Construction Engineering Verified Calculator

Refrigerant Charge Calculator

Refrigerant charge mass against circuit volume, with superheat and subcooling checked against the bands you supply to flag a floodback or flashing condition.

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Geometry-based calculation.Charge mass from a volume and density balance, with superheat and subcooling checked against the bands YOU supply. Refrigerant properties are entered, never looked up.

Superheat and subcooling against their target bands The vapour temperature measured at the evaporator outlet against the saturation temperature, and the condensing temperature against the liquid temperature measured at the condenser outlet, each drawn on one shared kelvin scale with the target band shown as a window. 0 K max K SUPERHEAT T_suction − T_evap — SUBCOOLING T_cond − T_liquid — CHARGE — —
  • Vapour / liquid state
  • Inside the target band
  • Outside the target band
  • Target band window
The vapour temperature measured at the evaporator outlet against the saturation temperature, and the condensing temperature against the liquid temperature measured at the condenser outlet, each drawn on one shared kelvin scale with the target band shown as a window. Schematic only — not to scale. Bar length is a temperature interval in kelvin on one shared scale for both. This is not a pressure-temperature chart; saturation temperatures are your inputs. Refrigerant density, saturation temperatures and target bands are all entered by you. This drawing shows interval comparisons, not refrigerant properties.

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What this calculator does

A circuit is commissioned with a charge weighed in, and then nobody checks whether that charge is actually right. Three things have to agree: the MASS in the circuit, the state at the evaporator, and the state at the condenser. A charge can be correct and the circuit still be damaging itself — a low superheat is a flooded compressor whatever the weigh-in said.

How to use it

  1. Enter the total internal circuit volume — every line, both heat exchangers and the receiver — and the refrigerant density at the charge condition.
  2. Enter the evaporating and condensing temperatures from your own pressure-temperature chart, and the suction and liquid line temperatures measured at the heat exchangers.
  3. Enter the charge you actually weighed in, and the superheat/subcooling bands you are targeting. Those bands differ between manufacturers and this tool has no default.
  4. Read the worst issue, not just the numbers. A floodback condition outranks a charge error every time, because it is the one that destroys the compressor.

Governing formula

Governing Formula
m = V · ρ → ΔT_evap = T_suction − T_sat(evap) → ΔT_cond = T_sat(cond) − T_liquid

Where:

  • V = Total circuit volume [m³]
  • ρ = Refrigerant density [kg/m³]
  • T_sat = Saturation temperature from your P–T chart [°C]

Derived Equations:

Charge error as a fraction: error = (m_actual − m_required) / m_required

Worked example — 0.05 m³ circuit at 900 kg/m³, 8 K superheat, 8 K subcooling

The figures below were produced by running this page's own engine with the example inputs (Total circuit volume (m³), Refrigerant density at charge condition (kg/m³), Evaporating (saturation) temperature (°C), Suction temperature at evaporator outlet (°C), Condensing (saturation) temperature (°C), Liquid temperature at condenser outlet (°C), Charge weighed in (kg), Target superheat — minimum (K), Target superheat — maximum (K), Target subcooling — minimum (K), Target subcooling — maximum (K)). If the calculator returns something different for the same numbers, that is a bug, not a rounding difference.

Expected results for the worked example
Charge the volume holds45 kg
Charge error0 %
Chargeok
Superheat8 K
Superheat checkok
Subcooling8 K
Subcooling checkok
Charge difference0 kg
Circuit commissioned correctly—
Most serious problem
What this meansThe charge is within 5 % of the volume, superheat is 8.0 K and subcooling is 8.0 K, all inside the target band. This circuit is commissioned correctly. Re-check after a warm day, because a charge that is right on a cool morning can be under-charged by the time the plant is fully loaded.
  1. The circuit holds 0.05 × 900 = 45 kg, and 45 kg was weighed in, so the charge is right on.
  2. Superheat is −2 − (−10) = 8 K, inside the 5–12 K band.
  3. Subcooling is 40 − 32 = 8 K, inside the 3–10 K band. All three checks pass.

Assumptions & limitations

Engineering calculation. Charge mass from a volume and density balance, with superheat and subcooling checked against the bands YOU supply. Refrigerant properties are entered, never looked up.

  • Refrigerant density, saturation temperatures and target superheat/subcooling bands are all USER inputs. This tool holds no refrigerant property table, no pressure-temperature chart and no manufacturer data, and looks nothing up.
  • The required charge is V × ρ, which is only a mass balance. It does not account for the fact that the liquid and suction lines hold vapour and liquid respectively, so it ignores the charge split between the two sides of the circuit.
  • Superheat and subcooling must be measured AT the evaporator outlet and condenser outlet. Readings taken elsewhere, or taken while the circuit is cycling rather than at steady load, do not mean what they appear to.
  • Liquid floodback and flash gas in the liquid line can also come from a failed expansion valve, a mis-sized line, an incorrect accumulator charge or a flooded suction line. A charge correction will not fix any of those.
  • No code or manufacturer acceptance check is applied. The target bands are the ones YOU supplied.

This tool supports professional engineering work; it does not replace a sealed design. Confirm every result against the applicable standard and a licensed engineer before it is built.

References & standards

  • ASHRAE Handbook — Fundamentals, refrigeration and thermophysical properties of refrigerants.
  • BS EN 378 — refrigeration systems and safety requirements.
Engineering Disclaimer & Verification Notice

This calculator provides preliminary engineering estimates for informational and planning purposes. Actual reverse osmosis / engineering system performance depends on site conditions, feed-water chemistry, membrane characteristics, operating pressure, temperature, recovery limits, fouling/scaling potential, and system design. Verify results using project-specific data, manufacturer projections, and applicable engineering standards before final design or operation.