Type of Steam

Pressure –Temperature Relationship of Water & Steam:

If water is heated beyond the boiling point, it vaporizes into steam, or water in the gaseous state. However, not all steam is the same. The properties of steam vary greatly depending on the pressure and temperature to which it is subject.

Saturated (dry) steam results when water is heated to the boiling point (sensible heating) and then vaporized with additional heat (latent heating). If this steam is then further heated above the saturation point, it becomes superheated steam (sensible heating).

Saturated Steam:-

As indicated by the black line in the above graph, saturated steam occurs at temperatures and pressures where steam (gas) and water (liquid) can coexist. In other words, it occurs when the rate of water vaporization is equal to the rate of condensation.

Advantages of using saturated steam for heating

Saturated steam has many properties that make it an excellent heat source, particularly at temperatures of 100 °C (212°F) and higher. Some of these are:

Wet Steam:

This is the most common form of steam actually experienced by most plants. When steam is generated using a boiler, it usually contains wetness from non-vaporized water molecules that are carried over into the distributed steam. Even the best boilers may discharge steam containing 3% to 5% wetness. As the water approaches the saturation state and begins to vaporize, some water, usually in the form of mist or droplets, is entrained in the rising steam and distributed downstream. This is one of the key reasons why separation is used to dis-entrain condensate from distributed steam.

Dry steam: 

Dry Steam is saturated steam that has been very slightly superheated. This is not sufficient to change its energy appreciably, but is a sufficient rise in temperature to avoid condensation problems, given the average loss in temperature across the steam supply circuit. Towards the end of the 19th century, when superheating was still a less-than-certain technology, such steam-drying gave the condensation-avoiding benefits of superheating without requiring the sophisticated boiler or lubrication techniques of full superheating.

Superheated Steam:

Superheated steam is created by further heating wet or saturated steam beyond the saturated steam point. This yields steam that has a higher temperature and lower density than saturated steam at the same pressure. Superheated steam is mainly used in propulsion/drive applications such as turbines, and is not typically used for heat transfer applications.

Advantages of using superheated steam to drive turbines:

• To maintain the dryness of the steam for steam-driven equipment, whose performance is impaired by the presence of condensate

• To improve thermal efficiency and work capability, e.g. to achieve larger changes in specific volume from the superheated state to lower pressures, even vacuum.

It is advantageous to both supply and discharge the steam while in the superheated state because condensate will be generated inside steam-driven equipment during normal operation, minimizing the risk of damage from erosion or carbonic acid corrosion. In addition, as the theoretical thermal efficiency of the turbine is calculated from the value of the enthalpy at the turbine inlet and outlet, increasing the degree of superheating as well as the pressure raises the enthalpy at the turbine inlet side, and is thereby effective at improving thermal efficiency.

Disadvantages of using superheated steam for heating:

For these reasons and others, saturated steam is preferred over superheated steam as the heating medium in exchangers and other heat transfer equipment. On the other hand, when viewed as a heat source for direct heating as a high temperature gas, it has an advantage over hot air in that it can be used as a heat source for heating under oxygen-free conditions. Research is also being carried out on the use of superheated steam in food processing applications such as cooking and drying.

Flash Steam:

The term ‘Flash Steam’ is traditionally used to describe steam billowing from condensate receiver vents and open-ended condensate tanks and discharge lines from steam traps.

A phenomenon caused, when hot condensate passes, from a high pressure system to a low pressure system. It happens instantaneously, virtually in a Flash, hence the name Flash steam.

Often mistaken as live steam leaking and a reflection on Trap condition.

How is Flash Steam Formed?

The case where the high pressure condensate temperature is higher than the low pressure saturation temperature

Flash steam occurs whenever water / condensate at high pressure and at a temperature that is higher than the saturation temperature at low-pressure discharge, is allowed to drop to the lower pressure. Conversely, if the temperature of the high-pressure water is lower than the saturation temperature at the lower pressure, flash steam cannot be formed. In the case of condensate passing through a steam trap; it is usually the case that the upstream temperature is high enough to form flash steam.

Consider a kilogram of condensate at 7 bar-g and a temperature of 169.6OC (saturation temp) passing through a steam trap and thus exposed to a lower pressure of 1.0bar-g.

The amount of energy in one kilogram of condensate at saturation temperature at 7.0bar-g is 171 kCal.

In accordance with the First Law of Thermodynamics, the amount of energy contained in the fluid upstream and downstream of the trap must be equal, as per the principle of conservation of energy.

