Dear Friends,
I am enclosing the Excel Spreadsheet which contains the boiler feed water required for the desuperheaters I hope this will be helpful.
|

Desuperheater Boiler Feed Water Required Calculations
Started by Padmakar Katre, Mar 17 2007 07:46 AM
5 replies to this topic
Share this topic:
#1
Posted 17 March 2007 - 07:46 AM
#2
Posted 17 March 2007 - 10:22 AM
Padmakar:
Your attachment spreadsheet did not make it into the posting.
Maybe you did not follow the correct procedure for uploading an attachment. The Forum doesn't offer any "friendly" instructions, so you have to practice at it.
Tell us if you need help in uploading.
#3
Posted 18 March 2007 - 03:00 AM
I am sorry I think I did mistake now I will upload it.
Attached Files
#4
Posted 06 June 2009 - 03:18 AM
QUOTE (Padmakar S Katre @ Mar 18 2007, 04:00 AM) <{POST_SNAPBACK}>
I am sorry I think I did mistake now I will upload it.
Hello Mr Padmakar
Your spread sheet , seems you hav eduly focused on getting the saturated steam out of boiler. But one thing which iam vague about , why it is required to bring the superheated steam to saturated steam out of the boiler. I conceive the superheated steam will have more adventagous by accounting of more enthalpy addition and hence more power generation. Our boiler vendor are using the desuperheater after the superheater , though i intend of their application , as perhabs to be used to configure and maintaining the superheated steam up to its boundary level
Awaiting for your reply
#5
Posted 12 June 2009 - 06:45 AM
Dear,
Let me clear you first thing that Desuperheater is not a part of any boiler. Desuperheater comes in the PRDS (Pressure Reduction and Desuperheating Section). The requirement of this section depends upon the type of boiler generated steam (saturated or Superheated), the users (based on the inlet pressure). When you have superheated steam coming from the boiler you can't use it in reboilers so you need to have saturated steam and you get it by injecting the boiler feed water into the superheated steam in a device called Desuperheater. Actullay in process plants there are different steam users at different pressure levels now when you let down the steam from a higher pressure to the required pressure/s (if steam grid consist of diff pressure steam headers) due to an adiabatic expansion across the pressure let down valve you will find the degree of superheat which we have to remove befor the steam would be used in reboilers. Here the need comes of injection of boiler feed water.
Reply to your second doubt is that in any boiler there is no any desuperheater but an attemptator which controls the superheater outlet temperature of the steam. The steam generated in boiler steam drum (heated in mud drum) will be the saturated steam which will go to superheater (part/section of boiler) to make the steam superheated. Here the outlet steam temperature is controlled by the injection of BFW in an attemptator (and not a desuperheater).
I hope this will clear your doubt.
Let me clear you first thing that Desuperheater is not a part of any boiler. Desuperheater comes in the PRDS (Pressure Reduction and Desuperheating Section). The requirement of this section depends upon the type of boiler generated steam (saturated or Superheated), the users (based on the inlet pressure). When you have superheated steam coming from the boiler you can't use it in reboilers so you need to have saturated steam and you get it by injecting the boiler feed water into the superheated steam in a device called Desuperheater. Actullay in process plants there are different steam users at different pressure levels now when you let down the steam from a higher pressure to the required pressure/s (if steam grid consist of diff pressure steam headers) due to an adiabatic expansion across the pressure let down valve you will find the degree of superheat which we have to remove befor the steam would be used in reboilers. Here the need comes of injection of boiler feed water.
Reply to your second doubt is that in any boiler there is no any desuperheater but an attemptator which controls the superheater outlet temperature of the steam. The steam generated in boiler steam drum (heated in mud drum) will be the saturated steam which will go to superheater (part/section of boiler) to make the steam superheated. Here the outlet steam temperature is controlled by the injection of BFW in an attemptator (and not a desuperheater).
I hope this will clear your doubt.
#6
Posted 12 June 2009 - 05:41 PM
excellent reply .....Padmakar.
I would also like to add that many times turbine drives exhaust steam will be at a pressure higher then next lower Pressure level in plant.So you have to letdown this stream and also desuperheat as you mentioned....
C.
I would also like to add that many times turbine drives exhaust steam will be at a pressure higher then next lower Pressure level in plant.So you have to letdown this stream and also desuperheat as you mentioned....
C.
Similar Topics
![]() Steam Sparger In Atmospheric Water TankStarted by Guest_owe_* , 16 May 2025 |
|
![]() |
||
Water Hammer Study: Hysys Dynamics Vs PipenetStarted by Guest_powerox29_* , 07 Apr 2025 |
|
![]() |
||
![]() Steam Carrying Liquid From The Sour Water Stripping TowerStarted by Guest_kaidlut_* , 12 Sep 2024 |
|
![]() |
||
![]() Dynamic Simulation After Feed Flow ReductionStarted by Guest_Kakashi-01_* , 20 Mar 2025 |
|
![]() |
||
Water TreatmentStarted by Guest_not_mikhail_* , 01 Apr 2025 |
|
![]() |