Convert common HVAC engineering units.
R744 / CO₂ Transcritical Cycle Analysis
Evaluate a four-state, single-stage transcritical CO₂ refrigeration cycle from explicit engineering inputs. Unlike the saturation P–T lookup, this workflow uses a frozen high-pressure property grid for supercritical gas-cooler and compressor states.
Free calculator — authorized account required
Create or sign in to your free professional account. Calculator access is activated only after the applicable Leal approval policy is satisfied; engineering method and reference content remain visible.
Model basis
- State 1 uses the entered evaporating saturation temperature and suction superheat.
- State 2s is the isentropic compression state at the entered transcritical high-side pressure.
- State 2 applies the entered compressor isentropic efficiency.
- State 3 uses the entered gas-cooler outlet temperature at the same high-side pressure.
- State 4 applies isenthalpic expansion back to the evaporating pressure.
- COP is refrigerating effect divided by compressor specific work. Optional capacity converts specific quantities to mass flow, compressor power and gas-cooler duty.
Useful during reference & conversion work.
- Resolve unit-system differences quickly across calculations, drawings, schedules and vendor data.
- Look up common formulas, constants and engineering reminders without leaving the HVACR workspace.
- Reduce repeated manual conversion work while keeping the final engineering review with the user.
Frequently asked questions
Does HVACR Studio choose the optimum high-side pressure?
No. High-side pressure is an explicit engineering input. This calculator evaluates the entered cycle and does not provide a controller setpoint or automatic pressure optimization.
Why is high-side pressure entered as absolute pressure?
Thermodynamic property states use absolute pressure. The transcritical model also enforces pressure above the R744 critical pressure rather than treating the gas cooler as a conventional condenser.
Is this a compressor selection tool?
No. Isentropic efficiency is an input. Compressor maps, envelopes, volumetric efficiency, motor efficiency, oil management, discharge-temperature limits and manufacturer selection remain separate.
What is excluded from the model?
Pressure drops, internal heat exchangers, flash tank/receiver separation, parallel compression, ejectors, heat recovery, fan/pump power and transient control behavior are not included in this bounded single-stage cycle.