Volumetric mass transfer coefficient, power input and gas hold-up in viscous liquid in mechanically agitated fermenters. Measurements and scale-up

Kód výsledku v IS VaVaI

<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F60461373%3A22340%2F18%3A43916338" target="_blank" >RIV/60461373:22340/18:43916338 - isvavai.cz</a>

Výsledek na webu

<a href="https://www.sciencedirect.com/science/article/pii/S0017931018302175?via%3Dihub" target="_blank" >https://www.sciencedirect.com/science/article/pii/S0017931018302175?via%3Dihub</a>

DOI - Digital Object Identifier

<a href="http://dx.doi.org/10.1016/j.ijheatmasstransfer.2018.04.045" target="_blank" >10.1016/j.ijheatmasstransfer.2018.04.045</a>

Jazyk výsledku

angličtina

Název v původním jazyce

Volumetric mass transfer coefficient, power input and gas hold-up in viscous liquid in mechanically agitated fermenters. Measurements and scale-up

Popis výsledku v původním jazyce

Transport characteristics such as volumetric mass transfer coefficients, k(L)a, power input, P and gas holdup, epsilon(G), are the key parameters in the design of mechanically agitated gas-liquid contactors. For their successful design, values of the key parameters can be estimated using empirical correlations. The goal of this work is to complete a complex study to investigate the behavior of k(L)a, P and epsilon(G) in multiple-impeller vessels in non-coalescent viscous batch. We used the dynamic pressure method (DPM). The experiments were conducted in multiple-impeller vessels of both laboratory and pilot-plant scale, which enabled the scale-up studies. Several impeller types with different diameters and their combinations on a common shaft were used in the vessel, under various impeller tip speeds and gassing rates. For all impeller combinations, the gassed and ungassed power consumption, gas hold-up and volumetric - mass transfer coefficient were measured in viscous batch. The measured transport characteristics were summarized into correlations. Several literature correlations were judged, using these extensive datasets. In addition to this, new correlation shapes were also established. The correlation given by and p(g)/V-L = K-1(p(v/)V(L))(K2) vs(K3) gave fairly good prediction of the impeller power. The correlation of this shape can also be employed to calculate the power dissipated in the bottom and upper stages of the multiple-impeller vessel. Correlation epsilon(G) = K-1 (p(g)/V-L)(K2) vs(K3), based on the theory of isotropic turbulence was shown to be reliable for various impeller types. For non-coalescent viscous batch, it is worth using correlation based on power dissipation k(L)a = K-1(p(TOT))(K2) v(s)(K3) ilp This correlation shape can be used to predict transport characteristics in industrial scale vessels under a wide range of operational conditions. (C) 2018 Elsevier Ltd. All rights reserved.

Název v anglickém jazyce

Volumetric mass transfer coefficient, power input and gas hold-up in viscous liquid in mechanically agitated fermenters. Measurements and scale-up

Popis výsledku anglicky

Transport characteristics such as volumetric mass transfer coefficients, k(L)a, power input, P and gas holdup, epsilon(G), are the key parameters in the design of mechanically agitated gas-liquid contactors. For their successful design, values of the key parameters can be estimated using empirical correlations. The goal of this work is to complete a complex study to investigate the behavior of k(L)a, P and epsilon(G) in multiple-impeller vessels in non-coalescent viscous batch. We used the dynamic pressure method (DPM). The experiments were conducted in multiple-impeller vessels of both laboratory and pilot-plant scale, which enabled the scale-up studies. Several impeller types with different diameters and their combinations on a common shaft were used in the vessel, under various impeller tip speeds and gassing rates. For all impeller combinations, the gassed and ungassed power consumption, gas hold-up and volumetric - mass transfer coefficient were measured in viscous batch. The measured transport characteristics were summarized into correlations. Several literature correlations were judged, using these extensive datasets. In addition to this, new correlation shapes were also established. The correlation given by and p(g)/V-L = K-1(p(v/)V(L))(K2) vs(K3) gave fairly good prediction of the impeller power. The correlation of this shape can also be employed to calculate the power dissipated in the bottom and upper stages of the multiple-impeller vessel. Correlation epsilon(G) = K-1 (p(g)/V-L)(K2) vs(K3), based on the theory of isotropic turbulence was shown to be reliable for various impeller types. For non-coalescent viscous batch, it is worth using correlation based on power dissipation k(L)a = K-1(p(TOT))(K2) v(s)(K3) ilp This correlation shape can be used to predict transport characteristics in industrial scale vessels under a wide range of operational conditions. (C) 2018 Elsevier Ltd. All rights reserved.

Druh

J_imp - Článek v periodiku v databázi Web of Science

CEP obor

—

OECD FORD obor

20401 - Chemical engineering (plants, products)

Projekt

<a href="/cs/project/GA15-21715S" target="_blank" >GA15-21715S: Experimentální studie přenosu hmoty kapalina-plyn za přítomnosti pevných částis a ve viskózní vsádce</a><br>

Návaznosti

P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)

Rok uplatnění

2018

Kód důvěrnosti údajů

S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Název periodika

International Journal Heat Mass Transfer

ISSN

0017-9310

e-ISSN

—

Svazek periodika

124

Číslo periodika v rámci svazku

24 April

Stát vydavatele periodika

GB - Spojené království Velké Británie a Severního Irska

Počet stran výsledku

19

Strana od-do

1117-1135

Kód UT WoS článku

000437077100097

EID výsledku v databázi Scopus

2-s2.0-85045556485