滤器belt filter翻盘式过滤器袋滤器bag filter旋风分离器cyclone separator盘式干燥箱compartment tray drier真空干燥器vacuum drier隧道式干燥器tunnel drier回转干燥器rotary drier穿流循环干燥器through circulation drier 喷雾干燥器spray drier气流干燥器pneumatic conveyor drier 圆盘式加料器dish feeder螺旋式加料器screw feeder颚式破碎机jaw crusher回转破碎机gyratory crusher滚洞破碎机roll crusher锤式破碎机hammer crusher冲击破碎机rotor impact breaker气流喷射粉碎机jet pulverizer棍磨机rod mill雷蒙机raymond mill锤磨机hammer mill辊磨机roller mill振动筛vibrating screen回转筛rotary screen风机fan罗茨鼓风机root's blower起重机crane桥式起重机bridge crane电动葫芦motor hoist发电机generator电动机motor汽轮机steam turbine五、管道工程piping engineering1 阀门valve阀杆stem内螺纹阀杆inside screw阀座valve seat (body seat)阀座环、密封圈sealing ring阀芯(包括密封圈,杆等)trim阀盘disc阀体body阀盖bonnet手轮hand wheel手柄hand level (handle)压盖gland闸阀gate valve平行双闸板double disc parallel seat楔形单闸板split wedge截止阀globe valve节流阀throttle valve针阀needle valve角阀(角式截止阀)angle valveY型阀(截止阀)Y-valve(Y-body globe valve)球阀ball valve三通球阀3-way ball valve蝶阀butterfly valve对夹式(薄片型)wafer type偏心阀板蝶阀offset disc (eccentric) butterfly valve斜阀盘蝶阀canted disc butterfly valve连杆式蝶阀link butterfly valve止回式蝶阀combined non-return butterfly valve 柱塞阀piston type valve旋塞阀plug valve三通旋塞阀three-way plug valve四通旋塞阀four-way plug valve旋塞cock衬套旋塞sleeve cock隔膜阀diaphragm valve橡胶衬里隔膜阀rubber lined diaphragm valve 直通式隔膜阀straight way diaphragm valve夹紧式胶管阀pinch valve止回阀check valve升降式止回阀lift check valve旋启式止回阀swing check valve落球式止回阀ball check valve弹簧球式止回阀spring ball check valve底阀foot valve切断式止回阀stop check valve活塞式止回阀piston check valve翻板止回阀flap check valve蝶式止回阀butterfly check valve安全泄气阀safety[SV]安全泄放阀relief valve[RV]安全泄压阀safety relief valve杠杆重锤式lever and weight type罐底排污阀flush-bottom tank valve波纹管密封阀bellow sealed valve电磁阀solenoid (operated) valve电动阀electrically(electric-motor)operated valve气动阀pneumatic operated valve低温用阀cryogenic service valve蒸汽疏水阀steam trap机械式疏水阀mechanical trap浮桶式疏水阀open (top) bucket trap浮球式疏水阀float trap倒吊桶式疏水阀inverted bucket trap自由浮球式疏水阀loose float trap恒温式疏水阀thermostatic trap压力平衡式恒温疏水阀balanced pressure thermostatic trap 热动力式疏水阀thermodynamic trap脉冲式蒸汽疏水阀impulse steam trap放汽阀(自动放汽阀)(automatic) air vent valve换向阀diverting (reversing) valve呼吸阀breather valve减压阀pressure reducing valve控制阀control valve执行机构actuator差压调节阀differential pressure regulating valve切断阀block (shut-off, stop) valve调节阀regulating valve快开阀quick opening valve快闭阀quick closing valve隔断阀isolating valve三通阀three way valve夹套阀jacketed valve非旋转式阀non-rotary valve2管子,管件,法兰管子pipe(按标准制造的配管用管)tube(不按标准规格制造的其它用管)钢管steel pipe铸铁管cast iron pipe衬里管lined pipe复合管clad pipe碳钢管carbon steel[C.S.]pipe合金钢管alloy steel pipe不锈钢管stainless steel[S.S.]pipe奥氏体不锈钢管austenitic stainless steel pipe铁合金钢管ferritic alloy steel pipe轧制钢管wrought-steel pipe锻铁管wrought-iron pipe无缝钢管seamless[SMLS] steel pipe焊接钢管welded steel pipe电阻焊钢管electric-resistance-welded steel pipe电熔(弧)焊钢板卷管electric-fusion(arc)-welded steel-plate pipe螺旋焊接钢管spiral welded steel pipe镀锌钢管galvanized steel pipe排污阀blowdown valve集液排放阀drip valve排液阀drain valve放空阀vent valve卸载阀unloading valve排出阀discharge valve吸入阀suction valve取样阀sampling valve手动阀hand operated(manually-operated) valve(水)龙头bibb;bib;faucet抽出液阀(小阀)bleed valve旁路阀by-pass valve软管阀hose valve混合阀mixing valve破真空阀vacuum breaker冲洗阀flush valve根部阀root (primary, header) valve水煤气钢管water-gas steel pipe塑料管plastic pipe玻璃管glass tube橡胶管rubber tube壁厚wall thickness[WT]壁厚系列号schedule number[SCH.NO.]加厚的,加强的extra heavy (strong)双倍加厚的,双倍加强的double extra heavy (strong) 弯头elbow异径弯头reducing elbow长半径弯头long radius elbow短半径弯头short radius elbow长半径180°弯头long radius return短半径180°弯头short radius return三通tee异径三通reducing tee等径三通straight tee带支座三通base tee45°斜三通45°lateralY型三通true"Y"四通cross异径管reducer同心异径管concentric reducer偏心异径管eccentric reducer管接头coupling;full coupling活接头union短管nipple预制弯管fabricated pipe bendU型弯管"U"bend法兰端flanged end万向接头universal joint对焊的butt welded[BW]螺纹的threaded[THD]承插焊的socket welded[SW]法兰flange[FLG]整体管法兰integral pipe flange钢管法兰steel pipe flange螺纹法兰threaded flange滑套法兰slip-on flange平焊法兰slip-on-welding flange承插焊法兰socket welding flange松套法兰lap joint flange[LJF]对焊法兰weld neck flange[WNF]法兰盖blind flange;blind异径法兰reducing flange压力级pressure rating(class)突面raised face[RF]凸面male face凹面female face全平面;满平面flat face;full face[FF]3.管道特殊件piping speciality粗滤器strainer过滤器filter临时过滤器temporary strainer(cone type)Y型过滤器Y-type strainerT型过滤器T-type strainer永久过滤器permanent filter洗眼器及淋浴器eye washer and shower 视镜sight glass阻火器flame arrester喷咀;喷头spray nozzle喷射器ejector取样冷却器sample cooler消音器silencer膨胀节expansion joint波纹膨胀节bellow补偿器compensator软管接头hose connection[HC]快速接头quick coupling金属软管metal hose橡胶管rubber hose挠性管flexible tube特殊法兰special flange漏斗funnel8字盲板spectacle (figure 8) blind爆破板rupture disk4,其它材料碳素钢carbon steel [C.S.]不锈钢stainless steel[S.S.]铸铁cast iron[C.I.]铝aluminum铜,紫铜copper钛titanium抗拉强度tensile strength非金属材料non-metallic material塑料plastic陶瓷ceramic搪瓷porcelain enamel玻璃glass橡胶rubber垫片gasket[GSKT]平垫片flat gasket填料packing型钢shaped steel角钢angle steel槽钢channel工字钢I-beam宽缘工字钢或H钢wide flanged beam扁钢flat bar圆钢round steel; rod钢带strap steel网络钢板checkered plate材料表bill of material[BOM]材料统计material take-off[MTO]散装材料bulk material综合管道材料表consolidated piping material summary sheet[CPMSS]汇总表summary sheet5.设备布置及管道设计中心线center line装置边界boundary limit[BL]区界area limit设备布置equipment arrangement (layout);plot plan 标高,立面elevation[EL]支撑点point of support[POS]工厂北向plant north方位orientation危险区hazardous area classification净正吸入压头net positive suction head绝对标高absolute elevation坐标coordinate管道研究piping study管道布置平面piping arrangement plan[PAP]管道布置piping assembly; layout详图detail"X"视图view "X""A-A" 剖视section "A-A"轴测图isometric drawing索引图key plan管道及仪表流程图piping and instrument diagram[P&ID] 管口表list of nozzles地上管道above ground piping地下管道under ground piping管线号line number总管header; manifold旁路by pass常开normally open常闭normally closed取样接口sampling connection伴热管tracing pipe蒸汽伴热steam tracing热水伴热hot-water tracing电伴热electrical tracing夹套管jacketed line全夹套管full jacketed 比例scale图figure草图sketch图例legend符号symbol件号part n。

离心泵外文翻译

离心泵外文翻译

JIANGSU UNIVERSITY本科毕业设计离心泵外文翻译学院名称:能动学院专业班级:动力流体0903 学生姓名:刘敏杰学号:3090201087指导教师:袁丹青、丛小青实用课程涡轮机械离心泵特性的测量杜伊斯堡-埃森大学工学院机械工程系涡轮机械Prof. Dr.-Ing. F.-K. Benra目录1离心泵概述1.1离心泵的应用领域及范围……………………………………………………………………………………1.2离心泵叶轮及水力设计2理论基础2.1叶轮的速度情况2.2流体在叶轮中被压缩2.3扬程的确定2.3.1有限叶片数的影响2.3.2叶片出口安放角2.4损失与效率2.5性能表现2.5.1离心泵性能特性2.5.2相似准则2.5.3离心泵的工况点2.5.4离心泵及其设备3离心泵的测试与调节3.1一种离心泵3.2离心泵的驱动设备3.3离心泵设备的启动3.4变量的测量3.4.1流动测量3.4.2压力的测量3.4.3转矩、转速等的测量4调试方法以及评价4.1阀门特性曲线4.2转速特性曲线4.3评估与总结文中对应符号下标及含义参考文献1.离心泵概述1.1离心式泵的应用范围1.2叶轮形式及水力设计1离心泵概述1.1离心泵的应用范围第一种离心式水泵已经在1689年由法国物理学家丹尼斯-帕潘。

