Zobrazeno 1 - 10
of 15
pro vyhledávání: '"Mogahid Osman"'
Publikováno v:
Advances in Applied Energy, Vol 4, Iss , Pp 100069- (2021)
This study investigates the potential of applying pressurized chemical looping reforming (CLR) mechanism for syngas to methanol production process combining of experimental demonstration of methane reforming to syngas and simulation for integration i
Externí odkaz:
https://doaj.org/article/a15e3981d00d48dbb86e3900c5ff0851
Publikováno v:
Energy & Fuels
This further investigates the concept of gas switching dry reforming (GSDR) that efficiently converts the two major greenhouse gases (CO2 and CH4) into a valuable product (syngas) for gas-to-liquid (GTL) syntheses. The proposed GSDR is based on chemi
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::17cdc4096ac471eec1f8c3cca143dcec
https://pubmed.ncbi.nlm.nih.gov/36091477
https://pubmed.ncbi.nlm.nih.gov/36091477
Publikováno v:
Advances in Applied Energy, Vol 4, Iss, Pp 100069-(2021)
This study investigates the potential of applying pressurized chemical looping reforming (CLR) mechanism for syngas to methanol production process combining of experimental demonstration of methane reforming to syngas and simulation for integration i
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::c767c9b4e09492a3920639d77c5e4ecf
http://www.sciencedirect.com/science/article/pii/S2666792421000615
http://www.sciencedirect.com/science/article/pii/S2666792421000615
Publikováno v:
Fuel processing technology
Chemical looping has great potential for reducing the energy penalty and associated costs of CO2 capture from fossil fuel-based power and chemical production while maintaining high efficiency. However, pressurized operation is a prerequisite for maxi
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::67e597cd29e64a48d2e4b5d837268adf
https://hdl.handle.net/11250/2755516
https://hdl.handle.net/11250/2755516
Publikováno v:
Chemical Engineering Journal
This study presents an experimental demonstration of pressurized chemical looping combustion (CLC) in an internally circulating reactor (ICR). The ICR concept is a novel alternative to the conventional interconnected fluidized bed CLC configuration a
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::43f03dabe0eab4bd940507f4158b012e
https://hdl.handle.net/11250/2727741
https://hdl.handle.net/11250/2727741
Autor:
Mercedes Boronat, Vicente J. Margarit, Avelino Corma, Mogahid Osman, Sulaiman S. Al-Khattaf, Cristina Martínez
Publikováno v:
Digital.CSIC. Repositorio Institucional del CSIC
instname
ACS Catalysis
RiuNet. Repositorio Institucional de la Universitat Politécnica de Valéncia
instname
ACS Catalysis
RiuNet. Repositorio Institucional de la Universitat Politécnica de Valéncia
[EN] Transalkylation of alkylaromatics catalyzed by acid zeolites is a process widely employed in the petrochemical industry for upgrading aromatic fractions. The reaction mechanism is complex as it can proceed either by intermolecular alkyl-transfer
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::a28ecec4cfc48cc35902041a355aeeae
http://hdl.handle.net/10261/202662
http://hdl.handle.net/10261/202662
Publikováno v:
Journal of the Taiwan Institute of Chemical Engineers. 61:106-116
The present study deals with oxidative dehydrogenation (ODH) of ethane to ethylene in absence of gas phase oxygen using VO x -Nb/La-γAl 2 O 3 catalysts. In catalyst formulation, La is used to modify γ-Al 2 O 3 , stabilizing its bulk phase transform
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::a40832277f8a9c7173efcc35adb2193f
https://doi.org/10.1016/j.jtice.2016.01.003
https://doi.org/10.1016/j.jtice.2016.01.003
Autor:
Babatunde A. Ogunbadejo, Sulaiman S. Al-Khattaf, Abdullah M. Aitani, Palani Arudra, Mogahid Osman
Publikováno v:
Catalysis Today. 243:109-117
The production of para -ethyltoluene ( p -ET) from the alkylation of toluene with ethanol was investigated over three MFI zeolites with varying SiO 2 /Al 2 O 3 ratio (80, 280, and 2000). The ethylation reaction was conducted in a batch fluidized-bed
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::2ac91c5d67a6e3888c1821527ec017dc
https://doi.org/10.1016/j.cattod.2014.08.019
https://doi.org/10.1016/j.cattod.2014.08.019
Publikováno v:
Journal of Industrial and Engineering Chemistry. 21:1077-1088
Transalkylation of toluene–tetramethylbenzene (TeMB) over MOR and BEA was investigated at 250–400 °C. Conversion of TeMB was higher than trimethylbenzene (TMB) and toluene. Xylene yield was in the following order: toluene − TMB − TeMB > tolu
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::020bc8cf0e7f8e83c69eb19801e3932d
https://doi.org/10.1016/j.jiec.2014.05.018
https://doi.org/10.1016/j.jiec.2014.05.018
Publikováno v:
International Journal of Chemical Reactor Engineering. 12:487-496
This communication reports the kinetics analysis of ethylation of ethylbenzene (EB) with ethanol over large pore size mordenite catalysts. In this regard, two different catalyst samples are selected with SiO2/Al2O3 = 180 and 21, respectively. The hig
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::c6c3da07f9a8f0d02164e52925ecab6b
https://doi.org/10.1515/ijcre-2014-0006
https://doi.org/10.1515/ijcre-2014-0006