Steam Turbine
From SysCAD Documentation
Navigation: Main Page -> Models -> Energy Transfer Models
Contents |
General Description
The steam turbine converts steam energy into shaft work, which then can be converted to electrical work through the generator.
The configuration of the Steam turbine is very simple; the user needs only supply the required exhaust pressure and the Turbine isentropic efficiency.
The conditions of the steam inlet to the turbine is very important to the operation of the Steam Turbine. This includes the Temperature, pressure, mass flow and quality of steam. This information is normally specified in the Steam Feeder.
From the information provided, SysCAD will calculate the exhaust steam temperature, quality and the amount of power that can be generated from the steam.
Diagram
The diagram shows the default drawing of the Steam Turbine, with the required connecting streams. The Steam Turbine expects the inlet to be Steam, the valid conditions are: 2 phase saturated wet steam, pure saturated steam or superheated steam. The outlet from the turbine is the Exhaust steam and generated power.
Inputs and Outputs
|
Label |
Input / Output |
No. of Connections |
Description | |
|
|
|
Min |
Max. |
|
|
Steam |
In |
1 |
1 |
The steam inlet. |
|
Exhaust |
Out |
1 |
1 |
The exhaust steam. |
Model theory
From the first law of thermodynamics, the energy balance is obtained by:
Assumptions
- The process is in steady state, thus dE = 0.
- A turbine can have heat transfer out through the casing, but typically they are well insulated so that the heat loss is small and given that the mass flow rate is large, the heat transfer per unit mass is almost nothing and thus is ignored. Thus Q = 0.
- The height difference between the inlet and outlet is negligible in terms of potential energy and this term is ignored. Thus, P = 0
- There may be some velocity effects (kinetic energy) if the exit velocity is very high. This is usually not known or measured and is implicitly included in the turbine efficiency - this term is ignored. Thus, K = 0.
- There is no loss of mass. Thus, mass in = mass out.
Calculating Work
From the above assumptions, the simplified energy balance is:
The analysis of turbine performance starts with the ideal turbine. The ideal work is what a turbine could produce when expanding steam from given initial conditions to a given final pressure with 100% efficiency. Thus step 1 of the calculation is:
(1) Calculate the ideal work output - an ideal turbine is isentropic so that exit entropy equals inlet entropy - the exit steam conditions and work is obtained from this.
The actual work is determined from the turbine efficiency (also known as the isentropic or adiabatic efficiency), which is simply a measure of how well the turbine is doing compared to a perfect machine operating under the same conditions. Thus step 2 of the calculation is:
(2) Actual work = ideal work * turbine efficiency.
The actual enthalpy out can be calculated from the actual work done, such step 3 is:
(3) Actual enthalpy out = enthalpy in - Actual work
From the actual enthalpy out and the specified required pressure of the exhaust, the actual temperature out and the quality of the steam can be calculated.
Calculating Power
Checking of Steam conditions
During the work calculations, checking of steam quality is important since the exhaust may have some condensation in it if enough energy is extracted from it. (Generally this is never more than a few percent in real turbines because water droplets moving close to the speed of sound can have a terrible erosive power which can damage the last few blade rows very quickly).
Typically, there are four cases of steam conditions that can exist in the turbine calculation:
| CASE | INLET STEAM | IDEAL EXHAUST | ACTUAL EXHAUST |
| (1) | superheated | superheated | Superheated |
| (2) | superheated | saturated | Superheated |
| (3) | superheated | saturated | Saturated |
| (4) | saturated | saturated | Saturated |
NB: saturated inlet means saturated exhaust.
In the case where the steam has some condensate in it - i.e. wet steam or the quality (x) is less than 100%, the calculations gets slightly lengthier.
For a detailed step-by-step calculation routine, please see section under Flowchart.
Flowchart
The following shows the steps in determining quality and condition of the exhaust steam, as well as the calculation of power generated.
Data Sections
The default access window consists of three sections:
- The first tab contains general information relating to the unit.
- The Info section, contains general settings for the unit and allows the user to include documentation about the unit and create Hyperlinks to external documents. This is fully described in Common Data Sections.
- Links tab, only visible in SysCAD 9.2, contains a summary table for all the input and output streams.
- Audit tab - contains summary information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples.
Class: Turbine - The first tab page in the access window will have this name.
Adding this Model to a Project
Insert into Configuration file
Sort either by DLL or Group.
|
|
DLL: |
HeatXch1.dll |
→ |
Units/Links |
→ |
Heat Transfer: Steam Turbine |
|
or |
Group: |
Energy Transfer |
→ |
Units/Links |
→ |
Heat Transfer: Steam Turbine |
See Project Configuration for more information on adding models to the configuration file.
Insert into Project
|
|
Insert Unit |
→ |
Heat Transfer |
→ |
Steam Turbine |
See Insert Unit for general information on inserting units.
Hints and Comments
- The steam turbine has a single extraction pressure, for modelling work of turbines with multiple extraction pressure sections; a number of turbines can be drawn in parallel with a steam feed splitter to simulate the process.
- Always double check if the steam feed conditions are valid. Use the VLE option in the Feeder-Cross Page Connector to add in a level of checking.
- If steam feed is not valid, then SysCAD will try and flash the feed stream to its saturated conditions (based on the inlet pressure.) This will change the feed stream temperature, as the flashing of the mixture will cool down the stream, while trying to keep its enthalpy constant.


