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Furnace Transfer Line Sizing


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#1 Preeti Shetty

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Posted 11 September 2013 - 04:28 AM

Good Afternoon Everyone,

 

I am sizing a Transfer Line i.e. from Furnace heater to the inlet of column, I have sized this line based on two phase line sizing criteria. I needed the Transfer line sizing criteria, like what parameters need to be checked while sizing transfer line as these line are critical lines.

 

Thank you,

 

Preeti.



#2 Himanshu Sharma

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Posted 11 September 2013 - 06:59 AM

if the column in question is a  Vacuum Column ?



#3 Preeti Shetty

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Posted 12 September 2013 - 04:03 AM

Hi,

Thanks for your response

 

The column is not a VDU its a Crude Distillation Tower operating at 2.5 bara.

 

Preeti S.



#4 AzoTik1985

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Posted 24 September 2013 - 01:39 AM

You have to keep annular regime in transfer line. Line should not be sharp turns.



#5 Himanshu Sharma

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Posted 05 October 2013 - 05:39 AM

well life is comparatively easier if it's an atmospheric Column rather than a Vacuum Column !
 
Please take care of Following
 
1.Annular flow Regime is most stable amd most preferable for any General Two-phase flow ,however also check for flow ragimes at turndown flowrates also and advise Mechanical piping group for proper supports.I would also prefer to size line in segments as per varying operating pressure along the length from variousheater passes to the Main tranfser line  (however that is more significant in case of vacuum heater/Column)
 
2.Ensure that pressure drop in the line matches with Furnace Outlet pressure(Infact heater and transfer line hydraulics should be done simultaneously)
 if Pressure Drop is higher Builtup backpressure at Furnace Outlet is more than it was designed and hence there are chances of         coking
if Pressure Drop is lower that designed Heater Oulet pressure there may be more flashing and increased velocity thereof may erode lines/cause piping supoort issues.
 
3.Try to minimize the run length  ,long transfer lines with many crosses and tee’s will rapidly coke and increase the pressure on the furnace which usually results in increased fouling of the tubes in the furnace.
 
4.For Design Pressure consideration,Calculate backwards from Column Maximum operating pressure and keep on adding dynamic loss elements.
 
5.Design Temperature is genreally governed by Heater COT.
 
Hope this helps,
 
Regards
Himanshu


#6 TechExpert

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Posted 06 October 2013 - 10:03 AM

Are there specific softwares for design of transfer lines?? 



#7 Himanshu Sharma

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Posted 07 October 2013 - 12:43 AM

PKS,

 

Well i am not aware of any software for transfer line sizing,we generally combine simulation(Pro-II) and Hydraulics softwares(In-house) for this sizing,needless to say Engineering acumen governs all !

 

Regards

Himanshu



#8 AzoTik1985

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Posted 10 October 2013 - 12:24 AM

I use Pro/II+Pipephase.



#9 Guest_Gerardo Villamizar P._*

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Posted 08 January 2014 - 02:40 PM

The one software you should use is a process simulator such as pro ii or hysys. Never, never you should use a std line sizing software since you have to develope these calculations using difference finite methods which is very easy to do through a process simulator. Some other procedures and concepts were correctly given in the above replies.

All the best.

Gerardo Villamizar
Gvillamizar@tipiel.com.co




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