




已阅读5页,还剩201页未读, 继续免费阅读
版权说明:本文档由用户提供并上传,收益归属内容提供方,若内容存在侵权,请进行举报或认领
文档简介
电潜泵知识与控制理论培训,湛江,2,Introduction,xxx,3,电潜泵应用技术的基础知识 电潜泵系统构成, 主要设备的功能和工作原理及其相互间关系 电泵生产过程中需关注的参数, 重点讲解表现其工况特征和必须重点监测的数据 各类与电泵相关的上部完井方式及管串简介 气蚀, 稠油, 出沙等井况对电泵运行的影响及解决方案 其他与电泵运行寿命相关的因素 电泵技术发展和特殊应用 变频控制的基本理论及地面设备的整体构成 变频器主要参数的计算和设置 谐波应对方案和中压变频器简介 GCS/ICS 变频器的专题介绍和初级故障处理 井下实时监控技术的意义及产品介绍,A typical ESP installation,5,ESP System Technology Overview,6,Objective,Upon comletion of this course, you should be able to: Explain the uses for Electrical Submersible Pumps. List the major components of an ESP system. Explain the principle of an ESP system.,7,.,8,ESP Downhole System,The basic ESP downhole system components are .,The Monitoring System (optional),The Power Cable,The Motor,The Seal Section,The Pump,9,Built in Discharge head,Tubing screws in here,Bolts to the Seal,Pump Shaft,Built in Intake,Pump Housing,Rotating Impeller,Stationary Diffuser,The Pump,10,The Pump,Hangs from the production tubing Lifts the fluid through the tubing to the surface Is a multi-stage centrifugal type Is constructed from impellers and diffusers Must be sized to match the well production Has an intake and discharge that either bolts onto or is threaded into the pump housing Normally be set above the perforation for sufficient cooling.,11,LT = Lower Tandem pump ( with built in intake ),The seal bolts on here,12,LT/MT = Lower/Middle Tandem pump,Head,Shipping Cap,If MT (middle tandem) or LT (Lower Tandem) then a flange face is the head of the pump.,13,If Upper Tandem (UT) then a discharge is built into the pump.,UT Pump,Built in Discharge head,14,Middle Tandem pump Base,UT or MT pump,Shipping Cap,15,The Bolt on Head,The Middle Tandem or Lower Tandem Pump Head,16,Gas separator intake (cut away). May be bolted on to the base of a MT (Middle Tandem) or UT (Upper Tandem) Pump,The Seal bolts on here.,UT or MT pump bolts on here.,17,Centrifugal ?,18,Stages stacked on a shaft and compressed in a housing.,Centrilift Submersible Pump,19,Rotating (right to left) impellers,Stationary diffusers,Cutaway of Pump,20,Impeller,21,Pump Stage Hydraulic Design,ESP Stage designs fall into one of two hydraulic design categories ,Mixed Flow - flow path has both axial and radial direction with respect to the pump shaft,Radial Flow - flow path is generally perpendicular (radial) with respect to the pump shaft,22,Impeller Terminology,Impeller Hub,Bottom Shroud,Top Shroud,Impeller Skirt,Impeller Eye,Impeller Vane,Downthrust Washer,Upthrust Washer,23,Impeller,Eye,24,Impeller,The impeller rotates about the pump axis, with the shaft,It provides the centrifugal force to the fluid - gives it energy.,25,Impeller,Fluid enters the impeller through the eye near the shaft and exits the impeller on the outside.,26,Impeller - Cut Away,27,28,Diffuser,29,Diffuser,The diffuser does not rotate, it turns the fluid up into the next impeller,It transforms the fluid velocity, its energy, into head,30,Diffuser - Cut Away,31,Impeller & Diffuser,Diffuser directs fluid into the eye of the impeller,Impeller spins and gives energy to fluid which exits around the outside,Diffuser redirects the fluid up into the next impeller and turns fluid energy into head,32,Impeller in Diffuser - A Pump Stage,33,Pump Stage - cut away,34,Flow, Barrels per day (BPD),Operating Range,Head in Feet,BHP,Pump Curve,80,60,40,20,1,2,3,Efficiency %,Best Efficiency Point (BEP),Total Dynamic Head ( TDH ),36,Flow, Barrels per day (BPD),Operating Range,Head in Feet,BHP,Pump