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Process Chillers by the Numbers
Sizing, reading and running a process-water chiller from real refrigerant data: load, state points, flash gas, compressor, lift, cost and fault-finding
Size, check and run a process-water chiller with numbers: cooling load, the cycle from NIST R-134a data, saturation, flash gas, compressor work, temperature lift, cost and faults.
Start readingAbout this book
A process chiller is the refrigeration plant most factories own: a packaged machine that cools water for moulds, machine tools, hydraulic systems, lasers, welders, plating baths and food processes, and sends it round the plant in a closed loop. It is usually bought on a single number, its rated capacity, and then run for fifteen years by people who are rarely told what its gauges mean. Yet its performance, its running cost and most of its faults can be read from a handful of measurements, if they are interpreted with the right refrigerant data.
This book works through one process chiller with numbers. It sets out what the chiller is asked to do and the second law’s limit on it, calculates the cooling load, works the vapour-compression cycle point by point from NIST’s refrigerant data, and then looks in turn at saturation pressure and temperature, throttling and flash gas, compressor work and discharge temperature, the effect of temperature lift, running cost, and commissioning and fault-finding. Each chapter follows one running case, includes a plausible mistake and how it was found, and ends with an exercise and its worked answer.
It is written as a companion to the Library’s Heat Pumps and Refrigeration by the Numbers, which sets out the second law, the cycle, heat pump water heating, cold rooms and refrigerant rules for a food factory. This book does not repeat that ground. It goes deeper into one kind of machine, calculating its state points from published property data and showing how to read and diagnose it in service. It assumes school algebra and physics; the Library’s Heat Transfer by the Numbers covers the heat flows that evaporators and condensers rely on.
The running case
Every chapter follows one fictional machine. This is an illustration. A plastics moulder cools its injection-mould circuits with a process-water chiller, called CH-30 here, rated at 30 kW of cooling. Water leaves the chiller at 12 °C and returns from the moulds at 17 °C, a flow of about 1.43 kg/s. The chiller uses R-134a in a single vapour-compression circuit with an air-cooled condenser, sized to work in ambient air up to 35 °C. At its design point it evaporates at 2 °C with 5 K of superheat at the compressor’s inlet, condenses at 45 °C with 5 K of subcooling, and its compressor has an isentropic efficiency of 0.70.
All refrigerant properties are NIST’s, in the ASHRAE reference state. The moulder, the chiller’s ratings, its prices and its problems are invented. None describes KEVOS® work or a real business.
How to use the book
Read Chapters 1 to 3 first: they set out the job, the load and the cycle that every later chapter uses. Chapters 4 to 6 look inside the cycle, Chapter 7 at what changes its performance, Chapter 8 at what it costs to run, and Chapter 9 at commissioning a chiller and finding its faults. Every calculation was checked by running it, and values are given to more figures than a shop needs so that the arithmetic can be followed.
Source limits and professional responsibility
The thermodynamics in this book is standard, and the refrigerant data are NIST’s. The chiller’s efficiencies, operating hours, tariffs and prices are illustrations. Refrigerating systems contain gases under pressure, and in Australia the people who handle refrigerants must be licensed. Chillers are designed, installed and serviced by qualified, licensed people to the applicable standards and regulations, and qualified review governs real work. This book teaches how process chillers behave and how to check them. It is not a design for any system.
Who this book is for
Production, process and maintenance engineers, technicians, facilities managers and buyers who specify, commission, run or troubleshoot process-water chillers in factories.
What you will learn
- Measure or estimate a process cooling load and turn it into a water flow and a chiller rating.
- Work a chiller's cycle point by point from real refrigerant data and check its energy balance.
- Read evaporating and condensing temperatures, superheat and subcooling from gauges and thermometers.
- Show how flash gas, compressor efficiency and temperature lift drive capacity, power and cost.
- Commission a chiller against its rating and diagnose common faults from their numerical signatures.
Inside this book
Chapters
- 01The process chiller and its limitWhat a process chiller is and how its water circuit works, how it is rated, the second law's limit on CH-30, where the shortfall goes, COP, EER and tons, and a quoted figure that broke the second law.
- 02The cooling loadCooling load from flow and temperature difference with NIST water data, where CH-30's 30 kW comes from, measuring a load and its uncertainty, peaks and part load, and a chiller sized from nameplates.
- 03The vapour-compression cycle, point by pointThe four components and four states of CH-30's R-134a cycle from NIST data, refrigerant flow, compressor power, condenser heat and COP, the pressure–enthalpy diagram, and two reference states mixed.
- 04Saturation pressure and temperatureWhy boiling point follows pressure, the Clapeyron equation checked against NIST R-134a data, reading gauges, superheat and subcooling, and air in a condenser.
