During impact co-polymer production in unipol gas phase two reactors configuration, run lenght is small (30-40 days) as compared to homopolymer production (with one reactor). ICP run is interrupted by inter resin transfer system (IRTS) fouling which restricts resin transfer from reactor-1 to reactor-2. What are the best practices to minimize fouling in Reactor-2 and IRTS.
|

Maximizing Polypropylene Icp Production Run Length
Started by 122, Feb 28 2014 03:35 PM
No replies to this topic
Share this topic:
#1
Posted 28 February 2014 - 03:35 PM
Similar Topics
Design Of A Reactor For Production Of HmfStarted by Guest_Manue_* , 30 Mar 2023 |
|
![]() |
||
How To Design Cstr Reactor For Ethyl Acetate ProductionStarted by Guest_chemtoli_* , 07 Mar 2023 |
|
![]() |
||
Natural Gas Wells Location And Production Volume DataStarted by Guest_ChinmoyBasak_* , 08 Feb 2023 |
|
![]() |
||
![]() Polyester Production Distillation EfficiencyStarted by Guest_Tolgahan_* , 01 Sep 2022 |
|
![]() |
||
![]() Psv Inlet Pipe LengthStarted by Guest_R_Gowtham_* , 13 May 2022 |
|
![]() |