Evaluation of methods of extraction and partial characterization of cell wall carbohydrates of brewer's yeast strain,Saccharomyces cerevisiae

1986 ◽  
Vol 2 (3) ◽  
pp. 383-388 ◽  
Author(s):  
R. Al-Bassam ◽  
W. Al-jumaily ◽  
A. A. Rawi ◽  
F. A. Suffi
2008 ◽  
Vol 99 (7) ◽  
pp. 2107-2115 ◽  
Author(s):  
Manuela D. Machado ◽  
Mónica S.F. Santos ◽  
Cláudia Gouveia ◽  
Helena M.V.M. Soares ◽  
Eduardo V. Soares

1989 ◽  
Vol 9 (6) ◽  
pp. 2536-2543
Author(s):  
J Y Lee ◽  
D R Engelke

Saccharomyces cerevisiae cellular RNase P is composed of both protein and RNA components that are essential for activity. The isolated holoenzyme contains a highly structured RNA of 369 nucleotides that has extensive sequence similarities to the 286-nucleotide RNA associated with Schizosaccharomyces pombe RNase P but bears little resemblance to the analogous RNA sequences in procaryotes or S. cerevisiae mitochondria. Even so, the predicted secondary structure of S. cerevisiae RNA is strikingly similar to the bacterial phylogenetic consensus rather than to previously predicted structures of other eucaryotic RNase P RNAs.


2002 ◽  
Vol 51 (5) ◽  
pp. 323-334 ◽  
Author(s):  
Tomohiko NAKAMURA ◽  
Yoshitaka HITOMI ◽  
Michiko YOSHIDA ◽  
Yoshiharu SHIRASU ◽  
Tomomichi TSUKUI ◽  
...  

Materials ◽  
2020 ◽  
Vol 13 (16) ◽  
pp. 3624 ◽  
Author(s):  
Inga Zinicovscaia ◽  
Nikita Yushin ◽  
Daler Abdusamadzoda ◽  
Dmitrii Grozdov ◽  
Margarita Shvetsova

The performance of the brewer’s yeast Saccharomyces cerevisiae to remove metal ions from four batch systems, namely Zn(II), Zn(II)-Sr(II)-Cu(II), Zn(II)-Ni(II)-Cu(II), and Zn(II)-Sr(II)-Cu(II)-Ba(II), and one real effluent was evaluated. Yeast biosorption capacity under different pH, temperature, initial zinc concentration, and contact time was investigated. The optimal pH for removal of metal ions present in the analyzed solution (Zn, Cu, Ni, Sr, and Ba) varied from 3.0 to 6.0. The biosorption process for zinc ions in all systems obeys Langmuir adsorption isotherm, and, in some cases, the Freundlich model was applicable as well. The kinetics of metal ions biosorption was described by pseudo-first-order, pseudo-second-order, and Elovich models. Thermodynamic calculations showed that metal biosorption was a spontaneous process. The two-stage sequential scheme of zinc ions removal from real effluent by the addition of different dosages of new sorbent allowed us to achieve a high efficiency of Zn(II) ions removal from the effluent. FTIR revealed that OH, C=C, C=O, C–H, C–N, and NH groups were the main biosorption sites for metal ions.


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