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Heat Exchanger Fundamentals: Theory and Applications

Heat Exchanger Fundamentals: Theory and Applications banner
Preview this course
Self-paced Beginner

Heat Exchanger Fundamentals: Theory and Applications

4(144)
52 enrolled
1337 views
FREE
259 min
Anytime
Hindi
1337 views
Saurabh Kumar Gupta
Saurabh Kumar GuptaMechanical Engineer
  • Lifetime access
  • Certificate of completion
  • Foundational Learning
  • Access to Study Materials

Why enroll

People enroll in the course “Heat Exchanger Fundamentals: Theory and Applications” to gain a clear understanding of how heat exchangers work and how to design, select, and operate them efficiently in real-world systems. The course helps learners build strong fundamentals in heat transfer principles while also covering practical applications across industries such as power plants, oil & gas, and HVAC. It is especially valuable for engineers and technicians looking to improve system performance, troubleshoot operational issues, and enhance energy efficiency in thermal systems.

What enrolled engineers say

5 verified reviews
  • Feb 25, 2026

    Initially, I wasn’t sure what to expect from this course. Coming from a working HVACR background with some crossover into oil & gas facilities work, the basics of heat transfer weren’t new, but the way shell-and-tube and plate heat exchangers were broken down helped fill a few gaps. Flow arrangements like counterflow vs parallel flow finally clicked in a practical sense, especially when tied to pressure drop and maintenance tradeoffs. One challenge was slowing down and not overthinking the math. At a beginner level, it took a bit to accept the simplified assumptions, since real projects rarely behave that cleanly. That said, the examples were close enough to what shows up in HVAC chiller plants and oil & gas cooling loops to be useful. The section on fouling factors was particularly relevant, since that’s something often underestimated in both refinery exchangers and aerospace ground support equipment. A solid takeaway was learning how to quickly sanity-check exchanger selection before handing it off to a vendor. That alone saves back-and-forth on early design reviews. I can see this being useful in long-term project work.

    Adekunle A. Verified
  • Feb 25, 2026

    Initially, I wasn’t sure what to expect from this course. Coming from a working HVACR background with some exposure to oil & gas facilities, heat exchangers were something used daily but not always fully unpacked. The course helped close that gap, especially around shell-and-tube versus plate heat exchangers and why one makes more sense than the other beyond just “that’s what we’ve always used.” One challenge was wrapping my head around LMTD versus NTU methods. The theory made sense after a few passes, but applying it while also considering pressure drop felt a bit messy at first. That said, the breakdown of parallel flow and counterflow configurations clicked when tied back to real operating constraints, like fouling margins and pump sizing. A practical takeaway was being more deliberate about exchanger selection during early design. On a recent HVAC retrofit, the course helped justify a plate heat exchanger choice by quantifying efficiency gains instead of relying on rules of thumb. It also translated well to oil & gas cooling loops where pressure drop penalties matter. Overall, it felt grounded in real engineering practice.

    Sateesh Kumar Y. Verified
  • Feb 25, 2026

    Initially, I wasn’t sure what to expect from this course, especially since it’s labeled beginner and I’ve already worked around heat exchangers in HVACR and oil & gas projects. The value ended up being in how clearly the fundamentals were tied to real equipment like shell-and-tube units and plate exchangers, not just equations on slides. The sections on counterflow vs parallel flow helped close a gap I’ve had when reviewing vendor datasheets and trying to sanity-check performance claims. One challenge was getting fully comfortable with the LMTD method versus effectiveness-NTU. It took a couple of passes and working through the examples to see when each approach actually makes sense in practice, especially when fouling factors come into play. That part felt realistic, since fouling and pressure drop are constant headaches on operating units. A practical takeaway was being able to do quick back-of-the-envelope sizing to see if a proposed exchanger is even in the right ballpark before sending it out for detailed design. That’s already useful on HVAC retrofit jobs and small oil & gas skids. The content felt aligned with practical engineering demands.

    Irshad S. Verified

Is this course for you?

You should take this if

  • You work in HVAC or Oil & Gas Upstream
  • You're a Mechanical Engineering / Chemical & Process professional
  • You prefer self-paced learning you can revisit

You should skip if

  • You need a different specialisation outside Mechanical Engineering
  • You need live interaction with an instructor

Course details

A heat exchanger is a device designed to efficiently transfer heat energy from one fluid to another, either through direct contact or indirect contact via a separating wall. Heat exchangers are widely used in various industries, including power generation, chemical processing, HVAC, and refrigeration, to recover heat energy, cool or heat fluids, and optimize system performance. There are several types of heat exchangers, including shell-and-tube, plate, finned-tube, and regenerative heat exchangers, each with its own unique design characteristics and applications. Heat exchangers can be designed to operate in various flow configurations, such as parallel flow, counterflow, or crossflow, and can be optimized for specific performance requirements, including heat transfer rate, pressure drop, and fluid flow rates. By selecting and designing the appropriate heat exchanger, engineers can improve the efficiency, reliability, and cost-effectiveness of thermal systems, and reduce energy consumption and emissions. Effective heat exchanger design and operation are critical in many industrial and commercial applications.

