Tek-Tips is the largest IT community on the Internet today!

Members share and learn making Tek-Tips Forums the best source of peer-reviewed technical information on the Internet!

  • Congratulations MintJulep on being selected by the Eng-Tips community for having the most helpful posts in the forums last week. Way to Go!

Steam flow calculation 3

Status
Not open for further replies.

flinana

Electrical
Joined
May 21, 2003
Messages
129
Location
SA
I have a calculation based on enthalpy so as to attemperate steam to a turbine. The calculation has the following formula which I can´t understand.

Flow = m x(Enthalpy (HPT)- Enthalpy (CRH) /Enthalpy (CRH) - 764.8) kg/s

Enthalpy (HPT) = High pressure turbine. Enthalpy calculated from presssure and temperature before HP turbine

Enthalpy (CRH) = Enthalpy calculated from pressure and temperature before reheater, to where the HP steam is bypassed.

m = mass flow according to Steam valve opening, using pressure and temperature before valve.

Find logic attached.

The part I dont get is (Enthalpy (HPT)- Enthalpy (CRH) /Enthalpy (CRH) - 764.8).

Can someone explain.

thanks
 
Finana,

You have stream IN with enthalpy equal to enthalpy (HPT).
You have stream OUT with enthalpy equal to enthalpy (CRH)

The value 764.8, I presume expressed in kJ/kg, should be the specific water enthalpy at saturation pressure (9.08 barg) or saturation temperature (180.344 °C) before reheater. What works here is the enthalpy of evaporation, which is the difference between the specific enthalpy of steam and the specific enthalpy of water.
 
thanks, but i dont get is why the enthalpy out does not include the enthalpy from the ST outlet. Enthalpy in = enthalpy out, i.e.Enthalpy of steam = enthalpy of steam after water has been sprayed. But the pressure reading is taken after the connection from the ST hP exhaust!! see my dwg attached.
 
 http://files.engineering.com/getfile.aspx?folder=869b8baf-a248-4ba5-8afb-630c5e02f117&file=20101001110907.pdf
sounds like they've taken the worst case (no work by the turbine)
 
Good point hacksaw. But why attemperate in that case?
 
Just rearrange the terms and end up with the first law balance across the spray station:

(Whpt+Ws)*Hcrh = Whpt*Hhpt+Ws*Hs

where Hs= spray water enthalpy
 
Status
Not open for further replies.

Part and Inventory Search

Sponsor

Back
Top