自那时以来,离心泵进入各行各业,尤其是径向流类型的泵被大量应用在建筑行业的液体输送上。

除了水,其他类型的水也可以作为输送介质,特别是石油,但除此之外,腐蚀性液体或固液混合物也可以利用离1.2叶轮形式与水力设计尽管离心泵应用在各种行业内,其种类与形式很多,但是大致可以用H,V图来进行归纳(图1-2).根据流量,扬程,转速,叶轮形式,用以达到最高效率。

参考特殊形式的转速,根据不同的应用领域,叶轮的形式各不相同(图1-3).1.低比转速(n=10-30):带有简单弯曲叶片的径向式叶轮。

低流量,高扬程。

2.中比转速(n=30-50):叶轮径向流出,双曲面叶片设计,中流量,中扬程。

PumpSmart技术在离心泵节能及安全运行实践中的应用

PumpSmart技术在离心泵节能及安全运行实践中的应用

铜基镶嵌 自润滑 轴瓦使用 过程 中能够实 现免维 护 ,保
障 了生产 的顺利进行 。铜基镶嵌 自润滑轴瓦 的使用 寿命 为1 年 ,其综 合成本仅 为轴承 干油润滑 系统运行 费用 的十分之

l m / mi n 的极限载荷 :2 5 N / m m
最 高滑 动速 度 :干0 . 4 r r d s ,油5 r r d s
统浪 费 ,降低 了系统 的可 靠性和性 能。 由于离心泵 的过大 选型 ,需要使 用流量控制 阀( F C V ) 将 流量调 回正 常状 态 ,更
种 不 良的工况下 ,为泵提供保 护 ,减少大约7 5 %的维 护工作
量 和维修费用。
二 、 离 心 泵 的 节 能 减 排
多地控 制多余 流量 。 由于通过 阀的流体速率 较高 ,加速离 心泵 的腐 蚀和磨 损 ,即从 泵 、系统相 互作 用 的角度 来讲 ,
流量控制阀( F c V ) 增加 了系统 曲线 的磨损耗。 在泵送系统中 ,离 心泵 的选型有 以下几个原则 : ( 1 ) 满足工作中所需 的最 大流量和最大扬程 ; ( 2 ) 正常运行工况点尽可能靠 近其设计工况点 ;
P u m p S m a r t 专 门设计用 来实现泵 的节能降耗 ,它 由两部
摩 擦 系数 :< O . 1 6
的油管作 为吹 扫气源管路 。前期改 造后 ,运 行半年 ,使用
情况 良好 。所 以后期又对 剩余轴承 进行 了改 造 ,整套 系统
至今已经运行 了2 年多 ,效果显著。
三 、 经 济 效 益
最 高使 用温度 :3 0 0 — 4 0 0  ̄ C
极 限 动 载荷 :1 0 0 N / mm z

离心泵在炼油及化工厂中的应用(第二节) FINAL

离心泵在炼油及化工厂中的应用(第二节) FINAL
绿色环保
随着环保意识的日益增强,离心泵的设计和制造将更加注 重绿色环保,采用环保材料和制造工艺,减少对环境的污 染。
WENKU DESIGN
WENKU DESIGN
2023-2026
END
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感谢观看
KEEP VIEW
WENKU DESIGN
WENKU DESIGN
WENKU
REPORTING
经济性
选择具有良好声誉和可靠性的制造商,确 保泵的质量和性能。
在满足工艺要求的前提下,考虑泵的购置 、运行和维护成本,选择经济合理的方案 。
常见类型离心泵特点比较
单级双吸离心泵
具有平衡轴向力的特点,适用 于大流量、低扬程的场合。
自吸式离心泵
具有自吸能力,适用于输送含 有气体的介质或需要自吸的场 合。
运行管理规范及操作要点
严格遵守离心泵的操作 规程,确保设备的正常
运行和安全。
01
监控离心泵的运行状态, 及时发现并处理异常情 况,如泄漏、振动、噪
音等。
03
建立完善的设备档案, 记录离心泵的安装、调 试、运行和维护等相关
信息。
05
定期对离心泵进行维护 保养,包括更换润滑油、
清洗过滤器等。
02
对离心泵进行定期的性 能测试和评估,确保其 性能稳定并满足生产要
检查泵体、叶轮、轴等零部 件是否完好无损,无裂纹、
变形等缺陷。
确认离心泵型号、规格和性 能参数是否符合设计要求。
01
清理泵内及进出口管道内的
杂物和污垢,确保流道畅通。
02
03
检查电机的绝缘性能、接线 是否正确,以及接地是否可
靠。
04
05

