2026-10-26
Almost every chiller sizing problem we are asked to solve on site has the same root cause: the cooling capacity was taken from a catalogue headline instead of being calculated for the real duty. A chiller that is 30% oversized will short-cycle, control humidity poorly and waste energy for a decade. A chiller that is 10% undersized will never hold set point on the hottest week of the year — exactly when the process cannot stop.
This guide walks through the two things that actually determine the right machine: the heat load you have to remove, and the working conditions under which the machine has to remove it. Both are engineering inputs. Neither should be a guess.
Answer: Cooling capacity is the rate at which a chiller removes heat from the chilled water circuit, expressed in kW, tons of refrigeration (TR), BTU/h or kcal/h. It is a rate, not a quantity — running a 100 kW chiller for two hours removes 200 kWh of heat energy. Because it is a rate measured at defined conditions, a capacity figure without its test conditions is incomplete information.
Answer: No, but the conversion is fixed. One US refrigeration ton equals 3.517 kW, and one kW equals 3,412 BTU/h or 860 kcal/h. When a Chinese or European supplier quotes kW and a US buyer quotes tons, most sizing errors come from mixing metric refrigeration tons (3.86 kW) with US tons (3.517 kW). Confirm the unit system before comparing offers.
| Capacity unit | Equivalent in kW | Equivalent in TR (US) | Equivalent in BTU/h |
|---|---|---|---|
| 1 kW | 1 | 0.284 | 3,412 |
| 1 TR (US) | 3.517 | 1 | 12,000 |
| 1 TR (metric) | 3.861 | 1.098 | 13,175 |
| 1,000 kcal/h | 1.163 | 0.331 | 3,968 |
Cooling capacity must always be equal to or greater than the total heat load, plus a design margin. A complete load for an industrial installation is normally built from six paths. Leaving one out is the most common reason a system ends up short.
| Heat path | What it covers | Typical calculation approach |
|---|---|---|
| Transmission load | Heat entering through walls, roof, glazing | Q = U × A × ΔT |
| Product load | Heat released by goods being cooled | Q = m × cp × ΔT (sensible) + latent heat of phase change |
| Process / equipment load | Moulds, hydraulics, lasers, welders, dryers, pumps | Measured electrical draw × heat rejection factor into the circuit |
| Infiltration load | Warm humid air entering through doors, openings, make-up air | Q = ρ × V̇ × Δh (ρ ≈ 1.2 kg/m³) |
| People load | Occupants | 75–130 W per person depending on activity and room temperature |
| Lighting and small equipment | Luminaires, computers, instruments | Installed watts × usage factor (LED benches: 5–10 W/m²) |
For comfort/room systems, transmission and infiltration usually dominate. For process cooling, product and equipment load dominate — and they are the paths most often underestimated because they are quoted as averages rather than peaks.
Answer: In process cooling it is almost always the equipment or product path, not the building envelope. In a mould-cooling application the mould itself can account for 60–80% of the total load. This is why copying a "W/m²" rule of thumb from a comfort-cooling table will size an industrial chiller badly.
Answer: Only as a first sanity check, never for final selection. Rough planning values of 100–150 W/m² work for light commercial spaces, but a workshop with injection moulding machines or a laser cell can exceed 400 W/m². Use the area figure to detect an obviously wrong answer, then calculate the six paths properly.
Take a 400 m² moulding workshop in southern China with 8 injection moulding machines, 20 operators and 300 kg/h of PET parts. Design ambient 35°C, room target 26°C.
Subtotal: 83.7 kW. With a 10–15% design margin: 92–96 kW, or roughly 27 TR at the design condition. Note the direction of the calculation: the margin is added to a calculated duty, not used as a substitute for one.
Answer: 10–15% is normal practice for a well-defined duty, and up to 20% where batch processes create unknown peaks. Beyond that, the margin starts creating new problems: short cycling, unstable evaporator control, poor dehumidification and higher specific power. If a duty is genuinely uncertain, select two smaller modular units instead of one large over-margined unit.
Answer: Use Q (kW) = flow (m³/h) × 1.163 × ΔT (K). A 96 kW chiller with a 5 K chilled water rise therefore needs about 16.5 m³/h. Always check the resulting flow and pressure drop against the evaporator datasheet — capacity that cannot be delivered at your available flow is capacity you do not have.
