I work in power plant piping. For a long time I could route a main steam line, but I could not fully explain why it was the size it was. The answer was always "process gave us the data." Power Plant Engineering by Black & Veatch is the book that closed that gap for me. This is what it taught me, and why I still recommend it to every piping engineer who joins a power project.
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Quick verdict
- What it is: A thick (about 880 pages) reference on how thermal power plants are designed, written from the experience of engineers at Black & Veatch. Edited by Lawrence F. Drbal, Patricia G. Boston and Kayla L. Westra. Published by Chapman & Hall in 1996.
- What it is best at: The thermodynamics behind the plant. The Rankine cycle, heat balances, turbines, feedwater heaters, condensers and cooling towers.
- Who should read it: Piping engineers, layout designers and stress engineers on power projects who want to understand the process behind the pipe.
- Who it is not for: Someone looking for a piping code book. It does not replace ASME B31.1.
Why a piping engineer should read a power plant book
Piping in a power plant is not like piping in a process plant. A few lines carry almost all the energy of the plant. Main steam, hot reheat, cold reheat and feedwater are the big ones. Their pressures and temperatures are set by the thermodynamic cycle, not by the piping team.
If you don't understand the cycle, you work from numbers you can't question. You size what you're told to size. In a design review, you can't explain why a line is that big, why the material changed, or why a small pressure drop matters so much.
That was me. This book changed it.
Insight 1: The Rankine cycle finally made sense
I had studied the Rankine cycle in college. I could draw the T-s diagram. But I never linked it to the pipes I was drawing at work.
The book explains the cycle the way a plant designer uses it. Water is pumped to high pressure. The boiler turns it into superheated steam. The steam expands through the turbine. The condenser turns it back into water. Then it all repeats.
Once I saw it that way, each part of the cycle became a pipe I already knew:
| Part of the Rankine cycle | The piping system |
|---|---|
| Boiler outlet to turbine inlet | Main steam |
| HP turbine exhaust back to the boiler | Cold reheat |
| Reheater outlet to IP turbine | Hot reheat |
| Turbine extractions to heaters | Extraction steam |
| Condenser to deaerator | Condensate |
| Boiler feed pump to the boiler | Feedwater |
This table looks simple. For me it was the moment the whole plant connected. Every system I worked on now had a place in one loop.
Insight 2: Main steam pipe size comes from the cycle
This is the part that helped my career the most.
The book's chapters on thermal heat balances show where the numbers come from. The heat balance diagram gives you, at every point in the cycle, the mass flow, pressure, temperature and enthalpy. Those four numbers are the inputs to main steam pipe sizing.
Here is the logic I now follow, and the way I explain it to juniors:
- Take the flow, pressure and temperature from the heat balance. Use the case that gives the worst result for the line, which is usually the maximum flow case.
- Find the specific volume of the steam. Use steam tables at that pressure and temperature. High-pressure steam is dense. Low-pressure steam takes up a lot more room.
- Work out the volume flow. Volume flow = mass flow × specific volume.
- Choose a velocity. Your project's design criteria set the allowed steam velocity. It balances pressure drop, noise, erosion and cost.
- Get the inside diameter. Area = volume flow ÷ velocity. Then the diameter follows from the area.
- Check the pressure drop. The turbine is designed for a set inlet pressure. Every bar you lose in the main steam line is energy the turbine can't use.
- Calculate the wall thickness to ASME B31.1. Use the design pressure, the design temperature and the allowable stress of the material at that temperature.
A simple worked example
These numbers are only an example. They are not from a real project.
- Main steam flow: 100 kg/s
- Pressure: 160 bar
- Temperature: 540 °C
- Specific volume from steam tables: about 0.0204 m³/kg
Volume flow = 100 × 0.0204 = 2.04 m³/s
At a velocity of 50 m/s, the area needed is 2.04 ÷ 50 = 0.0408 m².
Inside diameter = √(4 × 0.0408 ÷ π) ≈ 0.228 m, or about 228 mm.
Now picture the same flow as low-pressure steam. The specific volume goes up many times, and so does the pipe. That's why cold reheat lines are so much bigger than main steam lines, even though they carry a similar flow. I knew that fact before. After this book, I understood why.
Why temperature changes everything
The steam temperature doesn't just change the specific volume. It sets the material. At main steam temperatures, carbon steel loses its strength. Plants move to creep-strength alloy steels such as P91 or P22. A higher temperature means a lower allowable stress, a thicker wall and much more costly pipe.