Curve,80,60,40,20,1,2,3,Efficiency %,Best Efficiency Point (BEP),37,Head in Feet,Pump Curve,0,10,20,30,40,50,60,Flow, Barrels per day (BPD),0,200,400,600,800,1000,Developing the Pump Stage - Head / Capacity Curve,38,Pump Stage,Fluid Reservoir,Developing the Pump Stage Head Capacity Curve,39,Fluid Reservoir,Head (Lift),1,Developing the Pump Stage Head Capacity Curve,40,Head in Feet,Single stage performance for a given RPM and fluid viscosity,Pump Stage Characteristics,0,10,20,30,40,50,60,1,Developing the Pump Stage Head Capacity Curve,41,Fluid Reservoir,Head,1,Developing the Pump Stage Head Capacity Curve,42,Head,Flow,1,2,Fluid Reservoir,Developing the Pump Stage Head Capacity Curve,43,Head in Feet,Pump Stage Characteristics,0,10,20,30,40,50,60,1,2,Developing the Pump Stage Head Capacity Curve,44,Head,Flow,1,2,Fluid Reservoir,Developing the Pump Stage Head Capacity Curve,45,Head,Flow,1,2,3,Fluid Reservoir,Developing the Pump Stage Head Capacity Curve,46,Head in Feet,Pump Stage Characteristics,0,10,20,30,40,50,60,Flow, Barrels per day (BPD),0,200,400,600,800,1000,1,2,3,Developing the Pump Stage - Head / Capacity Curve,47,Head in Feet,Pump Curve,0,10,20,30,40,50,60,Flow, Barrels per day (BPD),0,200,400,600,800,1000,Developing the Pump Stage - Head / Capacity Curve,48,Use the pump curve to size a pump,We have a well, we want to produce 600BPD, and we need at least 280ft pump head. How many stages do we need?,49,600 bpd,Fluid Reservoir,Using the Pump Curve to size a pump,50,Head in Feet,Pump Curve,0,10,20,30,40,50,60,Flow, Barrels per day (BPD),0,200,400,600,800,1000,40 feet/stage 600 BPD,56 feet/stage 0 BPD,Using the Pump Curve to size a pump,51,600 bpd,Fluid Reservoir,Using the Pump Curve to size a pump,52,600 bpd,Fluid Reservoir,For 600 BPD Stages = 280/40 = 7,Using the Pump Curve to size a pump,53,600 bpd,Fluid Reservoir,Using the Pump Curve to size a pump,54,600 bpd,Fluid Reservoir,Using the Pump Curve to size a pump,55,Multiple Stages,The head that one stage develops is multiplied by the number of stages to determine the total head a pump will deliver. At a given flow rate !,600 bpd,56,Flow, Barrels per day (BPD),Operating Range,Head in Feet,BHP,Pump Curve,80,60,40,20,1,2,3,Efficiency %,Best Efficiency Point (BEP),57,Pump Performance,Pump stage performance has three measured parameters which are Flow Rate Head (Discharge pressure can be calculated) Brake Horsepower or Motor Load From the above, Pump Efficiency may be calculated,58,Using the pump curve,Example: A well will produce 4000 BPD with a GC3500 pump when the pump produces a TDH (total dynamic head) of 5000 ft. Specific gravity of the produced fluid = 1.00 How many stages we need? How big the motor should be?,59,Pump Curve,GC3500 Single Stage Performance, 3500 RPM SpGr = 1.0, 60 Hertz, 4000 BPD,42 ft/stg,1.8 HP/stg,70% efficient,60,Using the pump curve,So we need a motor bigger than 214HP, say 255HP.,61,Pump Thrust,62,In Floating Impeller Pumps the Impeller does not Float,It is free to move up and down on the pump shaft,Impeller Position,63,Pump Thrust Load,Forces acting on the Impeller,64,Under normal operating conditions, fluid circulates on top and underneath the impeller shrouds,Pump Thrust Load,65,The impeller discharge pressure is on the upper and lower impeller shrouds,Pump Thrust Load,66,The larger cross sectional area on the upper shroud causes the net force to be Down,Pump Thrust Load,This causes the impeller to be moved down,This is a positive downward force termed Downthrust,67,Pump