外文翻译--泵的概述

外文翻译--泵的概述

外文原文:Pump's outlineThe pump is the application very widespread general machinery, may say that is place of the fluid flow, nearly has the pump in the work. Moreover, along with science's and technology's development, pump's application domain is expanding rapidly, according to the over-all state statistics, pump's power consumption approximately composes the national total output of electrical energy 1/5, obviously the pump is natural consumes energy the wealthy and powerful family. Therefore, raises the pump technical level to save the energy consumption to have the important meaning.First. Centrifugal pump's principle of workThe drive leads impeller revolving through the pump spindle to have the centrifugal force, under the centrifugal action of force, the liquid is flung along the leaf blade flow channel to the impeller export, the liquid sends in after the volute collection the eduction tube. The liquid obtains the energy from the impeller, • causes the pressure energy and the speed can increase, and depends upon this energy the hydraulic transport to the operating location. while the liquid is flung which exports to the impeller, the impeller eye center has formed the low pressure, • has had the differential pressure in the imbibition pot and between the impeller center liquid, in the imbibition pot's liquid under this differential pressure function, after inhales the pipeline and pump's suction chamber unceasingly enters in the impeller.Second, centrifugal pump's structure and main spare partA centrifugal pump mainly by the pump body, the impeller, the packing ring, the rotation axis, the axis seals parts and so on box to be composed, some centrifugal pumps are also loaded with the guide pulley, the inducer, the balance disc and so on.1. Pump body: Namely pump's shell, including suction chamber and delivery chamber.①Suction chamber: Its function is enables the liquid to flow in evenly the impeller.②Delivery chamber: Its function collects the liquid, and sends in it the subordinate impeller or guides the eduction tube, at the same time reduces the liquid the speed, causes the kinetic energy to further turn the pressure energy. The delivery chamber has the volute and the guide vane two forms.2. Impeller: It is in the centrifugal pump transmits the energy for the liquid only part, the impeller with the bond fixation on the axis, leads revolving alongwith the axis by the prime mover, passes to through the leaf blade prime mover's energy the liquid.Impeller classification:①According to liquid inflow classification: Single suction impeller (in impeller's one side has an entrance) and double attracts the impeller (liquid from impeller's lateral symmetry liudao impeller passage).②Is opposite according to the liquid in centerline's flow direction classification: Runoff type impeller, axial-flow propeller and interflow type impeller.③According to impeller's structural style classification: Shrouded impeller, open type impeller and semi-opened impeller.3. Axis: Is transmits the mechanical energy the important components, the • prime mover's torque passes to the impeller through it. The pump spindle is the pump rotor's major parts, on the axis is loaded with components and so on impeller, axle sleeve, balance disc. The pump spindle depending on the both sides bearing supporting, makes the high speed rotation in the pump, thus the pump spindle in a big way wants the bearing capacity, to be wear-resisting, to be anti-corrosive. Pump spindle's material selects the carbon steel or the alloy steel and after the quenching and retempering treatment generally.4. Packing ring: Is installs in the rotation impeller and the static pump housing (center-section and guide vane's assembly) between packing assembly. It is function is through controls between the two gap method, increases in the pump between the high and low pressure cavity the fluid flow resistance, reduces divulging.5. Axle sleeve: The axle sleeve is uses for to protect the pump spindle, causes it not to corrode and the attrition. When necessity, the axle sleeve may replace.6. Axis seals: The pump spindle and around packing box between end cover's installs short for axis to seal, mainly prevents in pump's liquid divulging and the air enters in the pump, achieves seals and prevents the air admission to cause the pump cavitation goal. the axis seals form: Namely has skeleton's rubber seal, the packing seal and the mechanical seal.7. axial force balancing unit.Third. Centrifugal pump's prime task parameter1. Current capacity: Namely the pump in unit of time discharges the liquid quantity, usually indicated with the Unit of volume that mark Q, the unit has m3/h, m3/s, l/s and so on,2. Lifting: The transportation unit weight's liquid (pump suction flange) (pump discharge flange) from the pump inlet place to the pump exit, its energy's increment, indicated with H, the unit is m.3. Rotational speed: Pump's rotational speed is the pump each minute revolving number of times, expressed with N. Electrical machinery rotational speed •N generally about 2900 n/min.4. Net positive suction head: Centrifugal pump's net positive suction head isNPSH • uses the expressed that pump's performance's main parameter,rsymbolic representation.5. Power and efficiency: Pump's power input is shaft power P, is also electric motor's output. Pump's output is the active power.Fourth, pump proper energy lossPump mechanical energy which obtains from the prime mover, has a part to transform into the liquid energy, but another part because in the pump consumes loses. In the pump all losses may divide into the following several items: 1. Hydraulic loss by the liquid in pump impact, the turbulent flow and the surface friction creates. The impact and the eddy current loss are because the liquid flow change direction produces. The liquid flows through the flow channel general meeting which contacts to present the surface friction, from this produces the energy loss is mainly decided by flow channel's length, the size, the shape, the surface roughness, as well as liquid speed of flow and characteristic.2. Volumetric loss: volumetric loss was already obtained the energy liquid to have a part to flee the result which in the pump the class and leaked outward.is 0.93~0.98 generally. Improves the packing Pump's volumetric efficiencyvring and the seal structure, may reduce the leakage, raises the volumetric efficiency.3. Mechanical loss mechanical loss refers to the impeller lap side and the pump housing friction loss between the liquid, namely the disc loses, as well as pump spindle when packing, bearing and balancing unit and so on mechanical part movement friction loss, generally before primarily.Fifth, pump's speed change--Proportionality law1. Centrifugal pump's speed change:A centrifugal pump, when its rotational speed change, its rated flow, lifting and the shaft power will have the change according to the certainproportion relations. At present, uses the frequency conversion velocity modulation electrical machinery to realize centrifugal pump's speed change, is a new important energy conservation way. 2. proportionality law expression:2121n n Q Q = 22121⎪⎪⎭⎫ ⎝⎛=n n H H 32121⎪⎪⎭⎫ ⎝⎛=n n N N In the formula, Q, H, N-- pump's rated flow, lifting and shaft power Thesubscript 1,2 express the different rotationalspeed separatelyn-- rotational speedSixth, centrifugal pump's ratio rotationCompared to the rotation is the comprehensive parameter which derives by the law of similarity, it is the operating mode function, to a pump, the different operating mode has differently compared to the rotation, for ease of carries on the comparison to the different type pump's performance and the structure, the application optimum condition (the peak efficiency spot) the ratio rotation represents this pump.When chooses the pump, may according to job requirement Q, H and unifies electrical machinery's rotational speed, calculates the n s number, determines pump's type approximately. At that time, 30<s n used the positive displacement pump generally, at that time, 30>s n used the centrifugal pump, the interflow pump, the axial flow pump and so on. Seventh,centrifugal pump'scavitation andinspirationcharacteristic1.Cavitation phenomenonsThe pumping station transportation medium's liquid condition and the gas are can transform mutually, the transformed condition is the pressure and the temperature. Under certain temperature, the liquid starts the critical pressure which vaporizes for the vaporization pressure. The temperature is higher, the liquid vaporization pressure is higher. Pump when revolution, if its overflow part local region (for example impeller blade import later somewhere), the liquid absolute pressure drops when pulled out delivers the liquid at that time under the temperature vaporization pressure, the liquid then in this place starts to vaporize, the bubble formation (air bubble internal pressure approximately wasequal to vaporization pressure). When these air bubbles along with liquid flow forward motion to high pressure region, down to around the air bubble high-pressured liquid causes the air bubble to reduce suddenly congeals. While air bubble vanishing, the liquid particle by the high speed packing hole, occurs hits mutually forms the intense pressure surge, causes the overflow part to receive the corrosion and the destruction. The above process is called the cavitation.2. Cavitation will cause serious results:(1). has the vibration and the noise.(2). is influential to pump's operating performance: When the cavitation develops the certain extent, the • steam bubble produces massively, will stop up the flow channel, will cause pump's current capacity, lifting, the efficiency and so on obviously to drop.(3). will have the destruction to flow channel's material quality: Is mainly nearby the leaf blade entrance the metal weary disintegration.3. centrifugal pump's inspiration characteristic:(1). Pump has the cavitation basic condition is: Under leaf blade entrance lowest liquid flow pressure k P <= this temperature liquid vaporization pressure v P .(2). effective net positive suction head: The pump entry (potential head is the entire flood peak which zero) the liquid has subtracts the value which the vaporization delivery head remains only, with expression.(3). pump essential net positive suction head: Liquid flow from pump inlet to impeller in minimal pressure point of force K place complete energy loss, with expression.(4). With r NPSH and a NPSH difference and relation:a NPSH >r NPSH Pump not cavitationa NPSH =r NPSH The pump starts the cavitationa NPSH <r NPSH Pump serious cavitation(5). regarding a pump, to guarantee that its safe operation does not have the cavitation, must the net positive suction head also be supposed to add asecurity allowance regarding the pump, therefore, pump's permission net positive suction head is:[]NPSH=()c1.1~NPSH5.14. Enhances the centrifugal pump anti-cavitation performance themethod to include:NPSH, is machine the pump (1). I mprovement machine pump structure, reducesrdesign question.(2). Enhancement installment effective net positive suction head. Most mainly the most commonly used method uses the irrigation inspiration installment.In addition, reduces the inspiration pipeline resistance loss as far as possible, reduces the liquid the saturated steam tension, namely when design inspiration pipeline selects caliber big as far as possible, length short, the bend and valve few, transportation liquid temperature as far as possible low and so on measures, may enhance the installment the effective cavitation remainder.5. axial force balancing unit(1). axial force production reason①Around because the impeller the both sides the fluid pressure distributed situation different (wheel cap lateral pressure is low, • wheel disk pressure high) causes axial force A1, its direction for from impeller back side direction impeller eye.②The fluid flows in and flows out dynamical reaction A2 which impeller's direction and the speed different produce, its direction and A1 are opposite, therefore line shaft directive force A=A1-A2, the direction is ordinary and A1 same (general A2 is small).(2). Axial force balanced①Uses double attracts the type impeller: The impeller lateral symmetry, the fluid from the both sides inspiration, the axial force automatic counter-balance achieves balanced.②Opens the balancing hole or installs the compensating pipe:A: Opens several balancing holes in the impeller wheel disk photograph well regarding the induction port place.B: After order to avoid the balancing hole, because the mainstream is disturbed increases the hydraulic loss, may suppose the compensating pipe to replace the balancing hole, namely uses an acorn tube leading-in point pressure to the wheeldisk back side.③Uses the balanced leaf blade: Casts several radial direction muscle piece at the back of the leaf wheel disk, the • muscle piece drives at the back of the impeller in the gap fluid to accelerate to revolve, increases the centrifugal force, •, thus causes at the back of the impeller the pressure obviously to reduce.④Using thrust bearing withstanding axial force. Generally in the small single suction pump the thrust bearing may withstand the complete axial force, prevents the pump spindle to flee moves.Eighth. centrifugal pump's operating procedure1. Centrifugal pump starts the inspection(1) Electrical machinery overhaul, before connecting the shaft coupling, inspects electrical machinery's rotation direction first to be whether correct.(2) inspection pumps out the inlet line and the attached pipeline, the flange, the valve installs whether to meet the requirement, foot bolt and grounding to be whether good, whether the shaft coupling does install.(3) jigger inspection, rotates whether normally.(4) inspection lubricating oil oil level is whether normal, refuels without the oil, and inspects the lubricating oil (fat) oil material nature.(5) turns on various cooling water valve, and inspects the pipeline to be whether unimpeded. Attention cooling water not suitable oversized or too small, will create the waste oversized, too small, then the cooling performance will be bad. Generally the cooling current of water becomes the striation(6) dozen of pumping's inlet valve, closes pump's outlet valve, and turns on the pressure gauge valve.(7) inspection machine pump's seal condition and oil seal opening. attention: The hot oil pump wants evenly before the start preheating.2. centrifugal pump's start(1) all operates the inlet valve, closes the outlet valve, the starting dynamo.(2), when the pump outlet pressure is bigger than the service pressure, inspects each work on six cylinders, turns on the outlet valve gradually.when(3) starting dynamo, if the start or has time the unusual sound, should the dump inspection, after eliminating the breakdown, immediately only then starts.when(4) start, pays attention to the human not to face the shaft coupling, by against departs offends somebody.3. the centrifugal pump stops the pump to operate(1) to close pump's outlet valve slowly.(2) shuts off electrical machinery's power source.(3) closes the pressure gauge valve.(4) parking, cannot stop the cooling water immediately, should pump's temperature only then cut off the water supply falling to 80 degrees below.(5) according to the need, closes the inlet valve, the pump body blows off.4. centrifugal pump operates when matters needing attention(1) centrifugal pump when revolution avoids the idle operation.(2) avoids when closes the outlet valve the long time revolution.(3) refuses the water used battery charger.the(4) centrifugal pump must in close in outlet valve's situation to start.中文译文:泵的概述泵是应用非常广泛的通用机械,可以说是液体流动之处,几乎都有泵在工作。

化工原理离心泵的应用

化工原理离心泵的应用

化工原理离心泵的应用简介离心泵是化工行业中常见的一种泵类设备。

它利用离心力将液体从低压区域抽取并转移到高压区域,广泛应用于化工生产中的流体输送、增压和循环系统等方面。

本文将介绍化工原理离心泵的应用及其优势。

应用领域离心泵在化工行业有着广泛的应用,包括但不限于以下几个方面:1.石油化工:离心泵常被用于原油抽送、精馏塔进料和产物输送等方面。

在石油炼制的过程中,离心泵的高效性能能够满足输送高温高压的原油和液化气等需求。

2.化学工程:离心泵在化学反应过程中扮演着重要的角色,可用于各种化学液体的输送、混合和循环。

例如,用于化学反应锅的进料泵和产物泵等。

3.冶金工业:离心泵常用于冶金行业,用于将冶金矿石、高温熔融的金属和废水等物质输送。

离心泵在冶金工业中的应用能够提高生产效率,并为后续处理过程提供便利。

4.电力工程:离心泵被广泛应用于电力工程中的循环水系统、冷却水系统和供水系统等。

离心泵的高效能力和稳定性能可以保证电厂正常运行,并提供足够的冷却和供水需求。

5.医药工业:离心泵在医药工业中用于输送药液、溶液、废液等,广泛应用于药品制造、注射液生产等工艺过程中。

优势及特点化工原理离心泵相较其他类型的泵具备以下优势和特点:•高效性能:离心泵以其高效、稳定的特点而闻名。

其结构紧凑、能耗低、效率高,能够在保证流量和压力的情况下减少能量的损耗。

•高扬程:离心泵在输送介质时能够产生较高的扬程,适用于液体输送中的高位差和长距离输送。

•安全可靠:离心泵的结构简单,运行过程中稳定可靠,不易发生意外情况,最大程度保障工作环境的安全性。

•适应性强:离心泵适用于各种介质的输送,包括清洁液体、腐蚀性液体、高温液体等,能够满足不同行业的不同需求。

•维护方便:离心泵结构简单,易于安装和维护。

维护过程中的零部件更换和保养相对简单,减少了维护成本和时间。

注意事项在化工原理离心泵的应用中,需要注意以下几个事项:•选型合理:根据具体应用的需求,选择适合的离心泵类型、型号和材质。

离心泵在化工生产中应用最为广泛

离心泵在化工生产中应用最为广泛

离心泵在化工生产中应用最为广泛,这是由于其具有性能适用范围广(包括流量、压头及对介质性质的失迎性)、体积小、结构简单、操作容易、流量均匀、故障少、寿命长、购置费和操作费均较低等突出优点。

