Numerical Analysis of Particle Uneven Distribution at Riser and Deposit Phenomenon at Cyclone in RFCC Reactor

One of the main problems associated with reactors in commercial Residue Fluidized Catalytic Cracking (RFCC) process in refinery plant is that each of six outlets of the riser has different particle mass flow rates. This phenomenon causes particle uneven distribution and catalyst loss. High conversio...

Full description

Bibliographic Details
Main Authors: H. Cho, B. Cha, S. Kim, J. Ryu, J. Kim, I. Moon
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2015-05-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/5001
id doaj-281328571a9f41119bc76b1557aed415
record_format Article
spelling doaj-281328571a9f41119bc76b1557aed4152021-02-20T21:11:46ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162015-05-014310.3303/CET1543234Numerical Analysis of Particle Uneven Distribution at Riser and Deposit Phenomenon at Cyclone in RFCC ReactorH. ChoB. ChaS. KimJ. RyuJ. KimI. MoonOne of the main problems associated with reactors in commercial Residue Fluidized Catalytic Cracking (RFCC) process in refinery plant is that each of six outlets of the riser has different particle mass flow rates. This phenomenon causes particle uneven distribution and catalyst loss. High conversion of cracking reaction requires uniform catalyst distribution in the riser. The riser termination device (RTD) is installed to reduce product gas residence time and achieve rapid separation between catalysts and product gas. RTD is made up of six close-coupled cyclone sets at the top of riser. Also, particle deposit formation in the cyclone duct has caused shutdown problems as well as a decrease of the cyclone efficiency. This study analyzes flow pattern of catalyst particles in the riser and the cyclone. Moreover, particle mass flow rates are investigated at each outlet by the number of feed injector. The cracking reaction is taken into account in the simulation scheme and its conversion is evaluated in the riser by employing multiphase-particle in cell (MP-PIC) method, one of computational particle fluid dynamics (CPFD) methodologies. It applies both a stochastic particle model and Lagrangian method for particle phase, and Eulerian method for fluid phase, respectively. Mass flow rates at the outlets of riser are different from each outlet from 107.8 kg/s to 144.1 kg/s, which means solid loading ratio for certain cyclones increased. The solid loading ratio affects the cyclone separation efficiency. As a result, particle uneven distribution flow was identified. Standard deviations of particle mass flow rate at the 4-injector riser case and 6-injector riser case represent respectively 11.3 and 8.8. So, this article suggests that particle uneven distribution will be alleviated by using 6-injector riser than 4-injector riser.https://www.cetjournal.it/index.php/cet/article/view/5001
collection DOAJ
language English
format Article
sources DOAJ
author H. Cho
B. Cha
S. Kim
J. Ryu
J. Kim
I. Moon
spellingShingle H. Cho
B. Cha
S. Kim
J. Ryu
J. Kim
I. Moon
Numerical Analysis of Particle Uneven Distribution at Riser and Deposit Phenomenon at Cyclone in RFCC Reactor
Chemical Engineering Transactions
author_facet H. Cho
B. Cha
S. Kim
J. Ryu
J. Kim
I. Moon
author_sort H. Cho
title Numerical Analysis of Particle Uneven Distribution at Riser and Deposit Phenomenon at Cyclone in RFCC Reactor
title_short Numerical Analysis of Particle Uneven Distribution at Riser and Deposit Phenomenon at Cyclone in RFCC Reactor
title_full Numerical Analysis of Particle Uneven Distribution at Riser and Deposit Phenomenon at Cyclone in RFCC Reactor
title_fullStr Numerical Analysis of Particle Uneven Distribution at Riser and Deposit Phenomenon at Cyclone in RFCC Reactor
title_full_unstemmed Numerical Analysis of Particle Uneven Distribution at Riser and Deposit Phenomenon at Cyclone in RFCC Reactor
title_sort numerical analysis of particle uneven distribution at riser and deposit phenomenon at cyclone in rfcc reactor
publisher AIDIC Servizi S.r.l.
series Chemical Engineering Transactions
issn 2283-9216
publishDate 2015-05-01
description One of the main problems associated with reactors in commercial Residue Fluidized Catalytic Cracking (RFCC) process in refinery plant is that each of six outlets of the riser has different particle mass flow rates. This phenomenon causes particle uneven distribution and catalyst loss. High conversion of cracking reaction requires uniform catalyst distribution in the riser. The riser termination device (RTD) is installed to reduce product gas residence time and achieve rapid separation between catalysts and product gas. RTD is made up of six close-coupled cyclone sets at the top of riser. Also, particle deposit formation in the cyclone duct has caused shutdown problems as well as a decrease of the cyclone efficiency. This study analyzes flow pattern of catalyst particles in the riser and the cyclone. Moreover, particle mass flow rates are investigated at each outlet by the number of feed injector. The cracking reaction is taken into account in the simulation scheme and its conversion is evaluated in the riser by employing multiphase-particle in cell (MP-PIC) method, one of computational particle fluid dynamics (CPFD) methodologies. It applies both a stochastic particle model and Lagrangian method for particle phase, and Eulerian method for fluid phase, respectively. Mass flow rates at the outlets of riser are different from each outlet from 107.8 kg/s to 144.1 kg/s, which means solid loading ratio for certain cyclones increased. The solid loading ratio affects the cyclone separation efficiency. As a result, particle uneven distribution flow was identified. Standard deviations of particle mass flow rate at the 4-injector riser case and 6-injector riser case represent respectively 11.3 and 8.8. So, this article suggests that particle uneven distribution will be alleviated by using 6-injector riser than 4-injector riser.
url https://www.cetjournal.it/index.php/cet/article/view/5001
work_keys_str_mv AT hcho numericalanalysisofparticleunevendistributionatriseranddepositphenomenonatcycloneinrfccreactor
AT bcha numericalanalysisofparticleunevendistributionatriseranddepositphenomenonatcycloneinrfccreactor
AT skim numericalanalysisofparticleunevendistributionatriseranddepositphenomenonatcycloneinrfccreactor
AT jryu numericalanalysisofparticleunevendistributionatriseranddepositphenomenonatcycloneinrfccreactor
AT jkim numericalanalysisofparticleunevendistributionatriseranddepositphenomenonatcycloneinrfccreactor
AT imoon numericalanalysisofparticleunevendistributionatriseranddepositphenomenonatcycloneinrfccreactor
_version_ 1724259284927119360