Thrust Load,At some point the volume of fluid going up into the pump will lift the impeller up, overcoming the Downthrust pressure,This causes the impeller to be moved up,68,Pump Thrust Load,The downward force is now reversed (negative), it is termed Upthrust,This causes the impeller to be moved up,At some point the volume of fluid going up into the pump will lift the impeller up, overcoming the Downthrust pressure,69,Pump Thrust Load,This increases the Upthrust,This causes the impeller to be held up,This creates a larger cross sectional area on the bottom shroud which increases the pressure underneath,70,Hydraulic Thrust,Total hydraulic thrust has two components, an up thrust component and a down thrust component The up thrust component is primarily created by the velocity through the impeller or hydraulic impact force The down thrust is primarily created by the pressure generated by the stage These two components combine to make up total hydraulic thrust Fluid viscosity has a dramatic affect on hydraulic thrust,71,Flow from Diffuser,Impeller Flow Path,Fluid velocity & viscous drag forces add to upthrust.,Hydraulic Thrust,Pressure generated by the stage,72,Thrust and Impeller Position,In normal operation the larger cross sectional area on the upper shroud causes more pressure on top, pushing the impeller down,The pump is designed to operate in slight to moderate Downthrust.,73,Washers are fitted to prevent wear:,Downthrust washers,Upthrust washer,Pump Thrust Load,74,Downthrust Washer,75,Hub Washer,Eye Washer,76,Upthrust Washer,77,Impeller - Top,Impeller - Bottom,78,Hub,Upper Shroud,Vane,Lower Shroud,Skirt,Eye,Upthrust Washer,Down thrust Washer,Impeller - Name the parts:,79,Shaft Thrust,Shaft thrust is the result of the pump discharge pressure acting on the cross sectional end of the pump shaft,The two things that determine shaft thrust is the pump discharge pressure (or TDH) and the diameter of the pump shaft. This thrust is transmitted directly to the seal section thrust bearing,80,Variable Speed Operation,ESPs may also be ran at variable speeds. Changing the speed or frequency of an ESP system follows the “Affinity Laws” New Flow Rate = Old Flow (New Hz/Old Hz) New Head = Old Head (New Hz/Old Hz)2 New Brake HP = Old BHP (New Hz/Old Hz)3,81,Flow, Barrels per day (BPD),Operating Range,Head in Feet,BHP,Pump Curve,80,60,40,20,1,2,3,Efficiency %,Best Efficiency Point (BEP),82,GC2200 Single Stage Performance RPM 60Hz = 3500 (Sg = 1),83,GC2200 Single Stage Performance RPM 60Hz = 3500 (Sg = 1),84,Fluid Reservoir,Normal RPM,85,Fluid Reservoir,Fluid Reservoir,Normal RPM,Slower RPM,86,Fluid Reservoir,Fluid Reservoir,Fluid Reservoir,Normal RPM,Slower RPM,Faster RPM,87,88,89,90,Variable Speed Operation,New Flow Rate = Old Flow (New Hz/Old Hz) New Head = Old Head (New Hz/Old Hz)2,“Affinity Laws” ,60Hz Operating Range Min flow = 1500bpd 54ft BEP flow = 2200bpd 46ft Max flow = 3000bpd 25ft,Min flow = 2000bpd 96ft BEP flow = 2933bpd 82ft Max flow = 4000bpd 44ft,80Hz Operating Range,?,91,92,93,Tornado Curve,Min Flow,BEP Flow,Max Flow,94,The Gas Separator,Takes the place of a standard pump intake Is used in applications where free gas causes interference with pump performance Separates a portion of the free gas from the fluid entering the intake to improve pump performance Rotary gas separator types include: Induced Vortex with passive chamber Rotating chamber,95,The Gas Separator,96,The Seal Chamber Section,Is located between the pump and motor