AUTIXON / ENGINEERING TOOLS
From compressor room to point of use. Assess electricity, pressure, leakage and the next justified improvement.
Start with motor power, discharge pressure, energized hours and tariff. Open detailed operating data only when available. Nameplate screening does not diagnose actual efficiency.
Use one consistent annual period. State hours must cover the total for a state-based energy calculation. Enter zero only for a confirmed absent state. Normalized flow: dry air, 0 °C, 1.01325 bar absolute.
No default factory, fabricated leakage or automatic saving. Add the data you have and analyze the system.
Assess compressor energy, leakage, unloaded operation, pressure performance, treatment losses, heat recovery and prioritized optimization.
Each compressor is modeled from available power, capacity and operating-state hours. Pressure, leakage, receiver, dryer and network inputs activate deeper analyses; every estimate retains its method and evidence level. Combined savings are constrained to reduce overlap.
Annual energy = Σ(state power × state hours)Specific energy = compressor energy / delivered normal volumeLeakage cost = estimated leakage energy × electricity tariffA 75 kW unit loaded for 4,000 h and drawing an entered 30% of rated power for 1,000 unloaded hours uses 322.5 MWh/year before auxiliary treatment loads.
Separate measured quantities from inferred leakage or control losses. First actions should target the largest supported cost with acceptable confidence, not a generic equipment replacement.
It can be estimated from off-production cycling or an explicit leakage percentage, but it is labeled estimated.
Only when process minimum pressure and network drop leave a safe margin; the assumption used must remain visible.
No. Variable demand, unloaded operation and sequencing evidence must justify the study.
No. It is a separate thermal-energy potential valued only against the displaced thermal source.