因而,本章将离心泵作为流体力学原理应用的典型实例加以重点介绍。

一. 离心泵的基本结构和工作原理讨论离心泵的基本结构和工作原理,要紧紧扣住将动能有效转化为静压能这个主题来展开。

(一)离心泵的基本结构离心泵的基本部件是高速旋转的叶轮和固定的蜗牛形泵壳。

具有若干个(通常为4~12个)后弯叶片的叶轮紧固于泵轴上,并随泵轴由电机驱动作高速旋转。

叶轮是直接对泵内液体做功的部件,为离心泵的供能装置。

泵壳中央的吸入口与吸入管路相连接,吸入管路的底部装有单向底阀。

泵壳侧旁的排出口与装有调节阀门的排出管路相连接。

(二)离心泵的工作原理当离心泵启动后,泵轴带动叶轮一起作高速旋转运动,迫使预先充灌在叶片间液体旋转,在惯性离心力的作用下,液体自叶轮中心向外周作径向运动。

液体在流经叶轮的运动过程获得了能量,静压能增高,流速增大。

当液体离开叶轮进入泵壳后,由于壳内流道逐渐扩大而减速,部分动能转化为静压能,最后沿切向流入排出管路。

所以蜗形泵壳不仅是汇集由叶轮流出液体的部件,而且又是一个转能装置。

当液体自叶轮中心甩向外周的同时,叶轮中心形成低压区,在贮槽液面与叶轮中心总势能差的作用下,致使液体被吸进叶轮中心。

依靠叶轮的不断运转,液体便连续地被吸入和排出。

液体在离心泵中获得的机械能量最终表现为静压能的提高。

【动画】离心泵的基本结构和工作原理需要强调指出的是,若在离心泵启动前没向泵壳内灌满被输送的液体,由于空气密度低,叶轮旋转后产生的离心力小,叶轮中心区不足以形成吸入贮槽内液体的低压,因而虽启动离心泵也不能输送液体。

这表明离心泵无自吸能力,此现象称为气缚。

吸入管路安装单向底阀是为了防止启动前灌入泵壳内的液体从壳内流出。

空气从吸入管道进到泵壳中都会造成气缚。

离心泵毕业论文中英文资料对照外文翻译文献

离心泵毕业论文中英文资料对照外文翻译文献

离心泵毕业论文中英文资料对照外文翻译文献离心泵中英文资料对照外文翻译文献文献名称(外文)CENTRIFUGAL PUMPS IN THE CHEMICAL INDUSTRYAbstract : A centrifugal pump converts the input power to kinetic energy in the liquid by accelerating the liquid by a revolving device - an impeller. The most common type is the volute pump. Fluid enters the pump through the eye of the impeller which rotates at high speed. The fluid is accelerated radially outward from the pump chasing. A vacuum is created at the impellers eye that continuously draws more fluid into the pump . This article stresses on a series of centrifugal pumps,From a brief introduction to the principles.Keywords: centrifugal pump ,Introduction ,Working principle , Cavitation ,Mechanism of Cavitation ,Solution and Remedies1. IntroductionPump ,device used to raise ,transfer ,or compress liquids and gases .Four general classes of pumps for liquids are described below .In all of them ,steps are taken to prevent cavitation (the formation of a vacuum) ,which would reduce the flow and damage the structure of the pump .Pumps used for gases and vapors are usually known as compressors .The study of fluids in motion is called fluid dynamics.Water pump ,device for moving water from one location to another ,using tubes or other machinery .Water pumps operate under pressures ranging from a fraction of a pound to more than 10,000 pounds per square inch .Everyday examples of water pumps range from small electric pumps that circulate and aerate water in aquariums and fountains to sump pumps that remove water from beneath the foundations of homes .One type of modern pumps used to move water is the centrifugal pump .Early version of the centrifugal pump ,the screw pump ,consists of a corkscrew-shaped mechanism in a pipethat ,when rotated ,pulls water upward .Screw pumps are often used in waste-water treatment plants because they can move large amounts of water without becoming clogged with debris .In the ancient Middle East the need for irrigation of farmland was a strong inducement to develop a water pump .Early pumps in this region were simple devices for lifting buckets of water from a source to a container or a trench .Greek mathematician and inventor Archimedes is thought to have devised the first screw pump in the third century BC .Later Greek inventor Ctesibius develop the first lift pump .During the late 17th and early 18th Centuries AD ,British engineer Thomas Savery ,French physicist Denis Papin ,And British blacksmith and inventor Thomas Newcomen contributed to the development of a water pump that used steam to power the pump’ piston .The steam-powered water pump’s first wide use was in pumping water out of mines .Modern-day examples of centrifugal pumps are those used at the Grand Coulee Dam on the Columbia River .This pump system has the potential to irrigate over one million acres of land .Also known as rotary pumps ,centrifugal pumps have a rotating impeller ,also known as a blade ,that is immersed in the liquid .Liquid enters the pump near the axis of the impeller ,and the rotating impeller sweeps the liquid out toward the ends of the impeller blades at high pressure .The impeller also gives the liquid a relatively high velocity that can be converted into pressure in a stationary part of the pump ,known as the diffuser .In high-pressure pumps ,a number of impeller may be used in series ,and the diffusers following each impeller may contain guide vanes to gradually reduce the liquid velocity .For lower-pressure pumps ,the diffuser is generally a spiral passage ,known as a volute ,with its cross-sectional area increasing gradually to reduce the velocity efficiently .The impeller must be primed before it can begin operation ,that is ,the impeller must be surrounded by liquid when the pump is started .This can be done by placing a check valve in the suction line ,which holds the liquid in the pump when the impeller is not rotating .If this valve leaks ,the pump may need to be primed by the introduction of liquid from an outside source such as the discharge reservoir .A centrifugal pump generally has a valve in the discharge line to control the flow and pressure .For low flows and high pressures ,the action of the impeller is largely radial .For higher flows and lower discharge pressure ,the direction of the flow within the pump is more nearly parallel to the axis of the shaft ,and the pump is said to have an axial flow .The impeller in this case acts as a propeller .The transition from one set of floe conditions to the other is gradual ,and for intermediate condition , the device is called a mixed-flow pump .2.The Centrifugal PumpThe centrifugal pump is by far the most widely used type in the chemical and petroleum industries .It will pump liquids with very wide ranging properties and suspensions with a highsolids content including ,for example ,cement slurries ,and may be constructed from a very wide rang of corrosion resistant materials .The whole pump casing may be constructed from plastic such as polypropylene or it may be fitted with a corrosion-resistant lining .Because it operates at high speed ,it may be directly coupled to an electric motor and it will give a high flow rate for its size .In this type of pump ,the fluid is fed to the centre of a rotating impeller and is thrown outward by centrifugal action .As a result of the high speed of rotation the liquid acquires a high kinetic energy and the pressure difference between the suction and delivery sides arises from the conversion of kinetic energy into pressure energy .The impeller consists of a series of curved vanes so shaped that the flow within the pump is as smooth as possible .The greater the number of vanes on the impeller ,the greater is the control over the direction of the liquid and hence the smaller are the losses due to turbulence and circulation between the vanes .In the open impeller ,the vanes are fixed to a central hub ,whereas in the closed type the vanes are held between two supporting plates and leakage across the impeller is reduced .As will be seen later ,the angle of the tips of the blades very largely determines the operating characteristics of the pump .The liquid enters the casing of the pump,normally in an axial direction,and is picked up by the vanes of the impeller.In the simple type of centrifugal pump,the liquid discharges into a volute,a chamber of gradually increasing cross—section with a tangential outlet.A volute type of pump is shown in Fig.(a).In the turbine pump[-Fig.(b)]the liquid flows from the moving vanes of the impeller through a series of fixed vanes forming a diffusion ring.This gives a more gradual change in direction to the fluid and more efficient conversion of kinetic energy into pressure energy than is obtained with the volute type.The angle of the leading edge of the fixed vanes should be such that the fluid is received without shock.The liquids flows along the surface of the impeller vane with a certain velocity whilst the tip of the vane is moving relative to the casing of the pump.The direction of motion of the liquid relative to the pump casing--and the required angle of the fixed vanes—is found by compounding these two velocities.In Fig.c,c.v u is the velocity of the liquid relative to the vane and t u is the tangential velocity of the tip of the vane ;compounding these two velocities gives the resultant velocity 2u of the liquid .It is apparent ,therefore ,that the required vane angle in the diffuser is dependent on the throughput ,the speed of rotation ,and the angle of the impeller blades .The pump will therefore operate at maximum efficiency only over a narrow range of conditions .Virtual head of a centrifugal pumpThe maximum pressure is developed when the whole of the excess kinetic energy of the fluid is converted into pressure energy. As indicated below .the head is proportional to the square of the radius and to the speed ,and is of the order of 60m for a single —stage centrifugal pump ;for higher pressures ,multistage pumps must be used .Consider the liquid which is rotating at a distance of between r and r+dr from the centre of the pump(Fig .d).dThe mass of this element of fluid dm is given by 2πrdrdρ,where ρ is the density of the fluidand 6 is the width of the element of fluid 。

