Steam Turbine with Open Regenerative Feed Heater

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SUMMARY

The discussion focuses on calculating the mass of steam bled from a steam turbine operating with a condenser pressure of 0.04 bar and a single open-type regenerative feed heater. The calculations utilize enthalpy values from steam tables, specifically h6 at 0.04 bar (121.41 kJ/kg) and h7 at 2 bar (505 kJ/kg). The correct equation for balancing the enthalpy is m (2264.1) + (1 – m) (121.41) = 505, leading to a calculated mass of steam bled of 0.179 kg to produce 1 kg of saturated feedwater at 2 bar.

PREREQUISITES
  • Understanding of steam tables and enthalpy calculations
  • Knowledge of regenerative feed heater operation
  • Familiarity with steam turbine thermodynamics
  • Basic algebra for solving equations
NEXT STEPS
  • Study steam tables for various pressures and enthalpy values
  • Learn about the principles of regenerative feed heaters in thermal systems
  • Explore advanced steam turbine cycle analysis techniques
  • Investigate energy loss considerations in thermal systems
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Mechanical engineers, thermal system designers, and students studying thermodynamics or steam turbine operations will benefit from this discussion.

PaxFinnica96
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Homework Statement
A steam turbine operates with a condenser pressure of 0.04 bar and has a single open-type regenerative feed heater. How much steam, at a pressure of 2 bar and a dryness fraction of 0.98, must be bled from the turbine to produce 1 kg of saturated feedwater at 2 bar?
Relevant Equations
m h3 + (1 – m) h6 = h7
I would very much appreciate anyone to cast their eye over my attempt at solving this problem which I've been struggling with the past few days. Many thanks in advance.

Assuming that:

  • energy input from open-type regenerative feed heater pump is negligible
  • no energy is lost
  • the heater pressure is the same as the bled pressure
h6 = hf at 0.04 bar = 121.41 kJ kg-1

h7 = hf at 2 bar = 505 kJ kg-1
Enthalpy at exit of turbine…

h3 = hf + x hfg at 2 bar (from steam tables)

h3 = 505 + 0.98 (1795) = 2264.1
Balancing the

m (2264.1) = (1 – m) (121.41) + 505

m = 0.26259

So, mass of steam bled from the turbine to produce 1kg of saturated feedwater as 2 bar would be 0.26259 kg
 
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PaxFinnica96 said:
Homework Statement:: A steam turbine operates with a condenser pressure of 0.04 bar and has a single open-type regenerative feed heater. How much steam, at a pressure of 2 bar and a dryness fraction of 0.98, must be bled from the turbine to produce 1 kg of saturated feedwater at 2 bar?
Relevant Equations:: m h3 + (1 – m) h6 = h7

I would very much appreciate anyone to cast their eye over my attempt at solving this problem which I've been struggling with the past few days. Many thanks in advance.

Assuming that:

  • energy input from open-type regenerative feed heater pump is negligible
  • no energy is lost
  • the heater pressure is the same as the bled pressure
h6 = hf at 0.04 bar = 121.41 kJ kg-1

h7 = hf at 2 bar = 505 kJ kg-1
Enthalpy at exit of turbine…

h3 = hf + x hfg at 2 bar (from steam tables)

h3 = 505 + 0.98 (1795) = 2264.1
Balancing the

m (2264.1) = (1 – m) (121.41) + 505
This equation should read

m (2264.1) + (1 – m) (121.41) = 505
 
Many thanks for your help, I get 0.179 kg
 

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