Two chillers with identical compressors can be rated 20% apart because they are rated at different conditions. The nameplate figure is normally quoted at a standard rating point such as AHRI 550/590: 6.7°C leaving chilled water and 29.4°C entering condenser water, or 35°C ambient air for air-cooled units. Your site is rarely at that point.
| Working condition factor | Direction of effect | Typical magnitude |
|---|---|---|
| Higher ambient temperature (air-cooled) | Capacity falls, power rises | −5 to −8% per +5°C above rating |
| Higher condenser water temperature | Capacity falls, power rises | −2 to −3% per +1°C |
| Lower leaving chilled water temperature | Capacity falls | −2 to −3% per −1°C |
| Glycol in the circuit | Capacity falls, flow rises | −5 to −8% at 20% ethylene glycol, −10 to −15% at 30% |
| Altitude (air-cooled) | Capacity falls with air density | −2 to −3% per 300 m above sea level |
| Condenser fouling | Capacity falls | −2 to −3% at 0.0001 m²·K/W fouling factor |
| Part-load operation | Capacity available, efficiency varies | Check IPLV / part-load curve, not just full load |
Answer: Because an air-cooled condenser rejects heat to ambient air, and its capacity is proportional to the condensing temperature it can achieve. When ambient rises from a 35°C rating point to 43°C on a rooftop in August, the condenser cannot reject the same heat and the compressor is pushed toward its high-pressure limit. The machine is not faulty; its rating conditions no longer match the site.
Answer: Yes, in two ways. Glycol has lower specific heat and higher viscosity than water, so the same volumetric flow carries less heat and the pump must work harder. A 30% ethylene glycol mix typically costs 10–15% of capacity plus additional pump head. Specify the minimum freeze protection you actually need, and ask for capacity data at your real glycol concentration.
Correction factors multiply. Take an air-cooled chiller quoted at 100 kW at 35°C ambient and 7°C leaving water, to be installed at 43°C ambient with 5°C leaving water:
100 kW × 0.88 (ambient correction) × 0.94 (chilled water correction) ≈ 82.7 kW of usable capacity. If the calculated load is 96 kW, this unit is short by roughly 14% — a gap that will only appear in the hottest month of the year. Correcting to site conditions before ordering is far cheaper than correcting after commissioning.
Answer: It is the fixed set of temperatures at which a manufacturer's published capacity is valid, defined by standards such as AHRI 550/590. Without it, two quotations cannot be compared. When you compare offers, compare the correction factors and the required compressor power at your conditions — not the headline kW.
Answer: Every 1°C rise in condensing temperature typically costs about 2–3% in compressor power for the same delivered cooling. That is why a chiller selected with 15% spare capacity but a marginal condenser can consume more electricity over a year than a correctly sized unit with a generously sized condenser. Capacity and efficiency must be evaluated together.
Reliable sizing ends with verification. Five questions will separate a solid offer from a spreadsheet with a number typed into it:
Answer: Ask for the datasheet at your conditions, the standard it was rated to, and a factory acceptance test with logged water temperatures, flow and power draw. A supplier who can produce a test report at your duty is telling you something a brochure cannot. It is also reasonable to ask what the correction factors are — a supplier who cannot explain them is probably quoting a nominal figure.
Answer: Size the installed capacity for peak load, then check how the machine behaves at average load. Most industrial chillers run below 60% load for the majority of the year, so a unit selected only on peak capacity with no part-load data may deliver poor efficiency in normal operation. Where load swings widely, modular units or a VFD screw chiller usually outperform one large fixed-speed machine.
Cooling capacity selection is a two-step discipline. First, build the heat load from all six paths and add a realistic 10–15% design margin. Second, correct the manufacturer's nominal capacity for the working conditions your site will actually experience. Skip either step and the chiller will either short-cycle its way through a decade of wasted energy, or fail in the week you need it most.
If you would like a second opinion on a duty, our engineering team at Shenzhen Anges Machinery has been building industrial chillers since 2004 and exports more than 80% of its output. Send us your heat load, ambient conditions and water temperature requirements, and we will return a capacity calculation with the correction factors shown — not just a model number.
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