Course suitable for

Key topics covered

Introduction Of Heat Exchanger
Overall Heat Transfer Coefficient | Fouling Factor
Logarithmic Mean Temperature Difference For Heat Exchanger
Previous Year Numerical Based On LMTD Method
Multipass And Crossflow Heat Exchanger | Correction Factor
The Effectiveness--The NTU Method
Numerical NTU Method Part-2

Course content

The course is readily available, allowing learners to start and complete it at their own pace.

7 lectures4 hr 19 min
  1. Introduction Of Heat Exchanger
    31 min
  2. Overall Heat Transfer Coefficient | Fouling Factor
    48 min
  3. Logarithmic Mean Temperature Difference For Heat Exchanger
    39 min
  4. Previous Year Numerical Based On LMTD Method
    27 min
  5. Multipass And Crossflow Heat Exchanger | Correction Factor
    30 min
  6. The Effectiveness--The NTU Method
    40 min
  7. Numerical NTU Method Part-2
    44 min

Opportunities that await you!

Career opportunities

Why people choose EveryEng

Industry-aligned courses, expert training, hands-on learning, recognized certifications, and job opportunities-all in a flexible and supportive environment.

What learners say about this course

Avinash
Avinash
Feb 4, 2026

Good

Ra Hul
Ra Hul
May 3, 2026

Hit a few conceptual bottlenecks lately, and this chapter lined up with what I needed. The piston-cylinder boundary work example in Chapter 04, especially the sign convention table when heat/work flip during compression, stuck; I’ve already referenced it in a repo note for an infra PR. Not everything landed; wanted a quicker bridge to open systems or a brief hvacr tie-in, but for a beginner pass it wasn’t fluff. It nudged how I think about scaling load paths in prod arch, RPS included.

Cute Yash
Cute Yash
May 3, 2026

Feels built by someone who’s had to push ideas all the way to prod, not just chalkboard. Chapter 04’s piston–cylinder with a linear spring example stuck; the step where boundary work flips sign after defining the system boundary cleared up a confusion I’ve seen bleed into infra docs and PRs. It’s beginner-friendly without hand-waving, though I wasn’t sold on skipping KE/PE so quickly. good enough that I’ve gone back twice to re-read the cyclic process section.

Arun Kumar
Arun Kumar Engineer
May 3, 2026

Doesn't talk down like you've never touched a terminal—it moves briskly and gets to the equations. Chapter 04's spring‑loaded piston example (Example 4.7) on boundary work and the energy balance clicked, especially the sign convention callout. I wasn't sold on the skim over transient heat; wished there was one more worked problem, even a PR-style checklist, before trusting it in prod calcs. Still, it lingered longer than most beginner material; later hvacr load checks kept echoing.

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Questions and Answers

A: A feels conservative because it respects the construction-to-operation boundary and avoids heating a dirty bundle. B sounds practical on schedule pressure, but heating before cleaning bakes debris onto tube walls and raises under-deposit corrosion risk. C appeals to corrosion engineers, yet hydrotesting after chemical clean reintroduces oxygenated water and debris unless the loop is perfectly controlled. D mirrors what people do when operations is impatient, but full cold flow before leak testing loads tube-to-tubesheet joints without proof of integrity.

A: A aligns with legal enforceability; auditors care what you committed to, not what changed later. B sounds safety-forward, but unilateral adoption without MOC alters scope and liability. C feels pragmatic, yet creates an undefined acceptance basis that fails traceability. D is common in procurement, though vendor stamps don’t override owner specs under COMAH scrutiny.

A: A is the quiet failure mode; PSV sizing protects pressure, not metal temperature. B is intuitive but the valve failed closed, isolating the header. C borrows from pump protection logic, yet check valves and hydraulics limit this case. D drifts into plant-wide scenarios unrelated to the initiating event.

A: A addresses the measurement chain; water tests live or die on ΔT accuracy. B jumps to design assumptions without validating test conditions. C is tempting if you distrust fabrication, but it’s invasive before basics are checked. D risks erosion and doesn’t explain whether the shortfall is real or an artifact.