Optimal oxygen feeding policy to maximize the production of Maleic anhydride in unsteady state fixed bed catalytic reactors

The effect of different oxygen feeding scenarios in a fixed bed reactor for the production of Maleic anhydride (MA) is studied. Two reactor configurations were examined. In the first configuration, a cross flow reactor (CFR) with 4 discrete feeding points is considered. Another configuration is the...

Full description

Bibliographic Details
Main Authors: E. Ali, M. Al-haj Ali, K. Alhumaizi, M. Elharbawi
Format: Article
Language:English
Published: Elsevier 2017-07-01
Series:Journal of King Saud University: Engineering Sciences
Subjects:
Online Access:http://www.sciencedirect.com/science/article/pii/S1018363915000367
id doaj-4ca99cb593d74e2889518f586558698c
record_format Article
spelling doaj-4ca99cb593d74e2889518f586558698c2020-11-24T22:50:22ZengElsevierJournal of King Saud University: Engineering Sciences1018-36392017-07-0129320421110.1016/j.jksues.2015.12.001Optimal oxygen feeding policy to maximize the production of Maleic anhydride in unsteady state fixed bed catalytic reactorsE. AliM. Al-haj AliK. AlhumaiziM. ElharbawiThe effect of different oxygen feeding scenarios in a fixed bed reactor for the production of Maleic anhydride (MA) is studied. Two reactor configurations were examined. In the first configuration, a cross flow reactor (CFR) with 4 discrete feeding points is considered. Another configuration is the conventional packed-bed reactor (PBR) with a single feed. Nonlinear Model Predictive Controller (NLMPC) was used as optimal controller to operate the CFR in dynamic mode and to optimize the multiple feed dosages in order to enhance the MA yield. The simulation results indicated that different combinations of the four feed ratios can operate the reactor at the best value for the yield provided the first feeding point is kept as low as possible. For the packed bed reactor configuration, a single oxygen feed is considered and is optimized transiently by NLMPC. The simulation outcomes showed that the reactor performance in terms of the produced MA mole fraction can also be enhanced to the same magnitude obtained by CFR configuration. This improvement requires decreasing the oxygen ratio in the reactor single feed by 70%.http://www.sciencedirect.com/science/article/pii/S1018363915000367Maleic anhydrideCross flow reactorFeed stagingForced periodic feedYield
collection DOAJ
language English
format Article
sources DOAJ
author E. Ali
M. Al-haj Ali
K. Alhumaizi
M. Elharbawi
spellingShingle E. Ali
M. Al-haj Ali
K. Alhumaizi
M. Elharbawi
Optimal oxygen feeding policy to maximize the production of Maleic anhydride in unsteady state fixed bed catalytic reactors
Journal of King Saud University: Engineering Sciences
Maleic anhydride
Cross flow reactor
Feed staging
Forced periodic feed
Yield
author_facet E. Ali
M. Al-haj Ali
K. Alhumaizi
M. Elharbawi
author_sort E. Ali
title Optimal oxygen feeding policy to maximize the production of Maleic anhydride in unsteady state fixed bed catalytic reactors
title_short Optimal oxygen feeding policy to maximize the production of Maleic anhydride in unsteady state fixed bed catalytic reactors
title_full Optimal oxygen feeding policy to maximize the production of Maleic anhydride in unsteady state fixed bed catalytic reactors
title_fullStr Optimal oxygen feeding policy to maximize the production of Maleic anhydride in unsteady state fixed bed catalytic reactors
title_full_unstemmed Optimal oxygen feeding policy to maximize the production of Maleic anhydride in unsteady state fixed bed catalytic reactors
title_sort optimal oxygen feeding policy to maximize the production of maleic anhydride in unsteady state fixed bed catalytic reactors
publisher Elsevier
series Journal of King Saud University: Engineering Sciences
issn 1018-3639
publishDate 2017-07-01
description The effect of different oxygen feeding scenarios in a fixed bed reactor for the production of Maleic anhydride (MA) is studied. Two reactor configurations were examined. In the first configuration, a cross flow reactor (CFR) with 4 discrete feeding points is considered. Another configuration is the conventional packed-bed reactor (PBR) with a single feed. Nonlinear Model Predictive Controller (NLMPC) was used as optimal controller to operate the CFR in dynamic mode and to optimize the multiple feed dosages in order to enhance the MA yield. The simulation results indicated that different combinations of the four feed ratios can operate the reactor at the best value for the yield provided the first feeding point is kept as low as possible. For the packed bed reactor configuration, a single oxygen feed is considered and is optimized transiently by NLMPC. The simulation outcomes showed that the reactor performance in terms of the produced MA mole fraction can also be enhanced to the same magnitude obtained by CFR configuration. This improvement requires decreasing the oxygen ratio in the reactor single feed by 70%.
topic Maleic anhydride
Cross flow reactor
Feed staging
Forced periodic feed
Yield
url http://www.sciencedirect.com/science/article/pii/S1018363915000367
work_keys_str_mv AT eali optimaloxygenfeedingpolicytomaximizetheproductionofmaleicanhydrideinunsteadystatefixedbedcatalyticreactors
AT malhajali optimaloxygenfeedingpolicytomaximizetheproductionofmaleicanhydrideinunsteadystatefixedbedcatalyticreactors
AT kalhumaizi optimaloxygenfeedingpolicytomaximizetheproductionofmaleicanhydrideinunsteadystatefixedbedcatalyticreactors
AT melharbawi optimaloxygenfeedingpolicytomaximizetheproductionofmaleicanhydrideinunsteadystatefixedbedcatalyticreactors
_version_ 1725672752920133632