3 replies to this topic

[Moaazgs]

I have to Design Fired Heater For Refinery Uses 

 

I Designed the Radiant and Convection Section For the Crude oil 

wheres the Stack Temp after Convection = 379 C 

I Need to integrate this energy

 

What I have to do to Reduce the Stack Temperature ?!

whats the Maximum temperature are acceptable For Stack Temp where is Will not effect on Environment ?!

 

 i have to add Air or Steam on pipes on the Convection section to Increase their Temperature For Further uses are that is Right  ?

Edited by Moaazgs, 27 June 2014 - 08:12 PM.

[sukanta87]

Hi Moaazgs,

 

There can be an economizer section for process streams as a sequence of radiant>convection>economizer>stack out.

[Moaazgs]

Thanks , Thats my first time to working on Design project , I wanna ask about Images from inside Crude heater to can imagine every part

[sukanta87]

I have not any design experience on fired heater. You can google or hope will get response from experts here.

Just for your starting you can check GPSA (Direct fired heater),

http://staging.detroitradiant.ideosolutions.com/wp-content/uploads/2013/01/LIODEG_Design-Engineering-Guide_10-11.pdf, 

mondane at http://www.modine.com/download/8np2jt6bu2vq4o8i9j8a1too60/9-200.pdf,

http://www.ametekpi....ed-heaters.pdf.

Edited by sukanta87, 01 July 2014 - 10:37 AM.