- 05Throttling and flash gasWhy an expansion valve keeps enthalpy constant, the Joule–Thomson effect, CH-30's 27% flash gas, what subcooling is worth, and a blocked filter-drier.
- 06Compressor work and discharge temperatureIdeal and real compression from NIST data, isentropic efficiency, why R-134a heats less than air, motor losses, discharge temperature, and a starved evaporator.
- 07Temperature lift and approachHow evaporating and condensing temperatures drive capacity, power and COP, approach temperatures, setpoints and head pressure, and a dirty condenser coil.
- 08Running cost and heat recoveryCH-30's electricity and annual cost with GST stated, what improvements are worth, whole-life cost, recovering condenser heat at the right temperature, and heat promised that was not there.
- 09Commissioning and fault-findingProving a chiller against its rating, the water-side capacity test and refrigerant-side checks, a log sheet, CH-30's fault signatures in numbers, and a cool-day test that passed a short chiller.
Apply This in Practice
Use these KEVOS® tools to try the method from this reading with your own numbers.
Explained in this book
Heat Pump and Chiller COP Check (Carnot Limit, Second-Law Efficiency, Running Cost)
Uses the approach temperatures this chapter explains to set the evaporating and condensing temperatures behind a chiller’s Carnot COP.
Used in Temperature lift and approach
Explained in this book
Vapour Pressure and Boiling Check (Clausius–Clapeyron, Boiling Point at Pressure, Margin)
Applies the Clausius–Clapeyron form this chapter compares with refrigerant data; the chapter shows why it can miss by over 10 % for refrigerants.
Applies this method
Air Compressor Power
Works out ideal-gas compressor power for air.
Applies this method
Gas Compression and Expansion Process
Works the ideal-gas compression process for air.
Applies this method
Heat Engine and Heat Pump Second-Law Check (Carnot Limit, Entropy Generated, Lost Work)
Compares a chiller’s COP with the Carnot limit for its water and air or refrigerant temperatures, and flags a quoted figure that breaks it.
Applies this method
Heat Pump, Chiller or Heat Engine Claim Check (Carnot Limit, Second-Law Efficiency, Running Cost)
Tests a chiller’s quoted COP against the second law’s limit between its water and air (or refrigerant) temperatures, as this chapter does for CH-30.
Applies this method
Vapour-Compression Refrigeration or Heat Pump Cycle Check (COP from State Enthalpies, Carnot Limit)
Works the cycle from the four enthalpies: refrigerant flow, compressor power, condenser heat and COP, against the Carnot limit.
Used in The vapour-compression cycle, point by point, Compressor work and discharge temperature
Related Tools and Examples
Useful alongside
Boiling Point and Vapour Pressure at Operating Pressure (Clausius–Clapeyron Check)
Estimates boiling point from pressure with the simple Clausius–Clapeyron form; this chapter shows why refrigerants need the full Clapeyron equation or NIST data instead.
Related to Saturation pressure and temperature
Useful alongside
Least Work to Chill a Product Below Ambient (Second-Law Minimum Power, Ideal COP, Chiller Claim Check)
Finds the least power to chill a water or product stream through its whole temperature range and checks a chiller’s power against it.
Related to The process chiller and its limit
References and source notes
The manuscript and worked examples are original KEVOS® writing. References inform particular concepts; their authors do not endorse this book. Web references were consulted on 27 October 2026.
- F. Reif, McGraw-Hill. Fundamentals of Statistical and Thermal Physics (1965). Supplied source, in copyright. Read as a subject map for the second law, refrigerators, throttling and the Joule–Thomson process, and equilibrium between phases with the Clausius–Clapeyron equation. No text, derivations as set out, figures, tables or problems are reproduced; the treatment, case, numbers and exercises in this book are its own.
- E. W. Lemmon, M. O. McLinden and D. G. Friend, National Institute of Standards and Technology. Thermophysical Properties of Fluid Systems, NIST Chemistry WebBook, SRD 69 (2026). Source of every refrigerant property in the book: R-134a saturation and superheated vapour data in the ASHRAE reference state (enthalpy and entropy zero for saturated liquid at −40 °C), and water's enthalpy for the cooling load. Values retrieved on the date checked.
- Australian Refrigeration Council. ARCtick: Australian Refrigeration Council (2026). The body that administers refrigerant handling licences and refrigerant trading authorisations on behalf of the Australian Government. Referred to in Chapter 9 for who may work on a chiller's refrigerant circuit.
- Standards Australia and Standards New Zealand. AS/NZS 5149 Refrigerating systems and heat pumps: safety and environmental requirements (edition as called up). Named by number and scope as the standard for the safety of refrigerating systems. No values are quoted from it.