| Feature |
One Atmosphere Boiler |
Water Tube Steam Boilers |
Electric High Pressure Steam Boilers |
| Maximum Steam Temperature1 |
300-1300°C Standard |
600°C with Economiser and Superheater |
134°C for 3 bar steam |
| Efficiency |
~95% |
<90% |
~85-95% |
| Idle Energy Waste |
Low |
High |
Moderate |
Non Steam Producing Energy Usage Time
(Start Up Time2) |
Nearly Instant |
60+ Minutes. Becomes slower with higher pressures and volume requirements |
~60 Minutes. Becomes slower with higher pressures and volumes. (Not including cool down and pressure release for autoclaves) |
| Suggested Inlet Temperature3 |
Tap |
40-60°F |
20-35°C |
| Capital Cost per Kg of Steam3 |
Low |
High |
Moderate. Depends on temperature/pressure required. |
| Operational Costs4 |
Low |
High |
Low-Moderate |
| Unit Footprint |
Starting at 1'x1'x1' |
Large |
Depends on size and pressure requirements. |
| Plug & Play Operations |
Yes |
No |
No |
| Requires Boiler Certifications5 |
No |
Yes |
Yes |
| Downtime6 |
Low |
Low-Moderate |
Low |
| Utilizes Combustion7 (Requires Ventilation) |
No |
Yes |
No |
| Energy Needed to produce 100 Kg/hr steam from cold start |
~100 kWh |
~150-200 kWh Equivalent (Inluding start up time consumption) |
~150kWh Equivalent (Inluding start up time consumption) |
| Power Weight [Kg Equipment/(Kg/hr) of steam] for a 100kW Generator |
~2 Kg per Kg/hr of steam |
~5 Kg per Kg/hr of steam (Weight increases with temperature/pressure) |
- |
| Maximum Work Potential (Based on second law limitation) Base is 1 Bar 100C liquid water for all. |
672 kJ/Kg for 500°C superheated steam
1973 kJ/Kg for 1300°C superheated steam |
755 kJ/Kg for 10 Bar saturated steam
1169 kJ/Kg at 100 Bar saturated steam |
Generally not used for creating work. |
| Enthalpy (heat) Content |
3489 kJ/Kg for 500°C superheated steam at 1 Bar |
2777 kJ/Kg for 10 Bar saturated steam
Saturation steam temperature 180°C |
2725 kJ/Kg for 3 Bar saturated steam
Saturation steam temperature 311°C |
| Running at Partial Capacity |
With MHI Electronic Controls, No loss of efficiency |
Significantly lower efficiencies, if model is capable |
Lower efficiencies |
| Air Contamination Effects |
Extremely high operation temperatures diminish effects of air |
Air contamination harms output |
No air contamination is allowed (strict) |
| Piping Losses |
Discrete, locatable units reduce necessary piping. Low, 1 atmosphere pipe pressure. |
High pipeline pressure combined with long piping distances leads to heat loss and dangerous conditions in the event of pipe failure. |
High pipeline pressure combined with long piping distances leads to heat loss and dangerous conditions in the event of pipe failure. |