Zobrazeno 1 - 10
of 16
pro vyhledávání: '"Rouzbeh Jafari"'
Publikováno v:
International Journal of Chemical Engineering, Vol 2012 (2012)
The successful design and operation of Liquid-Solid (LS) and Gas-Liquid-Solid (GLS) stirred tank reactors requires an accurate determination of the level of solid suspension needed for the process at hand. A poor design of the stirred tank to achieve
Externí odkaz:
https://doaj.org/article/9ea4c4c4eb6e4c1ba9253dd611dfd7b0
Publikováno v:
The Canadian Journal of Chemical Engineering. 101:160-171
Autor:
Rayane Hoballah, Bruno Blais, Alireza Shams, Priiyank Maheshwari, Rouzbeh Jafari, Jamal Chaouki, Roshanak Rabiee, Shahab Golshan
Publikováno v:
Industrial & Engineering Chemistry Research. 60:8888-8900
In this research, the volume of fluid (VOF) method is used to study the hydrodynamics of rotating packed beds (RPBs). The model is validated, and grid independence analyses are performed for cases with different operating conditions. The droplet size
Autor:
Roshanak Rabiee, Mohammad Monzavi, Jaber Shabanian, Alireza Shams, Shahab Golshan, Rouzbeh Jafari, Bruno Blais, Jamal Chaouki
Publikováno v:
Chemical Engineering Science. 253:117589
Autor:
Xi Gao, Jamal Chaouki, Naoko Ellis, John R. Grace, Tingwen Li, Liqiang Lu, Yupeng Xu, Rouzbeh Jafari, Jonathan Seville, Sina Tebianian, David J. Parker, Thomas Leadbeater
Publikováno v:
Chemical Engineering Science
Chemical Engineering Science, Elsevier, 2020, 217, pp.115501. ⟨10.1016/j.ces.2020.115501⟩
Chemical Engineering Science, Elsevier, 2020, 217, pp.115501. ⟨10.1016/j.ces.2020.115501⟩
International audience; The spatial distribution of solid particles is a key factor affecting the performance of fluidized bed reactors. Non-invasive techniques including radioactive particle tracking (RPT) and positron emission particle tracking (PE
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::70541a95a8b749067e5c7a29cefbd0a3
https://hal-ifp.archives-ouvertes.fr/hal-02913066
https://hal-ifp.archives-ouvertes.fr/hal-02913066
Autor:
Jamal Chaouki, Pablo García-Triñanes, Naoko Ellis, John R. Grace, Jonathan Seville, Sina Tebianian, Roy Hays, David J. Parker, Ray Cocco, S.B. Reddy Karri, Thomas Leadbeater, Rouzbeh Jafari, Kristian L. Dubrawski
Publikováno v:
Chemical Engineering Journal. 306:306-321
A transportable fluidization column, operating under identical conditions at three different locations, was employed to compare three experimental solids flux measurement techniques for hydrodynamic characterization of gas-fluidized beds. This paper
Autor:
Sina Tebianian, Ray Cocco, Rouzbeh Jafari, David J. Parker, Thomas Leadbeater, Jonathan Seville, John R. Grace, Jamal Chaouki, S.B. Reddy Karri, Pablo García-Triñanes, Roy Hays, Kristian L. Dubrawski, Naoko Ellis
Publikováno v:
Powder Technology. 296:45-52
The novel “travelling fluidized bed” (TFB), operated under identical conditions, was deployed to compare alternate experimental measurement techniques for the investigation of solid motion in gas-fluidized beds operating in the square-nosed slugg
Autor:
Ray Cocco, John R. Grace, Roy Hays, S.B. Reddy Karri, Rouzbeh Jafari, Kristian L. Dubrawski, Sina Tebianian, Jonathan Seville, David J. Parker, Thomas Leadbeater, Pablo García-Triñanes, Naoko Ellis, Jamal Chaouki
Publikováno v:
Chemical Engineering Science. 127:310-322
The novel traveling fluidization column, designed and built to assure identical operating conditions, was deployed to compare alternate experimental measurement techniques for hydrodynamic characterization of gas-fluidized beds. This paper compares m
Autor:
Apostolos Kantzas, Kristian L. Dubrawski, C.J. Lim, Jamal Chaouki, Sina Tebianian, Rouzbeh Jafari, M.Z. Qi, Jesse Zhu, Naoko Ellis, Todd Pugsley, R. Gerspacher, John R. Grace, Hsiaotao T. Bi, Gregory S. Patience
Publikováno v:
Powder Technology. 235:203-220
This paper compares invasive and non-invasive voidage measurement techniques from five different Canadian laboratories for the determination of local voidage profiles in gas-fluidized beds of 104 μm Fluid Cracking Catalyst (FCC) and 332 μm silica s