离心泵在炼油及化工厂中的应用(附录一) FINAL共77页文档

离心泵在炼油及化工厂中的应用(附录一) FINAL共77页文档

(1) 内装式:静环装在压盖内侧,静环端面面向工作腔。
(用于温度、压力较高,腐蚀性不强的场合)
(2) 外装式:静环装在压盖外侧,静环端面背向工作腔。
(用于低压、腐蚀性强的场合)
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(八)内流式和外流式机械密封 (一般和内装式、外装式一致)
(1)内流式:泄漏方向朝向轴心。(一般密封都采用这 种结构)
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(十)平衡型和非平衡型机械密封 (1)平衡型:载荷系数K<1.0 (用于高压场合) (2)非平衡型:载荷系数K≥1.0 (用于普通压力场合)
(十一)补偿机构形式
(1)磁力:系统压力较低时用 (2)波片弹簧、锥形弹簧、螺旋圆柱大弹簧、小弹簧 (3)橡胶波纹管、聚四氟乙烯波纹管、金属波纹管
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二、机械密封的基本零件
(一)对摩擦副密封环的要求 (二)摩擦副匹配要考虑的因素 (三)密封端面宽度 (四)密封环的主要技术要求 (五)摩擦副端面平面度检测 (六)密封端面的粗糙度要求 (七)动环(旋转环) (八)静环(不旋转) (九)密封环的种类 (十)整体式密封环
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(二)摩擦副匹配要考虑的因素
(1)一般选择一软一硬的材料配对,软环作窄环,如 YG6/M106K,只有介质含固体颗粒、易结晶、粘度高 时才选用硬对硬。
(2)尽量采用内装、内流式结构,防止机械杂质进入密封 端面,减少泄漏量。
(3)选导热性良好材料作动环。
以利散热,降低端面温度。
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(十一)硬质合金表面灼伤和裂纹 (十二)其它故障简介 (十三)泵抽空密封失效现象 (十四)密封腔中汽蚀,密封失效现象 (十五)密封端面汽化的失效现象 (十六)泵振动过大的失效现象 (十七)没有冲洗的故障现象 (十八)动环选材注意事项

