Utility Simulator
Explore how load, flow and operating conditions influence three utility systems. All outputs are educational estimates, not control settings.
Within illustrative band
Air and water flow are sufficient for this illustrative load.
What the simplified models assume
The cooling-tower example uses a 3 °C approach at 80% load, 80% fan speed and 100 m³/h circulating flow. Approach is scaled with load and simplified airflow/water-flow factors. Fan power follows a cubic speed relationship using a 15 kW reference. Wet-bulb temperature establishes the approximate thermodynamic cooling floor; this model omits fill condition, recirculation and detailed psychrometrics.
The compressor assumes 6.4 kW per m³/min at its reference point. Required production equals useful demand divided by one minus the leakage fraction. Filter differential and intake temperature apply simplified power penalties. It omits pressure-ratio curves, unloading cycles and compressor-specific control strategies. These assumptions are illustrative, not a promise of savings.
The boiler uses a 10 t/h reference and 2,778 kJ/kg illustrative steam enthalpy. Feedwater enthalpy is approximated by 4.186 times its Celsius temperature. Excess air and blowdown reduce estimated efficiency. Actual efficiency depends on fuel, pressure, feedwater chemistry and design; this model must never be used for combustion tuning. Daily cost equals estimated input power × running hours × entered USD energy tariff. For boilers, enter a fuel-energy tariff rather than an electricity price.
Guidance only. Follow manufacturer limits and site procedures; hazardous work requires qualified personnel.
