Zobrazeno 1 - 4
of 4
pro vyhledávání: '"B Zeljko Grbavcic"'
Publikováno v:
Journal of the Serbian Chemical Society
Journal of the Serbian Chemical Society, Vol 70, Iss 11, Pp 1373-1379 (2005)
Journal of the Serbian Chemical Society, Vol 70, Iss 11, Pp 1373-1379 (2005)
The mass transfer coefficient between fluid and an immersed sphere in liquid packed and fluidized beds of inert spherical particles have been studied experimentally using a column 40 mm in diameter. The mass transfer data were obtained by studying th
Publikováno v:
Hemijska Industrija, Vol 58, Iss 2, Pp 69-72 (2004)
Hemijska industrija
Hemijska industrija
Mass transfer in fluidized beds is an important operation for separation processes. Two effects can be achieved by using fluidized beds in mass transfer processes increasing interface area and relative movement between the phases. These effects are b
Autor:
M Jovan Jovanovic, B Mica Jovanovic, B Zeljko Grbavcic, Z Dimitrije Stevanovic, A Marina Mihajlovic
Publikováno v:
Hemijska industrija
Hemijska industrija (2014) 68(5):547-558
Hemijska Industrija, Vol 68, Iss 5, Pp 547-558 (2014)
Hemijska industrija (2014) 68(5):547-558
Hemijska Industrija, Vol 68, Iss 5, Pp 547-558 (2014)
Software for chemical processes modeling and simulation, in the past few decades, plays an important role in the development of chemical-process industry with its growing capabilities and wide range of application. Usage of process simulators in Serb
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::edca06ac341dd3d29e103812dd84e25c
http://TechnoRep.tmf.bg.ac.rs/handle/123456789/2640
http://TechnoRep.tmf.bg.ac.rs/handle/123456789/2640
Autor:
B Zeljko Grbavcic, R Darko Jacimovski, M Mihal Djuris, V Radmila Garic-Grulovic, M Nevenka Boskovic-Vragolovic
Publikováno v:
Hemijska industrija (2014) 68(1):15-25
Hemijska industrija
Hemijska Industrija, Vol 68, Iss 1, Pp 15-25 (2014)
Hemijska industrija
Hemijska Industrija, Vol 68, Iss 1, Pp 15-25 (2014)
Wall-to-bed momentum, heat and mass transfer in the vertical liquid-solids flow, as well as in the single phase flow, were studied. The aim of this investigation was to establish the analogy among those phenomena. Also, effect of particle concentrati