有关离心泵的中英翻译

有关离心泵的中英翻译

附录(一):Optimizing centrifugal pump operationCentrifugal pump operation is more than switching the pump on and directing the discharge flow to the required delivery point. This holds true even when a control value is installed in the discharge line for the purpose of flow or level control .A few very essential operating guidelines must be adhered to if early bearing or seal failure, premature erosion of internal wetted surfaces, or metal-to-metal contact of internal rotating and stationary surfaces, is to be avoided. In this article, Stan Shiels addresses the fundamentals of proper centrifugal pump operation and the most common areas of improper centrifugal pump operation. It is assumed that the pump has been successfully commissioned.The most common cause of centrifugal pump failure, separate from those causes associated with maintenance and/or design, but associated with how the pumps are operated may be summarized as follows:1. Insufficient suction pressure to avoid cavitation.2. Excessively high flow rate for the net positive suction head available (NPSHA).3. Prolonged operation at lower than acceptable flow rates.4. Operation of the pump at zero or near zero flow rate.S. Improper operation of the pump in parallel.6. Failure to maintain adequate lubrication for the bearings.7. Failure to maintain satisfactory flushing to mechanical seals.Insufficient suction pressure to avoid cavitation.While the provision of sufficient suction pressure to avoid cavitation may seem straightforward, requiring only that the net positive suction head available(NPSHA) be always greater than or equal to the net positive suction head required (NPSHR) by the pump, some misconceptions need to be revealed. When the pump manufacturer develops the pump's NPSHR curve, the calculated values of NPSHR are for conditions where theexpected head (as determined by the previously performed pumphydraulic performance test) has fallen of by 3% for that specific flow rate. This means that mild cavitation will exist when the NPSHA equals the NPSHR. Because of this a comfort margin of 3 feet, or 1meter, isrecommended, when determining the minimum acceptable NPSH margin:(NPSHA-NPSHR).The following piping faults will require an NPSH margin greater than 3 feet(1 meter) to ensure the absence of cavitation.~Where the inlet piping configuration is such that a number of 90 degree turns occur, in different planes, fairly close to the pump suction, the resultant fluid swirl will cause cavitation to occur, on occasion, even when the NPSH margin is 2 to 3 feet.~Where an eccentric inlet reducer is positioned in the pipe such that itforces asymmetric flow into the suction of a double suction pump. The side of the double suction impeller that receives the disproportionately higher percentage of the total flow will incur cavitation at an NPSHA much higher than the NPSHR indicated on the manufacturer's test curve.Excessively high flow rate for the NPSH availableBased upon the simple fact that NPSHA decreases as flow rate increases, and NPSHR increases as flow rate increases, there should be considerable effort place on ensuring that the point of intersection of these two parameters is not reached. This concept is illustrated in Figurel.Many centrifugal pumps are installed in a system, which cannot pro vide adequate suction pressure to avoid cavitation, if operated at flow rates much above their best efficiency point (BEP). It is probably never intended to operate these pumps in such a region, but transient conditions can often lead to intended operation at much higher than expected flow rates. One example is the case where a recycle control value has been installed to ensure that the pump is not operated below a minimum acceptable flow rate. At very low or zero process flow the recycle control value may attain a position of greater than 50% open. This of itself is not a problem, but the extremely high flow rate may occur when the process control value is again asked to open, and does so rather quickly. When the process control valve is faster acting than the recycle control valve, the combined process and recycle flows may necessitate a higher NPSHR than the suction system can provide.Manual operation must also be handled carefully when simple transfer operations between vessels is called for. At the start of such operation the receiving vessel may have a very high level. This leads to a negative static head, which can lead to an initial high flow rate until the level rises in the discharge vessel. This is a particularly risky operation where piping system resistance is low on the discharge side, but a relatively long section of suction piping exists.Prolonged operation at lower than acceptable flow ratesA centrifugal pump is most comfortable operating between 85% and 110% of its best efficiency point (BEP). However, by far the great majority of centrifugal pumps are forced to operate outside of this range. The degree to which it is acceptable to operate outside of this range is a function of two primary parameters:Suction Specific Speed (Ss) and Specific Speed (S). These parameters may be calculated for a pump provided the following data is known: For maximum diameter impeller:BEP FlowNPSHR at BEP FlowHead at BEP FlowPump Operating Speed (RPM)The following formulae allow Ss and S to be calculated:()0.50.750.50.75()()()bep bepbep bep SpecificSpeed S REP Q H SuctionSpecificSpeed Ss RPE Q NPSHR=⨯÷=⨯÷Where: QPM is pump rotational speed in revolutions per minute.bep Q flow at BEP for maximum diameter impeller.bep H is pump head at BEP for maximum diameter impeller.bep NPSHR is the pump net positive head required at BEP for maximum diameter impeller.The acceptable minimum continuous flow rate, which a centrifugal pump can be expected to endure without incurring damage or premature failure is also affected by a number of other parameters: such as, impeller head, fluid specific gravity , and percentage of total running time spent at the lower flow rate. When the pump's specific speed and suction specific speed are known the approximate percentage of the pump's maximum impeller diameter BEP flow at which suction recirculation can be expected to occur may be estimated.From this estimate the approximate minimum acceptable continuous flow rate for that specific pump may be estimated. Impeller geometry can be optimized to improve on initial estimates and, when conditions are marginal, it is always advisable to consult with the manufacturer's application engineer before deciding on the acceptable minimum continuous flow rate.A subsequent article can expend further on this much debated area of centrifugalpump operation. In the interim it is suggested that pump users request the minimum "stable" continuous flow rate recommended from the pump manufacturer, based upon the onset of flow instability .Impeller geometry can impact the "Cavitation Coefficient" which is defined by the following formula:211(2)u g NPSH u δ=⨯÷Where1u δ is the cavitation coefficientg is the gravitation constantNPSH is net positive suction head1u is fluid circumferential velocity at impeller entryThis is a dimensionless coefficient and would be valid for all geometrically similar pumps, independent of their size and speed of rotation.Operation of the pump at zero or near zero flow rateCentrifugal pumps are often used to pump out vessels, often to zero level. The pumps can, at times, be left unattended. If the level is allowed to fall to the point where the pump is allowed to run dry , failure of the mechanical seal will often follow rapidly. In such applications even a small recycle flow back to the suction vessel will not alleviate the problem, as the pump will still be able to empty the vessel. Many such applications are best protected by the installation of dual pressurized mechanical seals which will remain lubricated even during periods of completely dry running. In non hazardous applications a pump sealed with packing will survive better if the packing is lubricated from an external source; the source must, of course, be compatible with the fluid being pumped.Where batch delivery is normal operation, such that the pump will operate for long periods, but delivery is intermittent, a small continuous recycle flow back to the suction source will help to protect the pump during periods when delivery stops (typically by closing the delivery valve). Lack of some of the recycle protection for a centrifugal pump, which will see periods of zero flow, will certainly cause frequent pump failure. Any centrifugal pump operated at zero flow for even a few minutes will vapour temperature. It is worth remembering that once a pump has vapour-locked it will not generate any noticeable discharge pressure differential. Usually it is necessary to stop the pump and allow the gas to condense back into liquid, before pumping can resume.Improper operation of the pump in parallel.This topic has been covered in detail in a previous "Pump Academy" article, but the basics are worthy of mention in terms general centrifugal pump operating philosophy. The following principles should be applied to any operation of centrifugal pumps, which requires either continuous or intermittent parallel operation.~Shut-off heads of all pumps operating in parallel should be comparable typically as close as possible, with difference of no more than 2%or 3% recommended~V ery flat performance curves in one or more of the pumps operating in parallel is to be avoided;a drop of 10% to 20% between the shut-off and rated points is recommended. The point of hydraulic shut-off of the more worn pump of two initially identical pumps operating in parallel is shown in Figure 2, for high head rise to shut-off and low head rise to shut-off.~Multistage pumps, or expensive single-stage or two-stage pumps designed to operate in parallel, should be protected by low flow shut-down devices to avoid severe damage from occurring at transient low combined flow conditions. While the pumps may be identical, performance differences occur over time, and the better performing pump will effectively "shut-off" the weaker pump below a specific combined flow rate. The low flow shut-down will prevent the major damage that often results from such occurrences.~inlet and discharge piping configurations and lengths should be comparable between the pump and the suction and discharge headers. Proper piping configuration for pumps operating in parallel should include suction and discharge headers of larger diameter than the lines leading to and from the individual pumps. Differences in suction and/or discharge piping configuration will always lead to a disparity in pump flow rates.Failure to maintain adequate lubrication for the bearingsThis is a simple statement and sounds too fundamental to be ignored, but, even among those diligent pump operators who strive to maintain adequate lubrication, some inadvertent mistakes are made. Lubrication of rolling element bearings is the subject here. They may be oil lubricated or grease lubricated. The complete topic requires more attention than can be afforded in this text, but the basic essentials always hold true and can only be ignored at the risk of early pump failure.Oil lubrication is of three basic types: forced feed with a pressurized filtered and cooled oil supply to the bearings in a closed loop system; oil bath; and oil mistThe forced feed system is the most complicated and usually incorporates a low oil pressure shutdown protection; it is normally only present in large multistage pump installations. The key areas of concern are:~Maintenance of the correct viscosity of the oil and periodic monitoring for changes in viscosity and/or Total Acid Number (TAN) and the presence of water in the oil.~On occasion ferrographic analysis for the presence of wear particles helps to diagnose impendent bearing damage.~Lube oil cooler performance decline may lead to elevated temperatures and periodic oil temperature monitoring is also essential.~Oil filter differential pressure and main oil supply pressure to the bearings also requires frequent attention.A housing for oil bath lubrication normally incorporates a constant level oiler, although some pump users have chosen to seal their bearing housing and use synthetic oil, changing the oil only once every two or three years. For those bearing housings incorporating a constant level oiler the following basic principles apply:~Use of the correct viscosity oil for the operating temperature of the bearing (refer to the bearing manufacturer's literature).~Maintenance of a reserve of oil in the constant level oiler.~Clean storage of the make-up oil to prevent foreign material and/or moisture from entering the bearings.~Observance of the deterioration in the oiler level一remember, oilers whose level never falls over time may have a blocked connection between the oiler and the bearing housing.Oil mist lubrication requires that the same viscosity oil be used as for oil bath lubrication. On occasion a grade lighter oil may be used as the oil is being constantly replenished, although this approach should be taken with caution. While most oil mist systems incorporate an alarm for loss of oil mist pressure, each bearing housing should be periodically checked to confirm adequate venting of oil mist from the housing, and for proper condensation and drainage of bearing housing oil mist condensate collection pots.Grease lubrication of rolling element bearings requires proper attention to the following:~The type of grease used. A stiffer grease for higher speeds (3000 RPM and above) and a softer grease for lower speeds.~The grease should essentially contain the same viscosity of oil in it as that required for oil bath luibrication.~The amount of grease. This is of particular importance where pump operators are responsible for regreasing of bearings, as a major cause of failure of grease lubricated pump bearings is overgreasing. The idea that more is better is very wrong here.~Compatibility of greases. When regreasing it is essential that the grease to be added is compatible with the originally installed grease.As is the case for oil type selection, it is recommended that the bearing applications engineering department be consulted, when in doubt about which grease is best for each specific application.Failure to maintain satisfactory flushing to mechanical sealsThe flushing plan for a mechanical seal is the means of controlling the environment in which the seal operates. It follows then that any event that alters the intended flushing flow parameters will alter the seal's environment and may lead to seal failure. The following parameters, for some of the most commonly utilized seal flushing arrangements, should be regularly monitored for mechanical seals:Pump discharge flush to the seal to confirm that the temperature is correct. The dischargeflush should be at the same temperature as the pump discharge flow. In hot service a cooler flush will indicate lack of sufficient flow; this is often the only means available of checking flow, as most discharge flush plans do not have a flow indication.Suction flush from the seal cavity to the pump suction should also be checked for temperature. This may require that the temperature be checked initially to set a "benchmark." Any noticeable increase in this flush return to the pump suction may indicate a flow restriction.Cooled discharge flushes require adequate cooling to attain the required flush temperature. Discharge flush coolers foul over time and often the flush temperature is allowed to rise to the point of seal failure before cooler fouling is discovered. Both the cooling water differential temperature and the flush supply temperature to the seal should be monitored and the cooler replaced of cleaned before fouling progresses too far.Dual unpressurized seals rely on a head of liquid in a seal pot to provide a small pressure differential between the seal interspace and atmosphere. Both the seal pot level and the seal pot pressure should be observed for signs of change. Dualunpressurized seals are often utilized in volatile fluid service, where the vapour pressure is above atmospheric and any normal primary seal vapour leakage can be vented through the seal pot orifice to a safe collection point; a noticeable increase in seal pot pressure would indicate a primary (inner) seal failure. A reduction in seal pot level would indicate an outer seal failure.Dual pressurized seals incorporating a seal pot similarly should be monitored. The seal pot pressure must be maintained at a pressure above the seal cavity pressure for satisfactory seal operation. A reduction in seal pot level will indicate either a primary or or outer seal failure; further observation for obvious leakage of the outer seal is required to determine which one has failed. Loss of seal pot pressure may indicate a failure of the pressure blanketing system. Alarms are usually incorporated in dual seal systems incorporating seal pots. It is still advisable to monitor these parameters to allow early warning of loss of adequate seal flushing.Dual pressurized seals utilizing a flow-through barrier fluid system should have regular checks carried out for barrier fluid inlet and outlet temperatures and pressures. If the barrier fluid return pressure is allowed to drop to a value below the seal cavity (pump side) pressure, seal failure will follow in a pump media containing abrasives. Not all such systems have flow indication and a rise in differential temperature will usually indicate an increase in leakage rate of the inner seal, but could signify a reduction in barrier fluid flow rate; where flow rate is not subject to change it normally indicates an increase in inner seal leakage rate. A check of barrier fluid inlet pressure to the seal will assist in the diagnosis. A drop in barrier fluid return pressure, usually accompanied by arise in return temperature, is almost always associated with an inner seal failure.A last wordWhile there are many more causes of operational failure of centrifugal pumps, this discussion has dealt with the most frequently contributing areas. The operators of centrifugal pumps must extend their scope into the area of "ownership: Operators need to become familiar with tow these pumps operate, their key areas to monitor, and what to look for. It could also be said that many large process plants, which operate a large number of centrifugal pumps, do not provide sufficient pump training to permit the operating staff to understand key operating principles and satisfactory monitoring guidelines. We enjoy driving our automobiles. When have maintenance carried out: oil change, engine tune-up, transmission checked, brakes overhauled,tires renewed, fluid levels checked, hoses replaced, etc. most of us do not drive our cars until the oil breaks down completely and seizes the engine, the coolant hose blows, the brakes fail, the tires lose their tread, or the transmission fails. Periodic checks allow us to avoid such failures. We own our cars and do not want to incur the cost and inconvenience of such failures. A similar frame of mind toward centrifugal pump operation, supported by a proper program of operator training will pay dividends in terms of pump reliability and the cost of pump operation, and avoid some costly process debits.附录(二):优化离心泵的操作操作离心泵不仅指打开水泵阀门、接通排水管、导出排放液体到规定传输点还包括在排水管中安装控制阀以控制调节流量和液位等为了避免早期轴承或密封失效、内部潮湿表面过早浸蚀、以及内部旋转和固定部分金属表面发生摩擦等状况发生,在操作离心泵时须遵循一定的操作原则, 本文中,Stan Shiels给出了离心泵合理操作的基本法则和不正确使用离心泵的常见误区本文假设离心泵正常投入运行。

多级离心泵的工作原理及使用方法

多级离心泵的工作原理及使用方法

多级离心泵的工作原理及使用方法Centrifugal pumps work by converting mechanical energy from a motor into hydraulic energy in the form of flow and pressure. 多级离心泵通过将电机的机械能转换成流量和压力形式的液压能量。

This is achieved through the rotation of an impeller, which accelerates the fluid and then transfers it to the pump casing, where the kinetic energy is converted into pressure. 这是通过叶轮的旋转来实现的,叶轮加速流体然后将其传递到泵壳中,在泵壳中将动能转换成压力。

The impeller rotation creates a low pressure at the center, causing the fluid to be drawn into the pump and then pushed out through the discharge outlet. 叶轮的旋转在中心形成低压,导致流体被吸入泵中然后通过排出口排出。

This continuous flow and pressure generation make centrifugal pumps an essential part of various industrial and commercial applications. 这种连续的流动和压力生成使得离心泵成为各种工业和商业应用中必不可少的一部分。

With the ability to handle large flow rates and moderate to high-pressure levels, they are widely used in water supply, drainage, HVAC systems, and many other fields. 凭借其处理大流量和中高压水平的能力,它们被广泛应用于供水、排水、暖通系统和许多其他领域。