So when the cycle designer raises the steam temperature to improve efficiency, the piping engineer pays for it in wall thickness, weight, supports and welding. The book helped me see both sides of that trade-off.
Insight 3: Pressure drop is money
The book also covers engineering economics. That changed how I look at line sizing.
A bigger main steam pipe has less pressure drop. Less pressure drop means the turbine gets more of the boiler's energy. Over 25 or 30 years of running, that adds up to real fuel savings.
A bigger pipe also costs more. More material, heavier supports, bigger hangers, more welding. Thicker walls also make thermal stress harder to handle.
So the "right" size is an economic choice, not just a velocity check. Once I understood that, my design reviews changed. I stopped saying "the velocity is within limits." I started saying "this size is the best balance of pressure drop and cost for this plant."
Insight 4: Seeing the whole plant, not just my lines
The book covers the big equipment that piping connects to: turbine-generators, feedwater heaters, condensers and cooling towers. It explains what each one needs from the piping:
- Turbine: Low nozzle loads and clean, dry steam. That shapes your drains, your warm-up lines and your stress analysis.
- Feedwater heaters: They are fed by extraction steam. They must be protected from water flowing back into the turbine.
- Condenser: It runs under vacuum. Large low-pressure lines and expansion joints come with that.
- Cooling towers: They bring large-bore cooling water piping, often buried.
Before reading it, I treated each piping system as a separate job. After it, I understood how they depend on each other. That made me better at layout and better at talking to process and mechanical engineers.
How it helped me in interviews
Power plant piping interviews don't stay on drawings for long. In my interviews, the questions kept going back to the cycle:
- Why is the cold reheat line bigger than main steam?
- How do you size a main steam line?
- Why is P91 used for main steam and hot reheat?
- What does the heat balance diagram tell a piping engineer?
- Why do we need drains on steam lines, and where do they go?
- Why does pressure drop in main steam matter?
Because of this book, I could answer these from first principles, not from memory. I didn't just give the answer. I could explain the reason. That's what senior interviewers look for, and I believe it helped me move up in my power plant piping career.
What the book does not do
It's an honest recommendation, so here are its limits:
- It isn't a code book. For wall thickness, materials and testing you still need ASME B31.1, the power piping code.
- It isn't new. It came out in 1996. The thermodynamics hasn't changed, but newer topics such as ultra-supercritical plants and modern emissions controls aren't covered in depth.
- It's heavy. About 880 pages. Don't read it cover to cover at once. Read the cycle and heat balance parts first, then the equipment chapters for the systems you're working on.
How I suggest reading it
- Start with the cycle and heat balance chapters. That's the base for everything else.
- Get a real heat balance diagram from your project. Trace main steam, reheat and feedwater on it while you read.
- Do the pipe sizing yourself. Take one line, use steam tables, and work out the diameter. Compare it with what's on your drawings.
- Read the equipment chapters one by one, as you work on lines connected to that equipment.
- Keep ASME B31.1 next to it for the code side.
Who should buy it
- Piping engineers and designers who are new to power plants.
- Stress engineers who want to understand where the design conditions come from.
- Engineers moving from oil and gas into power.
- Anyone getting ready for a power plant piping interview.
If you work on process plants only, a guide to ASME B31.3 will help you more than this book.
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FAQ
Is Power Plant Engineering by Black & Veatch good for piping engineers? Yes. It isn't a piping book, but it explains the Rankine cycle, heat balances and plant equipment that set the design conditions for every major power plant pipe.
Which book is best for power plant piping? Use two books together. Read Power Plant Engineering by Black & Veatch for the process and thermodynamics, and a guide to ASME B31.1 for the code.
How is main steam pipe size selected? Take the flow, pressure and temperature from the heat balance. Find the specific volume from steam tables. Choose a velocity from your design criteria, work out the inside diameter, check the pressure drop, then calculate the wall thickness to ASME B31.1.
Why is the cold reheat pipe bigger than the main steam pipe? Cold reheat steam is at a much lower pressure, so its specific volume is much higher. The same mass of steam takes up far more space, so it needs a bigger pipe.
Is the 1996 edition still useful? Yes, for the basics. The thermodynamics of the Rankine cycle hasn't changed. Check current codes and standards for design values.
Try it yourself
Once you've worked through a sizing example, check your numbers with the Pipingmind calculators. If you want to see how a main steam isometric looks in 3D, open one in the free Pipingmind IDF Viewer.