Transfers the motor torque to the pump shaft Isolates (seals) the well fluid from the clean motor oil Equalizes the internal unit and wellbore pressure Provides area for motor oil expansion volume Absorbs the pump shaft thrust load The Four “Shuns” - expansion, equalization, isolation, & “absorbsion” aka “Equalizer”, “Protector”, or “Seal Section”,97,Motor,Pump,98,Motor,Pump,99,100,101,Motor,Pump,102,Motor,Seal,Pump,103,Located between the pump and motor Transfers the motor torque to the pump shaft,The Seal Section,104,Labyrinth Chamber,105,Labyrinth Chamber,106,107,Double Labyrinth Chamber,108,109,110,111,Motor,Labyrinth Chamber,112,113,114,Motor,Bag or Bladder,115,Motor,116,117,The Seal Chamber Section,Is located between the pump and motor Transfers the motor torque to the pump shaft Isolates the well fluid from the clean motor oil Provides area for motor oil expansion volume,118,119,Labyrinth Chamber,Motor Oil - Heated,120,Labyrinth Chamber,Motor Oil - Cooling,121,Double Labyrinth Chamber,Motor,122,Bag (or Bladder),Motor,Motor Oil - Heated,123,Bag (or Bladder),Motor,Motor Oil - Heated,124,Bag (or Bladder),Motor,Motor Oil - Heated,125,126,127,Bag (or Bladder),Motor,Motor Oil - Heated,128,Bag (or Bladder),Motor,Motor Oil - Heated,129,Bag (or Bladder),Motor,Motor Oil - Heated,130,Motor,Motor Oil - Cooling,131,Motor,Motor Oil - Cooling,132,Motor,Motor Oil - Heated,Double Bags,133,Motor,Motor Oil - Heated,Double Bags,134,Motor,Motor Oil - Heated,Double Bags,135,136,137,Motor,Motor Oil - Heated,Parallel Bags,138,Motor,Motor Oil - Heated,Parallel Bags,139,The Seal Chamber Section,Is located between the pump and motor Transfers the motor torque to the pump shaft Isolates the well fluid from the clean motor oil Provides area for motor oil expansion volume Equalizes the internal unit and wellbore pressure,140,Motor,141,n thousand feet,142,143,144,145,The Seal Chamber Section,Is located between the pump and motor Transfers the motor torque to the pump shaft Isolates the well fluid from the clean motor oil Equalizes the internal unit and wellbore pressure Provides area for motor oil expansion volume Absorbs the pump shaft thrust load,146,147,148,149,Compression, Fixed Impeller, Pumps,150,Compression, Fixed Impeller, Pumps,151,Motor,Seal,Pump,152,Seal (Lower Chamber),Motor,153,Heat Exchange Area,Thrust Bearing Area,Seal (Lower Chamber),Motor,154,Seal Unit Base,155,Bearing Retainer,156,Oil Pump,157,Bearing,158,Carbon Face,159,Thrust Runner,160,Thrust Runner Carbon Face,Thrust Runner,161,Upthrust Bearing,162,Upthrust Bearing,Bearing Runner,163,164,Bearing Assembly Complete,165,166,The Seal Chamber Section,Is located between the pump and motor Transfers the motor torque to the pump shaft Isolates the well fluid from the clean motor oil Equalizes the internal unit and wellbore pressure Provides area for motor oil expansion volume Absorbs the pump shaft thrust load,167,Seal Section Components - review,Major components are . Mechanical Seals - prevents fluid migration down the seal shaft Bag(s) or Bladder(s) - provides expansion volume and isolation for clean motor oil Labyrinth Chamber(s) - provides expansion and isolation volume in vertical or near vertical wells Thrust Bearing - carries the thrust load of the pump shaft and stages (fixed impeller type only),168,Seal Section Application,Use tandem seals in high pulling cost wells Seals are relatively low cost items as compared w/the total unit cost The more seal sections, the more mechanical seals and