Entropy In Engineering Thermodynamics by PK NAG (Chapter 07)
- 7-day money-back guarantee
- Lifetime access
- Certificate of completion
Why enroll
What enrolled engineers say
This course turned out to be more technical than I anticipated. Even though it’s tagged beginner, Chapter 07 on entropy goes straight into the why behind losses, which was useful coming from field-heavy work. Concepts like entropy generation and the Clausius inequality helped connect dots I’d previously treated as rules of thumb. On the oil & gas side, the discussion around isentropic processes made more sense of compressor and turbine efficiency calculations used in gas compression trains. In HVACR work, the T–s diagram explanations directly tied into vapor compression refrigeration cycles, especially understanding why real compressors drift from ideal behavior and how that shows up as extra power draw. One challenge was keeping track of reversible vs irreversible processes when solving problems; it’s easy to mix assumptions if you’re used to shortcut methods. Working through the solved examples helped slow that down. A practical takeaway was being able to sanity-check performance data using entropy changes instead of just trusting vendor curves. That filled a gap left by on-the-job learning, where entropy is mentioned but rarely explained. It definitely strengthened my technical clarity.
Coming into this course, I had some prior exposure to the subject from plant calculations, but entropy always felt like something you plug into equations without fully trusting it. Chapter 07 from PK Nag helped clear that up in a very grounded way. The treatment of entropy balance for closed and open systems finally connected with things seen in oil & gas work, especially when looking at gas turbine performance and why real compressors never hit ideal efficiency. One challenge was keeping the sign conventions straight while doing entropy generation calculations, particularly when heat transfer crosses system boundaries at different temperatures. It took a couple of reworks of the examples to stop mixing that up. The T–s diagram discussion also helped bridge that gap, and it directly tied into HVACR topics like vapor compression cycles and throttling losses in expansion valves. A practical takeaway was learning to use entropy generation as a quick check on where irreversibilities are creeping into a system, instead of just blaming “losses.” That’s already useful when reviewing HVAC load calculations and heat exchanger selections. The course filled a knowledge gap between theory and day-to-day engineering decisions. I can see this being useful in long-term project work.
Initially, I wasn’t sure what to expect from this course, especially since entropy always felt like one of those topics that stayed abstract back in college. Chapter 07 actually helped bridge that gap. The way entropy balance was tied to real processes made it easier to relate to day-to-day engineering work. From an oil & gas perspective, the discussion around irreversibility clicked when thinking about compressor inefficiencies and pressure drops across valves. Entropy generation finally felt like a useful diagnostic, not just a formula. On the HVACR side, linking entropy changes to refrigeration cycles and COP helped clarify why certain cycle modifications don’t give the gains people expect in practice. One challenge was keeping track of sign conventions and distinguishing reversible versus irreversible processes, especially when applying the equations to control volumes. That took a couple of re-reads and some side calculations. The practical takeaway was learning to set up a proper entropy balance before jumping into numbers, which is something already being applied while reviewing a heat exchanger issue on a current project. Overall, it felt grounded in real engineering practice.
Your instructor
Saurabh Kumar Gupta
Content Manager
Mechanical Engineer
Is this course for you?
You should take this if
- You work in Oil & Gas Upstream or HVAC
- You're a Chemical & Process / Mechanical Engineering professional
- You prefer self-paced learning you can revisit
You should skip if
- You need a different specialisation outside Chemical & Process
- You need live interaction with an instructor
Course details
Course suitable for
Key topics covered
Course content
The course is readily available, allowing learners to start and complete it at their own pace.
- Two reversible adiabatic curve never intersect5 min
- Clausius Theorem19 min
- Clausius Inequality | Property of Entropy25 min
- Entropy Principle | Entropy Generation57 min
- Application of Entropy Principle | Example PK nag Ex7.7 &7.954 min
- Solved Example PK Nag Book Ex-7.1 to 7.3 & 7.8 | Entropy Principle39 min
- Combined 1st and 2nd Law | Tds =dU+PdV | Tds=dH-vdP20 min
- Temperature Entropy Diagram | T S Diagram26 min
- Entropy Change for an Incompressible & Compressible Substance26 min
- Entropy Change in a Polytropic Process8 min
- Entropy Generation For Open System | Solved Example 7.12 & 7.1321 min
- Third Law Of Thermodynamics4 min
- Pk Nag Problem Chapter-7 Entropy (Page No.-225) | Q-2 to 1652 min
- Pk Nag Problems (Chapter-7 Entropy) Q 17 to Q 2635 min
- Pk Nag Problems | Chapter-7 Entropy | Q 27 to Q 3831 min
Opportunities that await you!
Career opportunities
Course Attachments
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
Nice
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.
Module-to-module flow felt natural, so it's easy to jump in between meetings without losing context. Chapter 04’s boundary work bit stuck, especially the P–V diagram walkthrough to W = ∫PdV and the spring-loaded piston example. wasn't sold on the heat vs work sign table; I wished for one more numeric check tied to the plot. I've already used the framing to trim an overcooked arch note in our repo and tighten a PR comment touching prod infra.
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.