Superheated Steam and Steam Phase DiagramPublished on 24/2/2012 and last updated on Friday 2nd of March 2018 at 03:36:16 PM
Superheated SteamWhen saturated steam generated in steam boiler is further passed through a heat transfer surfaces, then its temperature will starts increasing above evaporation or saturation.
Steam is described as super heated, if its temperature is more than that of its saturation temperature. Degree of super-heat is directly related with the temperature of the steam heated above the saturation temperature. Super heat can only be provided to saturated steam and not to steam with presence of moisture content. For achieving a super heat, saturated steam has to pass through another heat ex-changer. This heat ex-changer for super-heating is called a secondary heat ex-changer within the boiler. Hot flue gas coming out from the boiler is considered to be a best way of heating the saturated steam. Superheated steam finds its application in steam power plants for the generation of electrical power. In steam turbines, superheated steam enters at one end and exit from the other end into the condenser (may be of water or air cooled type). The differential of the Superheated steam energy between the turbine inlet and outlet causes the turbine rotor to turn. There is a gradual reduction of the steam energy while it passing through the turbine rotor.
So it is essential to have a sufficient super-heat at the turbine inlet, so as to avoid the condensation of wet steam at the later part of the turbine rotor. Basically steam turbine rotor has got number of stages and the steam has to pass through each stage before reaching the condenser. So if the enough superheat is not provided in the steam at the turbine inlet, then the steam may get saturated while reaching the later stages of the rotor and subsequently get wetter while passing through the each successive stage. Wet steam at the tail end of the rotor is very dangerous as it may lead to Water Hammer and severe erosion at the last stages of the turbine blades. In order to over-come this problem it is advisable to design the inlet steam parameters of steam turbine inlet in such way that super heated steam allow to enter at the turbine inlet and the turbine exhaust are designed to match the steam parameters close to saturated conditions. One of the major reasons for using the Super heated steam in steam turbine is appreciable improvement in the thermal efficiency of the cycle.
Heat engine efficiency can be found by using either: Carnot Cycle efficiency: Ratio of temperature difference between inlet and outlet to inlet temperature. Rankine cycle efficiency: Ratio of heat energy at the turbine inlet and outlet to the total heat energy taken from the steam. 2. Example of calculating the Carnot Cycle and Rankine Cycle Efficiency. Explained by Example: A turbine is supplied with superheated steam at 96 bar at 490oC. The exhaust is at 0.09 bar and at 12 % wetness. Temperature of saturated steam is : 43.7oC Determine and Compare the Carnot Cycle and Rankine cycle. Procedure to determine the Carnot cycle efficiency :
Procedure to determine the Rankine cycle efficiency : Where, Sensible heat in condensate corresponding to exhaust pressure of 0.09 bar in KJ/Kg = 183.3 3. Steam-Phase diagram is a graphical representation of data provided in the steam table. Steam-Phase diagram provides the relationship between enthalpy, temperature corresponding to various pressures. Liquid Enthalpy hf. This is represented by line A-B on the phase-diagram. When the water starts receiving heat from 0o C, then it receives all its liquid entahlpy along the saturated water line A-B on the phase diagram Enthalpy of Saturated Steam (hfg): Any further heat addition results in change in phase to saturated steam and is represented by (hfg) on phase diagram i.e B-C.
Dryness Fraction (x): When heat is applied then the liquid start changing its phase from liquid to vapour and then the dryness fraction of the mixture starts increasing i.e moving towards unity. In the phase diagram dryness fraction of the mixture is 0.5 at exactly mid of the line BC. Similarly at point c on the phase diagram dryness fraction value is 1. Line C-D Point c is in the saturated vapour line, any further heat addition results in increasing the steam temperature i.e beginning of steam superheating represented by line C-D. Liquid Zone → Region towards left side of the saturated liquid line Super heat zone → Region towards right side of the saturated vapour line Two phase Zone → Area between the saturated liquid and saturated vapour line is mixture liquid and vapour. Mixture with varied dryness fractions. Critical Point → It is the Apex point where saturated liquid and saturated vapour lines meet. Enthalpy of evaporation diminishes to zero at critical point, it means that water changes directly to steam at critical point and thereafter. Maximum temperature which liquid can attain or exist is equivalent to critical point. Critical point Parameters → Temperature 374.15oC Pressure → 221.2 bar Values above this are super-critical values and are useful in increasing the efficiency of the rankine cycle.