therefore, increased shaft isolation Can be designed as a “Thrust on Lower” (TOL) which gives added protection to the unit thrust bearing Use single or multiple bag seals in highly deviated wells The isolation capability of a labyrinth chamber is greatly reduced in deviations beyond 30 - 45 degrees from vertical,169,The Motor,Drives the downhole pump and seal section Is rated for a specific horsepower, voltage, & current Is a two pole, three phase, AC, induction type Rotates at approximately 3500 RPM at 60 Hertz Is constructed of rotors and bearings stacked on the shaft and loaded in a wound stator Contains synthetic oil for lubrication Relies on fluid flow past the housing OD for cooling,170,Motor Components,Stator Laminations,Kapton-Wrapped Magnet Wire,Rotor,Bearing with T-ring,Housing,Epoxy Encapsulation,171,rotor,Bearing with T-Ring,Stator,172,Stator Laminations on a Mandrel,173,Stator Laminations pressed into the motor housing,174,A wound Stator with Leads attached,175,Rotor Copper End Ring,Rotor Laminations,Rotor Bearing,Rotor T ring,Rotor Spacers,176,Rotor Bearing,Rotor,177,Motor Performance,Motors are rated by horsepower, voltage, & current At a constant voltage, by varying the pump load or brake horsepower applied to the motor, current will change At a constant load, by varying voltage, current will vary, as well,178,Motor Application,Motor operating temperature is determined by 5 factors Wellbore Temperature % Load vs. Nameplate Rating Fluid Velocity Past Motor (flow rate vs. unit/casing diameter) Cooling Properties of the Well Fluid (% gas, water cut, scaling tendencies, etc.) Power Quality (3 phase voltage/current imbalance, wave form distortion, full nameplate voltage available, etc.) All of the above factors determine if, and when, a motor will overheat during operation,179,SPH p49,180,Motor and VSD,181,Motor and VSD sizing the motor,Substitute the pump BHPHZ at the maximum design HZ for the NPHPHZ and solve for NPHP60,182,The Power Cable,Is made up of the power cable and motor lead Can be made in round or flat profile Is constructed of three insulated & jacketed copper conductors contained by metal armor Proper applications must address electrical, physical size, and operating temperature requirements,183,Cable Types - Flat,Components 1 - Conductor (Copper) 2 - Insulation (Polypropylene or EPDM) (Ethylene Propylene Diene Monomer) 3 - Jacket (Nitrile or EPDM) & Tape 4 - Armor (Galvanized, Stainless, or Monel) Benefits:
温馨提示
- 1. 本站所有资源如无特殊说明,都需要本地电脑安装OFFICE2007和PDF阅读器。图纸软件为CAD,CAXA,PROE,UG,SolidWorks等.压缩文件请下载最新的WinRAR软件解压。
- 2. 本站的文档不包含任何第三方提供的附件图纸等,如果需要附件,请联系上传者。文件的所有权益归上传用户所有。
- 3. 本站RAR压缩包中若带图纸,网页内容里面会有图纸预览,若没有图纸预览就没有图纸。
- 4. 未经权益所有人同意不得将文件中的内容挪作商业或盈利用途。
- 5. 人人文库网仅提供信息存储空间,仅对用户上传内容的表现方式做保护处理,对用户上传分享的文档内容本身不做任何修改或编辑,并不能对任何下载内容负责。
- 6. 下载文件中如有侵权或不适当内容,请与我们联系,我们立即纠正。
- 7. 本站不保证下载资源的准确性、安全性和完整性, 同时也不承担用户因使用这些下载资源对自己和他人造成任何形式的伤害或损失。
最新文档
- 合成气梭菌发酵乙醇的机制、现状与前景探析
- 合作学习赋能:普通高中英语词汇教学的创新与实践
- 教师招聘之《小学教师招聘》综合提升测试卷带答案详解(培优b卷)
- 2025年教师招聘之《幼儿教师招聘》题库综合试卷附参考答案详解(考试直接用)
- 2025年教师招聘之《幼儿教师招聘》测试卷附参考答案详解【预热题】
- 2025年公务员时事政治试题库附参考答案详解(培优a卷)
- 教师招聘之《小学教师招聘》通关模拟卷附参考答案详解(典型题)
- 教师招聘之《小学教师招聘》考前冲刺练习题库提供答案解析【历年真题】附答案详解
- 2025年教师招聘之《小学教师招聘》考试题库附参考答案详解【考试直接用】
- 2025内蒙古呼伦贝尔东北阜丰生物科技有限公司招聘8人笔试备考及完整答案详解一套
- 二年级语文上册《有趣的动物》课件PPT
- 不干胶贴标机设计学士学位论文
- 《劳动合同书》-河南省人力资源和社会保障厅劳动关系处监制(2016.11.15)
- 钢轨检测报告
- 战略管理:概念与案例
- GB/T 3505-2009产品几何技术规范(GPS)表面结构轮廓法术语、定义及表面结构参数
- GB/T 11186.1-1989涂膜颜色的测量方法第一部分:原理
- 09S304 卫生设备安装图集
- 功能材料概论-课件
- 微纳加工课件
- 危重病人紧急气道管理课件
评论
0/150
提交评论