Rankine cycle



The Rankine cycle is a William John Macquorn Rankine, a Scottish polymath.

Description

 

A Rankine cycle describes a model of the operation of steam heat engines most commonly found in power generation plants. Common heat sources for power plants using the Rankine cycle are coal, natural gas, oil, and nuclear.

The Rankine cycle is sometimes referred to as a practical TS diagram will begin to resemble the Carnot cycle. The main different is that a pump is used to compress the liquid water. This requires about 100 times less energy that compressing a gas in a compressor (as in the Carnot cycle).

The efficiency of a Rankine cycle is usually limited by the working fluid. Without the pressure going combined cycle gas turbine power stations.

The working fluid in a Rankine cycle follows a closed loop and is re-used constantly. The water cooling towers. While many substances could be used in the Rankine cycle, water is usually the fluid of choice due to its favorable properties, such as nontoxic and unreactive chemistry, abundance, and low cost, as well as its thermodynamic properties.

One of the principle advantages it holds over other cycles is that during the compression stage relatively little work is required to drive the pump, due to the working fluid being in its liquid phase at this point. By condensing the fluid to liquid, the work required by the pump will only consume approximately 1% of the turbine power and so give a much higher efficiency for a real cycle. The benefit of this is lost somewhat due to the lower heat addition temperature. Gas turbines, for instance, have turbine entry temperatures approaching 1500°C. Nonetheless, the efficiencies of steam cycles and gas turbines are fairly well matched.

Processes of the Rankine cycle

 

There are four processes in the Rankine cycle, each changing the state of the working fluid. These states are identified by number in the diagram to the right.

  • Process 1-2: The working fluid is pumped from low to high pressure, as the fluid is a liquid at this stage the pump requires little input energy.
  • Process 2-3: The high pressure liquid enters a boiler where it is heated at constant pressure by an external heat source to become a dry saturated vapor.
  • Process 3-4: The dry saturated vapor expands through a turbine, generating power. This decreases the temperature and pressure of the vapor, and some condensation may occur.
  • Process 4-1: The wet vapor then enters a phase-change.

In an ideal Rankine cycle the pump and turbine would be isentropic, i.e., the pump and turbine would generate no entropy and hence maximise the net work output. Processes 1-2 and 3-4 would be represented by vertical lines on the Ts diagram and more closely resemble that of the Carnot cycle. The Rankine cycle shown here prevents the vapor ending up in the superheat region after the expansion in the turbine [1], which reduces the energy removed by the condensers.

Variables

\dot{Q}Heat flow rate to or from the system (energy per unit time)
\dot{m}Mass flow rate (mass per unit time)
\dot{W}Mechanical power consumed by or provided to the system (energy per unit time)
ηthermThermodynamic efficiency of the process (net power output per heat input, dimensionless)
ηpumpturbIsentropic efficiency of the compression (feed pump) and expansion (turbine) processes, dimensionless
h1,h2,h3,h4The "specific enthalpies" at indicated points on the T-S diagram
h4sThe final "specific isentropic
p1,p2The pressures before and after the compression process

Equations

Each of the first four equations[1] is easily derived from the energy and thermodynamic efficiency of the cycle as the ratio of net power output to heat input. As the work required by the pump is often around 1% of the turbine work output, equation 5 can be simplified.

\frac{\dot{Q}_{\mathit{in}}} {\dot{m}} = h_3 - h_2

\frac{\dot{W}_{\mathit{pump}}} {\dot{m}} = h_2 - h_1  \approx  \frac{v_1{\Delta}p}{\eta_{pump}} \approx  \frac{v_1 (p_2 - p_1)}{\eta_{pump}}

\frac{\dot{Q}_{\mathit{out}}} {\dot{m}} = h_4 - h_1

\frac{\dot{W}_{\mathit{turbine}}} {\dot{m}} = h_3 - h_4 = (h_3 - h_{4s}) \times {\eta_{turb}}

\eta_{therm} = \frac{\dot{W}_{\mathit{turbine}}-\dot{W}_{\mathit{pump}}} {\dot{Q}_{\mathit{in}}} \approx \frac{\dot{W}_{\mathit{turbine}}} {\dot{Q}_{\mathit{in}}}

Real Rankine cycle (non-ideal)

  In a real Rankine cycle, the compression by the pump and the expansion in the turbine are not isentropic. In other words, these processes are non-reversible and entropy is increased during the two processes. This somewhat increases the power required by the pump and decreases the power generated by the turbine. It also makes calculations more involved and difficult.

In particular the efficiency of the steam turbine will be limited by water droplet formation. As the water condenses, water droplets hit the turbine blades at high speed causing pitting and erosion, gradually decreasing the efficiency of the turbine. The easiest way to overcome this problem is by superheating the steam. On the Ts diagram above, state 3 is above a two phase region of steam and water so after expansion the steam will be very wet. By superheating, state 3 will move to the right of the diagram and hence produce a dryer steam after expansion.

Variations of the basic Rankine cycle

  The overall temperature \left( \bar{T}_\mathit{in} = \frac{\int_2^3 T\,dQ}{Q_\mathit{in}} \right) of that cycle. Increasing the temperature of the steam into the superheat region is a simple way of doing this. There are also variations of the basic Rankine cycle which are designed to raise the thermal efficiency of the cycle in this way; two of these are described below.

Rankine cycle with reheat

In this variation, two turbines work in series. The first accepts condensing during its expansion which can seriously damage the turbine blades, and improves the efficiency of the cycle.

Regenerative Rankine cycle

  The regenerative Rankine cycle is so named because after emerging from the condenser (possibly as a subcooled liquid) the working fluid is heated by steam tapped from the hot portion of the cycle. On the diagram shown, the fluid at 2 is mixed with the fluid at 4 (both at the same pressure) to end up with the saturated liquid at 7. The Regenerative Rankine cycle (with minor variants) is commonly used in real power stations.

Another variation is where 'bleed steam' from between turbine stages is sent to feedwater heaters to preheat the water on its way from the condenser to the boiler.

Organic Rankine cycle

The organic Rankine cycle (ORC) uses an organic fluid such as efficiency of the cycle is much lower as a result of the lower temperature range, but this can be worthwhile because of the lower cost involved in gathering heat at this lower temperature. Alternatively, fluids can be used that have boiling points above water, and this may have thermodynamic benefits.

The Rankine cycle does not restrict the working fluid in its definition, so the inclusion of an "organic" cycle is simply a marketing concept that should not be regarded as a separate thermodynamic cycle.

References

  1. ^ http://www.solar2006.org/presentations/tech_sessions/t38-A007.pdf
  2. ^ http://www.eere.energy.gov/troughnet/pdfs/batton_orc.pdf
  3. ^ Nielsen et al, 2005, Proc. Int. Solar Energy Soc.
  • ^Van Wyllen 'Fundamentals of thermodynamics' (ISBN 85-212-0327-6)
  • Moran & Shapiro 'Fundamentals of Engineering Thermodynamics' (ISBN 0-471-27471-2)
  • Wikibooks Engineering Thermodynamics
 
This article is licensed under the GNU Free Documentation License. It uses material from the Wikipedia article "Rankine_cycle". A list of authors is available in Wikipedia.