Zobrazeno 1 - 10
of 10
pro vyhledávání: '"Libor, Labík"'
Autor:
Alberto Brucato, Francesca Scargiali, Radim Petricříček, Libor Labík, Franco Grisafi, Tomáš Moucha, Giuseppe Caputo
Publikováno v:
Chemical Engineering Research and Design. 132:584-592
The interest in the process industry on unbaffled stirred tanks has greatly expanded in the last years because they may bring about significant advantages in a number of applications, including biochemical, food and pharmaceutical processes where the
Publikováno v:
Chemical Engineering Science. 170:451-463
In the industrial fermentation processes, most liquids are non-coalescent and often exhibit increased viscosity. However, due to the limitations of most measurement methods, there is a lack of reliable data for predicting volumetric mass transfer coe
Publikováno v:
Chemical Engineering & Technology. 40:878-888
Publikováno v:
Chemical Engineering Science. 144:126-134
Our present research re-opens the problem of recalculation of the mass-transfer data between absorption and distillation by performing both processes in devices of the same geometry and using absorption and distillation systems whose physical propert
Unbaffled stirred tanks are increasingly recognized as a viable alternative to common baffled tanks for a range of applications such as biochemical, food or pharmaceutical processes where the presence of baffles is undesirable for some reason. In thi
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::7774e3103698e6b972fbb4fca5a70e9e
http://hdl.handle.net/10447/295104
http://hdl.handle.net/10447/295104
Publikováno v:
Chemical Engineering & Technology. 38:1646-1653
Publikováno v:
Chemical Engineering Journal. 240:55-61
Focused on liquid film-controlled processes in mechanically agitated aerated vessels, an attempt is made to develop scale-up correlations based on isotropic turbulence theory. It is shown that including the impeller tip speed fD (impeller frequency *
Publikováno v:
Biochemical Engineering Journal. 69:17-27
Mechanically agitated gas–liquid contactors are frequently used in the chemical, food and biochemical industries as fermenters and as hydrogenation or chlorination reactors. However wide the usage of such vessels is, their design is not based on ch
Publikováno v:
Chemical Papers. 70
Transport characteristics such as volumetric mass transfer coefficients, kLa, power input, P, gas hold-up, γ, and mixing time, tm, are the key parameters in the design of mechanically agitated gasliquid contactors. For their successful design, value
Publikováno v:
Chemical Papers; Apr2016, Vol. 70 Issue 4, p461-469, 9p