Convert common HVAC engineering units.
Two-Stage Compression & Intercooling
Analyze a bounded two-compressor-stage vapor-compression cycle with an explicit intermediate-pressure basis and constant-pressure external intercooling. Unlike flash economizing, the same refrigerant mass flow passes through both stages.
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Cycle model
- Low-stage suction starts from the entered evaporating dew condition and superheat.
- The first compressor raises the vapor to the selected intermediate pressure.
- An idealized external intercooler cools the vapor at constant intermediate pressure to the entered interstage superheat.
- The second compressor raises that vapor to condensing pressure.
- The condenser produces the entered bubble-referenced subcooled liquid state.
- Isenthalpic expansion returns the refrigerant to evaporating pressure.
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
How is this different from the flash economizer / vapor-injection tool?
This model keeps one refrigerant mass flow through both compressors and removes heat in an external constant-pressure intercooler. It has no flash separator, vapor injection or interstage mass addition.
Can I use zeotropic blends?
Yes within the generated range because the model does not split vapor and liquid composition. Interstage vapor conditions use dew-point references, while the condenser liquid state uses the bubble-point reference.
What does balanced intermediate pressure mean?
Balanced mode uses the geometric mean of evaporating and condensing absolute pressure. It approximately balances ideal stage pressure ratios; it is not an optimum pressure, compressor recommendation or control setpoint.
Does the intercooler duty size the intercooler?
No. It is the theoretical heat rejected between compressor stages. Heat-exchanger approach, airflow or water flow, fouling, fan/pump power and control method remain separate design inputs.