The paper presents the results of testing of immobilized brewers yeast cells kilning in fluidized bed, under various temperature and air flow conditions. Yeast immobilization was carried out by method of cell retention inside the matrix of Ca-alginate support. Kilning was done by compressor air, at the temperatures t=30, 40, 50 and 60° С and at air flow rate of 3.14 m/s, during 90 minutes. Humidity of the kilned particles was within the interval of 0.1-0.2 kg/ kg, while water activity was within the range of 0.28 (t=60° C) to 0.45 (t=30° C). This level of water activity in the kilned samples prevented any biological activity and secured conservation of im- mobilized starters. Testing of the kilned particles rehydration process showed that t...
The fluidized bed reactor has successfully been used to perform biotechnological processes addressed...
Alumina channeled beads and rough surface membranes prepared from aqueous sols of fibrillar pseudobo...
An extremely important condition for successful performances of continuous fermentation in reactor s...
Brewery yeast cells immobilized in Ca-alginate were dried in a laboratory scale spouted bed with a d...
In recent years, much attention has been paid to the technique for the immobilization of micro-organ...
Suhi pekarski kvasac suspendiran je u otopini Na-alginata i imobiliziran dokapavanjem u ...
Dried microorganisms used as startercultures become more and more important for food processing and ...
The aim of this work was to study the physiological changes of immobilized brewing yeast Saccharomy...
Immobilization techniques applied in beer production must secure overcoming of diffusion limitations...
Dried microorganism used as startercultures become more and more important for food processing and a...
In this thesis, the modelling and operation of the fermentation of glucose to ethanol using Saccharo...
For the production of dried starter cultures the conditions for thermal drying have to be controlled...
A phase-field model was formulated to describe yeast cell growth within the Ca-alginate microbead du...
Immobilized cell technology (ICT) has been attracting continual attention in the brewing industry ov...
Submitted by Johnny Rodrigues (johnnyrodrigues@ufcg.edu.br) on 2018-10-17T16:51:04Z No. of bitstream...
The fluidized bed reactor has successfully been used to perform biotechnological processes addressed...
Alumina channeled beads and rough surface membranes prepared from aqueous sols of fibrillar pseudobo...
An extremely important condition for successful performances of continuous fermentation in reactor s...
Brewery yeast cells immobilized in Ca-alginate were dried in a laboratory scale spouted bed with a d...
In recent years, much attention has been paid to the technique for the immobilization of micro-organ...
Suhi pekarski kvasac suspendiran je u otopini Na-alginata i imobiliziran dokapavanjem u ...
Dried microorganisms used as startercultures become more and more important for food processing and ...
The aim of this work was to study the physiological changes of immobilized brewing yeast Saccharomy...
Immobilization techniques applied in beer production must secure overcoming of diffusion limitations...
Dried microorganism used as startercultures become more and more important for food processing and a...
In this thesis, the modelling and operation of the fermentation of glucose to ethanol using Saccharo...
For the production of dried starter cultures the conditions for thermal drying have to be controlled...
A phase-field model was formulated to describe yeast cell growth within the Ca-alginate microbead du...
Immobilized cell technology (ICT) has been attracting continual attention in the brewing industry ov...
Submitted by Johnny Rodrigues (johnnyrodrigues@ufcg.edu.br) on 2018-10-17T16:51:04Z No. of bitstream...
The fluidized bed reactor has successfully been used to perform biotechnological processes addressed...
Alumina channeled beads and rough surface membranes prepared from aqueous sols of fibrillar pseudobo...
An extremely important condition for successful performances of continuous fermentation in reactor s...