化工设备常用词汇中英文对照

化工设备常用词汇中英文对照

化工设备泵pump轴流泵axial flow pump真空泵vacuum pump屏蔽泵canned pump柱塞泵plunger pump涡轮泵turbine pump涡流泵vortex pump离心泵centrifugal pump喷射泵jet pump转子泵rotary pump管道泵inline pump双作用往复泵double action reciprocating pump计量泵metering pump深井泵deep well pump齿轮泵gear pump手摇泵hand(wobble)pump螺杆泵screw (spiral)pump潜水泵submersible pump斜转子泵inclined rotor pump封闭式电磁泵hermetically sealed magnetic drive pump 气升泵air—lift-pump轴承bearing叶轮impeller虹吸管siphon高压容器high pressure vessel焚化炉incinerator火焰清除器flame arrester工业炉furnace烧嘴burner锅炉boiler回转窑rotary kiln加热器heater电加热器electric heater冷却器cooler冷凝器condenser换热器heat exchanger反应器reactor蒸馏釜still搅拌器agitator混合器mixer静态混合器static mixers管道混合器line mixers混合槽mixing tanks破碎机crusher磨碎机grinder研磨机pulverizer球磨机ballmill过滤器filter分离器separator干燥器drier翅片fins烟囱stack火炬flare筛子screen煅烧窑calciner倾析器decanter蒸发器evaporator再沸器reboiler萃取器extractor离心机centrifuger吸附(收)器adsorber结晶器crystallizer电解槽electrolyzer电除尘器electric precipitator洗涤器scrubber消石灰器slaker料仓bin料斗hopper加料器feeder增稠器thickener澄清器clarifier分级器classifier浮洗器flocculator废液池sump喷射器ejector喷头sprayer成套设备package unit仪器设备apparatus附属设备accessory旋转式压缩机rotary compressor往复式压缩机reciprocating compressor 水环式压缩机nash compressor螺杆式压缩机helical screw compressor 离心式压缩机centrifugal compressor 多级压缩机mutiple stages compressor 固定床反应器fixed bed reactor流化床反应器fluidized bed reactor管式反应器tubular reactor列管式换热器tubular heat exchanger螺旋板式换热器spiral plate heat exchanger 萃取塔extraction column板式塔plate column填料塔packed column洗涤塔scrubber吸收塔absorber冷却塔cooling tower精馏塔fractionating tower汽提塔stripper再生塔regenerator造粒塔prill tower塔附件tower accessories液体分配(布)器liquid distributor填料支持板support plate定距管spacer降液管downcomer升气管chimney顶(底)层塔盘top (bottom)tray挡板baffle抽出口draw nozzle溢流堰weir泡罩bubble cap筛板sieve plate浮阀float valve除沫器demister pad塔裙座skirt椭圆封头elliptical head高位槽head tank中间槽intermediate tank加料槽feed tank补给槽make—up tank计量槽measuring tank电解槽cell溜槽chute收集槽collecting tank液滴分离器knockout drum稀释罐thinning tank缓冲罐surge drum回流罐reflux drum闪蒸罐flash drum浮顶罐floating roof tank内浮顶罐covered floating roof tank球罐spheroid气柜gas holder湿式气柜wet gas-holder干式气柜dry gas-holder螺旋式气柜helical gas—holder星型放料器,旋转阀rotary valve抽滤器mutche filter压滤器filter press压滤机pressure filter板框压滤器plate-and—fram filter press 转鼓过滤器rotary drum filter带式过滤器belt filter翻盘式过滤器袋滤器bag filter旋风分离器cyclone separator盘式干燥箱compartment tray drier真空干燥器vacuum drier隧道式干燥器tunnel drier回转干燥器rotary drier穿流循环干燥器through circulation drier 喷雾干燥器spray drier气流干燥器pneumatic conveyor drier圆盘式加料器dish feeder螺旋式加料器screw feeder颚式破碎机jaw crusher回转破碎机gyratory crusher滚洞破碎机roll crusher锤式破碎机hammer crusher冲击破碎机rotor impact breaker气流喷射粉碎机jet pulverizer棍磨机rod mill雷蒙机raymond mill锤磨机hammer mill辊磨机roller mill振动筛vibrating screen回转筛rotary screen风机fan罗茨鼓风机root's blower起重机crane桥式起重机bridge crane电动葫芦motor hoist发电机generator电动机motor汽轮机steam turbine。

离心泵调节方式与能源耗损分析论文中英文资料对照外文翻译文献

离心泵调节方式与能源耗损分析论文中英文资料对照外文翻译文献

离心泵论文中英文资料对照外文翻译附录A 译文(一)离心泵使用时的调节方式与能源耗损分析离心泵是广泛应用于化工工业系统的一种通用流体机械。

它具有性能适应范围广(包括流量、压头及对输送介质性质的适应性)、体积小、结构简单、操作容易、操作费用低等诸多优点。

通常,所选离心泵的流量、压头可能会和管路中要求的不一致,或由于生产任务、工艺要求发生变化,此时都要求对泵进行流量调节,实质是改变离心泵的工作点。

离心泵的工作点是由泵的特性曲线和管路系统特性曲线共同决定的,因此,改变任何一个的特性曲线都可以达到流量调节的目的。

目前,离心泵的流量调节方式主要有调节阀控制、变速控制以及泵的并、串联调节等。

由于各种调节方式的原理不同,除有自己的优缺点外,造成的能量损耗也不一样,为了寻求最佳、能耗最小、最节能的流量调节方式,必须全面地了解离心泵的流量调节方式与能耗之间的关系。

1 泵流量调节的主要方式1.1 改变管路特性曲线改变离心泵流量最简单的方法就是利用泵出口阀门的开度来控制,其实质是改变管路特性曲线的位置来改变泵的工作点。

1.2 改变离心泵特性曲线根据比例定律和切割定律,改变泵的转速、改变泵结构(如切削叶轮外径法等)两种方法都能改变离心泵的特性曲线,从而达到调节流量(同时改变压头)的目的。

但是对于已经工作的泵,改变泵结构的方法不太方便,并且由于改变了泵的结构,降低了泵的通用性,尽管它在某些时候调节流量经济方便[1],在生产中也很少采用。

这里仅分析改变离心泵的转速调节流量的方法。

从图1中分析,当改变泵转速调节流量从Q1下降到Q2时,泵的转速(或电机转速)从n1下降到n2,转速为n2下泵的特性曲线Q-H 与管路特性曲线He=H0+G1Qe2(管路特曲线不变化)交于点A3(Q2,H3),点A3为通过调速调节流量后新的工作点。

此调节方法调节效果明显、快捷、安全可靠,可以延长泵使用寿命,节约电能,另外降低转速运行还能有效的降低离心泵的汽蚀余量NPSHr ,使泵远离汽蚀区,减小离心泵发生汽蚀的可能性[2]。

过程装备与控制工程专业外语(原文+翻译)

过程装备与控制工程专业外语(原文+翻译)

Unit 21Pumps1. IntroductionPump, device used to raise, transfer, or compress liquids and gases. Four' general classes of pumps for liquids are described below t In all of them , steps are taken to prevent cavitation (the formation of a vacuull1), which would reduce the flow and damage the structure of the pump, - pumps used for gases and vapors are usually known as compressors . The study of fluids in motion is called fluid dynamics.1.介绍泵是提出,转移或压缩液体和气体的设备。

下面介绍四种类型的泵。

在所有的这些中,我们一步步采取措施防止气蚀,气蚀将减少流量并且破坏泵的结构。

用来处理气体和蒸汽的泵称为压缩机,研究流体的运动的科学成为流体动力学。

Water Pump, device lor moving water from one location to another, using tubes or other machinery. Water pumps operate under pressures ranging from a fraction of a pound to more than 10,000 pounds per square inch. Everyday examples of water pumps range from small electric pumps that circulate and aerate water in aquariums and fountains to sump pumps that remove 'Water from beneath the foundations of homes.水泵是用管子或其他机械把水从一个地方传到另一个地方。

离心泵在化工生产中的应用

离心泵在化工生产中的应用

摘要离心泵的应用是很广泛的,在国民经济的许多部门要用到它。

它的使用涉及到各个领域,有工业,农业和能源方面,其至在军事方面都用到它的很多原理。

在化工生产的实际工况中,由于工作的环境恶劣,动力较强,它的震动幅度相对也较大,因此可能会出现各种各样的问题和故障,所以我重点写了离心泵的故障和它产生的原因以及一些处理它的方法。

不过之前我先分析了它的基木的知识,首先是它的构造,它的工作原理和在各领域的应用等。

关键词:原理,拆卸,安装,应用,故障,排除目录1离心泵的概论 (1)1.1离心泵的基本构造 (1)1.2离心泵的过流部件 (2)1.3离心泵的工作原理 (3)1.4离心泵的性能曲线 (4)2化工离心泵的应用 (7)2.1 离心泵在给水排水及农业工程中的应用 (8)2.2 离心泵在工业工程的应用 (9)2.3 离心泵在航空航天和航海工程中的应用 (8)2.4离心泵在能源工程中的应用 (10)3离心泵的拆装 (11)3.1 离心泵的结构图 (11)3.2 离心泵一般拆卸步骤 (11)3.3 离心泵的拆卸顺序 (12)3.4 离心泵泵拆卸注意的事项 (12)3.5离心泵的装配 (12)4常见故障原因分析及处理 (13)4. 1 离心泵启动负荷 (13)4.2泵不排液 (13)4.3泵排液后中断 (13)4. 4 流量不足 (13)4.5扬程不够 (14)4. 6 运行中功耗大 (14)4.7泵振动或异常声响 (14)4.8轴承发热 (15)4.9轴封发热 (15)4.10转子窜动大 (15)4. 11 发生水击 (15)4. 12 机械密封的损坏 (18)4.13故障预防措施 (18)小结 (19)参考文献 (20)致谢 (21)空气进入到泵内。

