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Mechanical Design Essentials\u003C\u002Fstrong>\u003C\u002Fp>\n\u003Cul>\n\u003Cli>Reading a heat exchanger datasheet\u003C\u002Fli>\n\u003Cli>Fluid allocation, velocities, pressure drop and baffle arrangements\u003C\u002Fli>\n\u003Cli>Fouling resistance and design margins: benefits and risks\u003C\u002Fli>\n\u003Cli>Materials selection and corrosion allowance\u003C\u002Fli>\n\u003Cli>Mechanical design under ASME Section VIII and API 660 and API 661 requirements\u003C\u002Fli>\n\u003Cli>Vibration, thermal expansion and design for maintainability\u003C\u002Fli>\n\u003C\u002Ful>\n\u003Cp>\u003Cstrong>Operation and Performance Monitoring\u003C\u002Fstrong>\u003C\u002Fp>\n\u003Cul>\n\u003Cli>Start-up, shutdown and safe operating limits\u003C\u002Fli>\n\u003Cli>Monitoring duty, approach temperatures and pressure drop\u003C\u002Fli>\n\u003Cli>Calculating and trending the overall heat transfer coefficient\u003C\u002Fli>\n\u003Cli>Energy and throughput cost of 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planning and risk-based inspection principles\u003C\u002Fli>\n\u003Cli>Inspection methods: visual, eddy current, IRIS and pressure testing\u003C\u002Fli>\n\u003Cli>Mechanical, hydro-jetting and chemical cleaning methods and their safety\u003C\u002Fli>\n\u003Cli>Bundle pulling, handling, testing and reassembly\u003C\u002Fli>\n\u003Cli>Bolted flange joint assembly and gasket practice under ASME PCC-1\u003C\u002Fli>\n\u003Cli>Plugging, retubing and replacement decisions and life cycle cost\u003C\u002Fli>\n\u003Cli>Action plan: improving exchanger reliability in your plant\u003C\u002Fli>\n\u003C\u002Ful>","\u003Cp>By the end of this programme, participants will be able to:\u003C\u002Fp>\n\u003Cul>\n\u003Cli>Explain the heat transfer principles behind exchanger performance, including LMTD and effectiveness methods\u003C\u002Fli>\n\u003Cli>Select suitable exchanger types for different services and operating conditions\u003C\u002Fli>\n\u003Cli>Read TEMA designations, datasheets and key mechanical design features of shell and tube exchangers\u003C\u002Fli>\n\u003Cli>Calculate duty and overall heat transfer coefficient from plant data and compare them with design\u003C\u002Fli>\n\u003Cli>Monitor performance and estimate the energy and throughput cost of fouling\u003C\u002Fli>\n\u003Cli>Identify common fouling and damage mechanisms and their operating causes\u003C\u002Fli>\n\u003Cli>Choose appropriate cleaning methods and plan cleaning based on performance data\u003C\u002Fli>\n\u003Cli>Define inspection scope and methods for shell and tube, plate and air-cooled exchangers\u003C\u002Fli>\n\u003Cli>Plan safe maintenance activities, including bundle removal, testing and bolted joint assembly\u003C\u002Fli>\n\u003Cli>Decide between plugging, repair, retubing and replacement on technical and economic grounds\u003C\u002Fli>\n\u003C\u002Ful>","\u003Cul>\n\u003Cli>\u003Cstrong>Process engineers:\u003C\u002Fstrong> process, operations and energy engineers responsible for exchanger performance\u003C\u002Fli>\n\u003Cli>\u003Cstrong>Mechanical and maintenance engineers:\u003C\u002Fstrong> static equipment, maintenance and reliability engineers\u003C\u002Fli>\n\u003Cli>\u003Cstrong>Inspection staff:\u003C\u002Fstrong> inspection engineers and technicians responsible for pressure equipment\u003C\u002Fli>\n\u003Cli>\u003Cstrong>Operations supervisors:\u003C\u002Fstrong> shift supervisors and senior operators in process and utility plants\u003C\u002Fli>\n\u003Cli>\u003Cstrong>Technical staff:\u003C\u002Fstrong> planners, technicians and project engineers involved in exchanger specification or turnarounds\u003C\u002Fli>\n\u003C\u002Ful>\n\u003Cp>Participants should have an engineering or technical background and some experience in plant operation or maintenance. The programme is not designed as an exam preparation course for any professional certification.