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ABC OF SUPER-CRITICAL

SUPER-CRITICAL FLUID:
A substance above its critical points at certain temperature & pressure. It do not have liquid- gas phase boundary. There is no surface tension in supercritical fluid. Above critical point in small increase in pressure causes a large increase in the density of the super critical phase. It has low viscosity and high diffusion.


1.    NO Gas –Liquid Phase boundary.
2.    NO Surface Tension
3.    low viscosities and high diffusivities
4.     capability to reduce particles up to a range of 5-2000 nm
5.    Less  reaction time



 Using water as the working fluid, this takes it into supercritical conditions. Efficiencies can be raised from about 39% for subcritical operation to about 45% using current technology

Tc (mix) = (mole fraction A) x Tc A + (mole fraction B) x Tc B


WHAT IS SUPER-CRITICAL?

Supercritical is a thermodynamic expression describing the state of a substance where there is no clear distinction between the liquid and the gaseous phase, as it is a Homogenous fluid.
Water reaches supercritical state at a pressure above 22.1 (MPa).
Operating pressure approx. at 19 MPa in the evaporator part of the boiler, the cycle is subcritical.
This means, that there is a non-homogeneous mixture of water and steam in the evaporator part of the boiler. In this case, a drum-type boiler is used because the steam needs to be separated from water in the drum of the boiler before it is superheated and fed into the turbine.
 Above pressure of 22.1 MPa in the evaporator part of the Boiler, the cycle is supercritical. The cycle medium is a single-phase fluid with homogeneous Properties and there is no need to separate steam from water in a drum.in supercritical cycle once-through boiler is required.

For once-through boilers, operating pressures up to 30 MPa represent the state of The art. However, advanced steel types must be used for components such as the boiler and the live steam and hot reheat steam piping that are in direct contact with steam under elevated conditions. Therefore, a techno-economic evaluation is the basis for the selection
Of the appropriate cycle parameters.




As the fluid pressure increases, Latent Heat (Enthalpy of Steam –Enthalpy of Water) reduces.
At Critical point it becomes zero.
In physical terms at this pressure water transforms to steam spontaneously.

SUPER CRITICAL STEAM PARAMETERS:

STEAM PRESSURE
STEAM TEMPERATURE
> 221.2 BAR
> 374.15 Deg C




   REQUIREMENT OF SUPER-CRITICAL

Supercritical coal fired power plants permits efficiencies that exceed 45%, depending on cooling conditions. Options to increase the efficiency above 50 % in ultra-supercritical power plants rely on elevated steam conditions as well as on improved process and component quality.

Steam conditions up to 30 MPa/600°C/620°C are achieved using steels with 12 % chromium content. Up to 31.5 MPa/620°C/620°C is achieved using austenite, which is a proven, but expensive, material.
Nickel-based alloys, e.g. Inconel, would permit 35 MPa/700°C/720°C, yielding efficiencies up to 48%. Other improvements in the steam cycle and components can yield a further 3 %.
Most of these technologies, like the double reheat concept where the steam expanding through the steam turbine is fed back to the boiler and reheated for a second time as well as heat extraction from flue gases have already been demonstrated.
There are no operational limitations due to once-through boilers compared to drum type boilers. In fact, once-through boilers are better suited to frequent load variations than drum type boilers, since the drum is a component with a high wall thickness, requiring controlled heating. This limits the load change rate to 3% per minute, while once-through boilers can
 Step-up the load by 5% per minute.

This makes once-through boilers more suitable for fast startup as well as for transient conditions.

Current designs of super-critical plants have installation costs that are only 2% higher than those of sub-critical plants. Fuel costs are considerably lower due to the increased efficiency & operating costs are at the same level as sub-critical plants. Specific installation cost i.e. Cost per megawatt (MW) decreases with increased plant size.

Reason behind need of super critical Power Plant:
      1. Demand for power is growing in fast pace with scarcity of Land,water & fuel.
       2. With tariff based bidding gaining ground, utilities have to bring down   their cost of generation to remain competitive.
      3. Requirement of Environment Green and Clean Technologies.
      4.  CDM (Clean Development mechanism) opportunities arising out of global warming concerns - by selling officially sanctioned certified emission reduction (CER) credits (Kyoto Protocol).


 Benefits of advanced supercritical power plants include:

1.     Reduced fuel costs due to improved plant efficiency.
2.     Significant reduction in CO2 emissions.
3.     Excellent availability, comparable with that of an existing sub-critical plant.
4.     Plant costs comparable with sub-critical technology and less than other clean coal technologies.
5.    Reduced NOx, SOx and dust emissions.
6.     Integrated with appropriate CO2 capture technology.

SUB-CRITICAL STEAM GENERATOR SYSTEMS

Water when heated at sub-critical pressure (< 22.1 MPa) increases in temperature until it starts to boil. While the water is boiling it exists as two phases, liquid and gas that have different mass densities, and remains at a constant temp. Known as the saturation temperature for the given pressure. Once all of the liquid has boiled off to steam (Evaporated) the temperature of the steam will continue to rise, at constant pressure, and is then referred to as superheated steam.

Sub-critical boilers typically have a means of separating the two phases, liquid and steam, to allow the process to be continuous. The separated liquid is recirculated through the evaporating section of the boiler and steam passes through to the superheating section.

This separation typically occurs in the boiler drum, a heavy thick walled steel pressure vessel with a series of cyclones and baffles to separate liquid from steam.
It is the mass of this boiler drum which limits the rate at which a sub-critical boiler can be brought on line and how well it responds to load changes which results in fuel being consumed for no energy compared with a more responsive boiler.

SUPER-CRITICAL STEAM GENERATOR SYSTEMS

When water is heated at a constant pressure above the critical pressure its temperature is Never constant and no distinction between gas and liquid can be made, the mass density of the two phases is the same. Properties of the water in the super-critical boiler continuously
Change from liquid to gas (steam).
i.e. Temperature rises steadily, Specific heat and rate of rise changes considerably

Liquid in the super-critical boiler is assumed to have changed to steam after the critical temperature for the super-critical pressure, as the steam is heated further it continues to gain temperature in a super heated state.

With the super-critical boiler there is no stage where the water exists as two phases and requires separation, so the boiler is constructed without a drum. Typically super-critical boilers are once through boilers where water pumped in at pressure by the Boiler Feed Pump passes progressively through the heating stages of the boiler and is delivered to the Turbine at final temperature with no re-circulation.

The actual location of the transition from liquid to steam in a once through super-critical Boiler is free to move with differing conditions. This means that for changing boiler loads & pressures the process is able to optimize the amounts of liquid and gas regions for efficient heat transfer keeping the high boiler efficiency over a wider range than sub-critical
Boilers with drums. 
TYPICAL BLOCK DIAGRAM FOR SUB-CRITICAL TURBINE CYCLE  




TYPICAL BLOCK DIAGRAM FOR SUPER CRITICAL TURBINE CYCLE