Zobrazeno 1 - 10
of 39
pro vyhledávání: '"M. Nikačević"'
Publikováno v:
Catalysis Today
In this study we investigate performance characteristics (catalyst effectiveness, CH4 selectivity, and hydrocarbon product distribution) of with a highly active Co/Re/Al2O3 catalyst particle for Fischer-Tropsch synthesis. In numerical simulations we
Publikováno v:
Chemical Industry and Chemical Engineering Quarterly, Vol 13, Iss 3, Pp 151-162 (2007)
n/a
Externí odkaz:
https://doaj.org/article/b990dec681614af186c0c44d6a857271
Publikováno v:
Chemical Industry and Chemical Engineering Quarterly, Vol 25, Iss 1, Pp 67-76 (2019)
Chemical Industry & Chemical Engineering Quarterly
Chemical Industry & Chemical Engineering Quarterly
Predictions of vapor liquid equilibrium for Fischer-Tropsch mixtures were compared using the classical Soave-Redlich-Kwong (SRK) and cubic-plus-association (CPA) equations of state. The performance of the two equations of state was evaluated based on
Autor:
Dragomir B. Bukur, Branislav Todic, Vladimir Dikić, Miloš Mandić, Menka Petkovska, Nikola M. Nikačević
Publikováno v:
Chemical Engineering Science
Dynamic performance of a milli-scale fixed bed reactor for Fischer-Tropsch synthesis (FTS) was studied using a dynamic pseudo-homogeneous 1D reactor model. The model uses detailed kinetics to describe the rates of FTS product formation. Dynamic respo
3D model of a Monolithic Honeycomb Adsorber for Electric Swing Adsorption for Carbon Dioxide Capture
Publikováno v:
JOURNAL OF ENGINEERING & PROCESSING MANAGEMENT. 12
The goal of this work was to develop a 3D model of Electric Swing Adsorption pro- cess for carbon dioxide capture from effluent gasses from power plants. Detailed 3D model of the composite honeycomb monolithic adsorber was developed for a sin- gle mo
Publikováno v:
Chemical Engineering Science
In this feasibility study, a novel industrial-scale reactor structure for continuous hydrogen production via intensified water-gas shift (WGS) reaction is proposed. It considers both trickling calcium-oxide sorbent for carbon dioxide removal (SOR) an
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::d0ec3a6456236b74c8e4d85791afefbd
http://TechnoRep.tmf.bg.ac.rs/handle/123456789/4341
http://TechnoRep.tmf.bg.ac.rs/handle/123456789/4341
Publikováno v:
Catalysis Today
One-dimensional pseudo-homogenous dynamic reactor model, incorporating detailed Fischer-Tropsch kinetics, was applied in a theoretical analysis of forced periodic operations. A milli-scale fixed-bed reactor was analyzed, using design and operation pa
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::2387607169aa71e075121e75ac65667e
http://TechnoRep.tmf.bg.ac.rs/handle/123456789/4453
http://TechnoRep.tmf.bg.ac.rs/handle/123456789/4453
Autor:
Branislav Todic, Nikola M. Nikačević, Miloš Mandić, Dragomir B. Bukur, Marko Stamenic, Vladimir Dikić
Publikováno v:
Industrial & Engineering Chemistry Research
Our previously developed mathematical model is used for parametric sensitivity and optimization study of conventional and milliscale fixed-bed reactors (FBRs) for Fischer-Tropsch synthesis (FTS). Five indicators are chosen to analyze the influence of
Autor:
Branislav Todic, Wenping Ma, Gary Jacobs, Nikola M. Nikačević, Dragomir B. Bukur, Burtron H. Davis
Publikováno v:
International Journal of Chemical Kinetics. 49:859-874
A detailed kinetic model of Fischer–Tropsch synthesis (FTS) product formation, including secondary methane formation and 1-olefin hydrogenation, has been developed. Methane formation in FTS over the cobalt-based catalyst is well known to be higher-
Publikováno v:
Journal of Chemical Technology & Biotechnology. 92:2178-2188
BACKGROUND Oscillatory baffled reactors have good prospect for use in batch to continuous transition for many industries. For reliable design and scale up it is essential to mathematically describe mixing and flow pattern of oscillatory flow. The aim