\u003C\u002Fp>","\u003Cul>\n\u003Cli>Heat transfer and exchanger performance fundamentals\u003C\u002Fli>\n\u003Cli>Heat exchanger type selection\u003C\u002Fli>\n\u003Cli>Datasheet and TEMA designation interpretation\u003C\u002Fli>\n\u003Cli>Performance monitoring and fouling cost analysis\u003C\u002Fli>\n\u003Cli>Fouling and damage mechanism identification\u003C\u002Fli>\n\u003Cli>Cleaning method selection and planning\u003C\u002Fli>\n\u003Cli>Heat exchanger inspection planning\u003C\u002Fli>\n\u003Cli>Bundle handling and bolted joint assembly\u003C\u002Fli>\n\u003Cli>Repair and replacement decision-making\u003C\u002Fli>\n\u003C\u002Ful>","\u003Cp>Heat exchanger fouling, leaks and tube failures cost plants energy, throughput and unplanned shutdowns, often because design margins, operating practice and maintenance are not managed together. This programme gives engineers and technicians a practical understanding of how heat exchangers are designed, operated, monitored, inspected and maintained to keep them reliable and efficient.\u003C\u002Fp>","\u003Cp>Heat exchangers are among the most common items of equipment in oil, gas, petrochemical, power, desalination and utility plants, and among the most common causes of lost performance. Units are selected with fouling allowances that hide real problems. Operating conditions drift away from design. Performance is not monitored until throughput falls. Cleaning is scheduled by habit rather than data, and tube failures are repaired without understanding the damage mechanism behind them.\u003C\u002Fp>\n\u003Cp>This programme follows the exchanger through its life cycle. It moves through five stages: thermal fundamentals and exchanger types, the basics of thermal and mechanical design, operation and performance monitoring, fouling and damage mechanisms, and inspection, maintenance and repair.\u003C\u002Fp>\n\u003Cp>\u003Cstrong>Built on recognised practice.\u003C\u002Fstrong> The programme references the TEMA Standards for shell and tube exchangers, API 660 for shell and tube heat exchangers, API 661 for air-cooled heat exchangers, ASME Boiler and Pressure Vessel Code Section VIII Division 1, API 510 for pressure vessel inspection, API RP 571 on damage mechanisms and ASME PCC-1 for bolted flange joint assembly. They are used as working references, not as a substitute for the full documents.\u003C\u002Fp>\n\u003Cp>\u003Cstrong>Decisions this programme improves.\u003C\u002Fstrong> Which exchanger type suits a service; whether a design specification and fouling allowance are sensible; when declining performance justifies cleaning; which cleaning method to use; what inspection scope a turnaround needs; and whether to plug, repair, retube or replace.\u003C\u002Fp>\n\u003Cp>\u003Cstrong>How it is delivered.\u003C\u002Fstrong> Twenty hours across five sessions, built around one running case: a crude preheat train with falling outlet temperature and a history of tube leaks. 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Heat exchanger fouling, leaks and tube failures cost plants energy, throughput and unplanned shutdowns, often…",{"@context":433,"@graph":434},"https:\u002F\u002Fschema.org",[435,463],{"@type":436,"@id":437,"name":286,"description":438,"url":439,"inLanguage":440,"provider":441,"educationalLevel":317,"timeRequired":444,"offers":445,"hasCourseInstance":450},"Course","https:\u002F\u002Feliteacademy.eu\u002Fcourse\u002Fheat-exchangers-design-operation-and-maintenance-in-dubai#course","Heat exchanger fouling, leaks and tube failures cost plants energy, throughput and unplanned shutdowns, often because design margins, operating practice and maintenance are not managed together. This programme gives engineers and technicians a practical understanding of how heat exchangers are designed, operated, monitored, inspected and maintained to keep them reliable and 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