Hi,
When I calculated the minimum reflux ratio from Mc Cabe Thiele method and Underwood equation, I got negative value. Please suggest how to find optimum reflux ratio in this type of situation.
Thanks,
Ashok
|

4 replies to this topic
Share this topic:
#1
Posted 28 September 2011 - 06:39 AM
#2
Posted 28 September 2011 - 06:57 AM
#3
Posted 28 September 2011 - 07:27 AM
Thank you Breizh.
I used the Underwood equation to calculate minimum reflux ratio for a 3 component mixture [formula taken from Unit operations of chemical engineering, Mc Cabe Smith], but the value of minimum reflux ratio [(L/D)min + 1] is -0.68. Now, Rmin = (L/D)min = -0.68-1 = -1.68. How can I proceed further to calculate value of Rmin..?
I used the Underwood equation to calculate minimum reflux ratio for a 3 component mixture [formula taken from Unit operations of chemical engineering, Mc Cabe Smith], but the value of minimum reflux ratio [(L/D)min + 1] is -0.68. Now, Rmin = (L/D)min = -0.68-1 = -1.68. How can I proceed further to calculate value of Rmin..?
#4
Posted 28 September 2011 - 08:01 AM
Consider this resource from Ludwig .
Hope this helps
Breizh
http://books.google....epage&q&f=false
An other esource is "Distillation design "by Henry Z Kister
Hope this helps
Breizh
http://books.google....epage&q&f=false
An other esource is "Distillation design "by Henry Z Kister
Edited by breizh, 29 September 2011 - 12:32 AM.
#5
Posted 29 September 2011 - 07:50 AM
Thanks Breizh
Similar Topics
Batch Adsorption: H/d Ratio For Vessel SizingStarted by Guest_Victor_process_Engineer_* , 28 Feb 2025 |
|
![]() |
||
Subcooled Reflux And Energy UsageStarted by Guest_jango_* , 20 Dec 2024 |
|
![]() |
||
![]() Ratio Pressure Drops-FlowratesStarted by Guest_panoska_* , 08 Nov 2024 |
|
![]() |
||
![]() How To Use 'choking Pressure Ratio'Started by Guest_Sansan_* , 27 Oct 2024 |
|
![]() |
||
Minimum Vapor Disengagement Area For A Kettle BoilerStarted by Guest_Engib33r_* , 17 Oct 2024 |
|
![]() |