Consequently, the heat contained in one kilogram of fluid downstream of the trap [1.0 Bar-g] is also 171 kCal. However, water at 1.0bar-g is only able to contain 120 kCal of heat (sensible heat at saturation temp & 1.0bar-g pressure), subsequently there appears to be an excess in heat on the upstream side by 171 – 120 = 51 kCal.

This excess heat is then used as enthalpy of evaporation resulting in part of condensate quantity again converting into steam referred to as Flash Steam and this process is known as flashing.

The amount of flash steam produced at the Lower / downstream / final pressure (P2) can be determined using the Equation:


P1 = Initial pressure (higher pr)

P2 = Final pressure (lower pr)

hf = Liquid enthalpy/Sensible heat  (kCal/kg)

hfg= Enthalpy of evaporation / Latent Heat  (kCal/kg)

Example – 1:
Example – 2:

The Principles of Conservation of Energy and mass between two process states:

1 kg of condensate at 7.0bar-g and 169.6°C produces 0.097 kg of flash steam at 1.0bar-g pressure.

The total mass of flash and condensate remains at 1 kg.

The principle of energy conservation states that the total energy in the low pressure state must equal the total energy in the high pressure state.

Therefore, the amount of heat in the flash steam and condensate must equal to 171 Kcal, that in the initial condensate.

Steam tables give the following information:

Total enthalpy of saturated water at 1.0bar-g pressure (hf) = 120 kCal/kg

Total enthalpy in saturated steam at 1.0bar-g pressure (hg) = 646.2 kCal/kg

Therefore, at the lower pressure state of 1.0bar-g,

Total enthalpy in the water = 0.903 kg X 120 kCal / kg [A]   = 108.36 kCal/kg

Total enthalpy in the steam = 0.097 kg X 646.2 kCal / kg [B] = 62.68 kCal/kg

Total enthalpy in condensate and steam at the lower pressure = A + B = 171 kCal/kg

Therefore, according to the steam tables, the enthalpy expected in the low pressure state is the same as that in the high pressure state – the principle of conservation of energy.

About Us
About Uni Klinger
Vision & Mission
Manufacturing Resources
Fluid Control Division
Fluid Sealing Division
Safety Valve and Control Valve Division
UKL Global Footprints
Fluid Control Division
Piston Valves
Bellow Seal Valves
Disc Check Valve
High Pressure Valve
Steam Traps
Thermodynamic Steam Traps
Thermostatic Steam Traps
Ball Float Traps
Clean Steam Trap
Inverted Bucket Traps
Bi Metallic Bi Thermostatic Trap
Automatic Pumping Trap
Trap Modules
Intelligent Trap Valve Station
High Pressure Thermodynamic Steam Trap Compact Module
Steam supply and Condensate return Manifolds
Pipeline Accessories
Air Vent & Air Vent Assembly
T & Y Type Strainers
Air Eliminators
Moisture Separators
Sight Glass
Pressure Reducing Station
Heat Recovery Products
Flash Vessels
Pressured Power Pump Unit
Steam Injectors
Deaerator Head
Liquid Level Gauges
Leak Tector
Hot Water Generation System
Fluid Sealing Division
Jointing Sheets
Compressed Asbestos Fiber (CAF)
Compressed Non-Asbestos Fiber (NCAF)
Expanded PTFE Sheets
Graphite sheet
Metallic/ Semi-Metallic Gaskets
Spiral Wound Gasket
Metal Jacketed Gasket
Kammprofile Gasket
Ring Joints
Gland Packing
Non-Asbestos Gland Packing
Industrial Gasket Division
Safety Valve and Control Valve Division
UKL-AST Safety Relief Valve
SMU-7000 Safety Relief Valve
SMFN -7000 & SU-7000 Safety Relief Valve
AST Spa Products
AST CV-8000 Control Valve
AST SMS-7100 Safety Valve for Steam Boiler
AST SVP-7200 Pilot Operated Safety Valve
Steam Engineering Services
More Industries
Fertilizer Industry
Aerated Concrete Block Industry
Tyre Industry
Rice Industry
Sugar Industry
Edible Oil Industry
Captive Cogen Industry
Soap Industry
Textile Industry
Chemical Industry
Hotel Industry
Pharma Industry
Brewery Industry
Dairy Industry
Rubber Industry
Case Study
Case Study-Textile Industries
Case Study-Chemical Industry
Case Study-Tyre Industry
Ask the Expert
Return On Invesment
ROI by Flash Vessel
ROI by Pressure Powered Pump
ROI by Pressure Reducing Station
Steam Engineering Guideline
Advantages of Steam
The Boiler
Contact Us
Enquiry Form
Sales and Factory Offices
Whats New