始终保持水泵内的真空!当泵轴与填料摩擦产生热量就要靠水封管住水到水封圈内使填料冷却!保持水泵的正常运行。

所以在水泵的运行巡回检查过程中对填料函的检查是特别要注意!在运行600个小时左右就要对填料进行更换。

离心泵的工作流程

离心泵的工作流程

离心泵的工作流程Centrifugal pumps are widely used in many industrial applications for various fluid transfer and circulation purposes. 离心泵广泛应用于许多工业领域,用于各种流体传输和循环工作。

These pumps work by converting mechanical energy into kinetic energy to increase the velocity of the fluid being pumped. 这些泵通过将机械能转换为动能,从而提高正在抽送的流体的速度。

The basic working principle of a centrifugal pump involves transferring energy from a rotating impeller to the fluid. 离心泵的基本工作原理包括将旋转叶轮的能量传递给流体。

As the impeller rotates, it creates a centrifugal force that pushes the fluid towards the pump outlet. 当叶轮旋转时,会产生一个离心力,将流体推向泵出口。

This force increases the velocity of the fluid, which results in increased pressure within the pump casing. 这种力会增加流体的速度,从而增加泵壳内的压力。

Ultimately, the pressurized fluid is discharged through the outlet of the pump. 最终,加压的流体通过泵的出口排出。

One of the key components of a centrifugal pump is the impeller, which is responsible for transferring energy to the fluid. 离心泵的一个关键组件是叶轮,它负责将能量传递给流体。

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CENTRIFUGAL PUMP INCHEMICALPRODUCTIONAPPLICATIONCentrifugal pump in chemical production, this is most widely used because of its performance wide range (including flow, pressure head of media properties and ShiYing sexual), small volume, simple structure, easy operation, flow uniformity, low malfunction, long service life, CaoZuoFei are lower cost and prominent advantages.(1)centrifugal pump principle of workCentrifugal pump working principle is: centrifugal pump so can turn the water away is because only centrificating. Water pump before work, pump body and feed water full line must be cans in vacuum condition, when the impeller fast turns, leaf prompted water quickly spin, spin in the water under the action of the centrifugal force, pump impeller flew in from the water was thrown in the central part of the impeller, after forming vacuum area. Water in the water atmospheric pressure (or water pressure) under the action of water pipe pressure came through a tube. This cycle unceasingly, can achieve continuous pumped. In the centrifugal pump is worth mentioning: before initiating must to the pump housing filled with water, can start after, otherwise will cause, the vibration of the pump body, thus reduce heat pump, damage to (hereinafter referred to as "cavitation erosion") cause equipment accident!Centrifugal pump is a lot of more phyletic, classification methods common has the following kinds of kind: 1, press the impeller inhaled way points: single suction style centrifugal pump double suction type centrifugal pump. 2, press the impeller number points: single grade centrifugal pump mulfistage centrifugal pump. 3, according to the structure of impeller points: open impeller centrifugal pump impeller half open centrifugal pump closed impeller centrifugal pump. 4, according to work pressure points: low voltage centrifugal pump medium centrifugal pumphigh-pressure centrifugal pump. 5, according to pump shaft position points: horizontal centrifugal pump edge vertical centrifugal pump.(2) basic structure, centrifugal pumpsCentrifugal pump is the basic structure by six parts, it is respectively, pump body, impeller pump shaft, bearing, sealing ring, the stuffing box.1, centrifugal pump impeller is higher than the core part, its great strength, speed and a impeller blades of the main function, impeller before assembly through the static balance experiments. Internal and external surface requirements on the impeller of smooth, to reduce water friction losses.2, the pump body also called pump shell, it is the pump body. Play support fixed effect, and is connected to install bearing bracket.3 and the role of pump shaft couplings and motor was borrowed, will connect to the torque motor impeller, so it is the main component of mechanical transmission.4, bearing is set in the pump shaft support of pump shaft components, a rolling bearing and sliding bearing two kinds. Rolling bearings use butter as lubricant refueling appropriate to general for 2/3 ~ 3/4 volume too much, too little and can calorific a sound and fever! Sliding bearings use transparent oil for lubricant, refuels to oil level line. Too much oil to leak and drift along the pump shaft, too little bearing and melech overheating burnt out cause an accident! The water pump operation process of the highest temperature bearing in general 85 degrees running in about 60 degrees, if gao will find the reasons (whether have impurities, whether black, oily water) and deal with whether!5, sealing ring and say minus leak rings. The import and pump impeller shell of the gap between will cause the water pump high-pressure zone within the clearance flow by low pressure area, the influence of the pump, low efficiency, &safe-durable! Gap with the pump impeller had caused moment shell friction wear. In order to reduce leakage increased reflow resistance, delaying the impeller and pump shell used in the pump housing life, with inner and impeller sealing, department of foreign aid in the gaps remain sealed between 0.25 ~ 1.10 mm advisable.6, stuffing box, mainly by packing rings, packing cone, water storage tube packing gland, composed. The role of the stuffing box is mainly to closed pump shell with the space between the pump shaft, don't let pump of water inside don't flow to the outside to also don't let the outside air into the pump inside. Always keep the vacuum pump inside! When the pump shaft and packing friction heat water controlwater to be about to rely on water circle make packing cooling! Maintain normal operation of pump. So the water pump operation circuit checking process to the stuffing box examination is special attention should be paid to! About 600 hours in operation for packing replacement to.(3) centrifugal pump impeller and other components1. Centrifugal pump impellerCentrifugal pump impeller is the key components.according to the mechanical structure can be divided into closed, semi-enclosed and open 3 kinds. Closed impeller suitable for conveying clean liquid. Semi-enclosed and open impeller suitable for conveying containing solid particles of suspending liquid in the efficiency of, this kind of pump low.Closed and semi-enclosed impeller in operation, leave the impeller's part of high pressure fluid can leak into the impeller and pump shell cavity, between the side because of impeller suction pressure low, liquid at the entrance is liquid in the role of the pressure before and behind impeller to differ, they generate pointing the suction side impeller axial thrust. This force to promote the suction side impeller pump impeller and mobile, cause the contact point of moab shell caused serious damage, the vibration of the pump unit, destroying the normal operation of pump. HouGaiBan in impeller drilled several holes, can reduce the pressure on both sides of the impeller is poor, and decrease the harmful effects of axial thrust, but also reduced the pump efficiency. These holes called balance holes.according to absorb fluid can be divided into different ways of impeller with single suction style double suction type two kinds, single suction style simple structure, liquid only impeller from one side of the inhalation. Double suction style impeller can simultaneously from impeller symmetry to inhaled liquid, it not only hasa greater ability to absorb fluid, and basically eliminate the axial thrust.(3) on the impeller blade according to the geometrical shape, can be bent, radial after blade is divided into three, before and after bending due to bend the kinetic energy transfer liquid leaves, so for static pressure can be used extensively.2. The centrifugal pump impellerIn order to reduce leave the liquid directly into the pump impeller shell caused by impact energy loss in the impeller and pump shell, between sometimes device a fixed blade and contain keep-off device. The blade into the pump impeller shell has gradually turned into the liquid flow, make continuous expansion and partial kinetic energy effectively converted to static pressure can. Multistage centrifugal pump impeller usually are installed.The snail shaped pump, impeller blade and the bent on after all can improve kinetic energy to guide the conversion, and therefore can plenum are regarded as turn can device.3. Shaft sealing deviceBecause of pump shaft rotation and pump shell stationary, and in the axis and the contact point of the pump housing must have certain gap. To avoid pump internal high-pressure liquid leakage along the gap, or prevent outside air from the opposite direction into the pump must set within the shaft seal device. Centrifugal pump shaft sealing device has a filler letter and mechanical (end) seal. Stuffing box is will pump shaft through pump shell ring gap to finish seal, in which loaded soft packing (such as oil or coating graphite baptized of asbestos rope, etc.). Mechanical seal is by an outfit in the acting-ring axis and another fixed in the pump housing formed by static ring. Two rings of end borrow spring force tiejin each other relative rotation, and played the sealing effect. Mechanical seal applies to seal higher occasions, such as the conveying acid, alkali, inflammable, explosive and poisonous liquid.(4)the centrifugal pump introduces below several important performance curve.1, flow - head characteristic curveIt is the basic of centrifugal pump performance curve. Less than 80 than speed centrifugal pump has the characteristics of rise and fall, both sides among (both under convex curved), says hump performance curve. In 80 ~ 150 than speed centrifugal pump has between plain performance curve. More than 150 RPM centrifugal pump performance curves with steep drop. In general, when flow hours, head is high, with the increase of flow is decreasing. Head2, flow - power curveThe shaft power increases with the flow, when flow Q = 0, the corresponding shaft power is not equal to zero, and for certain value (about the normal operation of the 60 percent). The power consumed mainly by the mechanical loss. This is full of water pump, if long time running, will lead to the temperature rising pump, pump shell, bearing can calorific, serious when may make pump body thermal deformation, we called "stuffy head", then head for maximum, when water valve gradually opened, the flow rate will increase, shaft power also slow increase.3, flow - efficiency curveIts curve shape, when flow xiangshan head is equal, efficiency and equal to zero, with the increase of flow, efficiency, but also gradually increase the efficiency increased to a certain value has decreased, after a high efficiency in highest efficiency point near, efficiency is higher, this area is called efficient area.离心泵在化工生产的应用离心泵在化工生产中应用最为广泛,这是由于其具有性能适用范围广(包括流量、压头及对介质性质的失迎性)、体积小、结构简单、操作容易、流量均匀、故障少、寿命长、购置费和操作费均较低等突出优点。

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