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  • Articles  (28)
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  • yeast
  • 1995-1999  (28)
  • Process Engineering, Biotechnology, Nutrition Technology  (28)
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  • 1
    Electronic Resource
    Electronic Resource
    Springer
    World journal of microbiology and biotechnology 15 (1999), S. 679-681 
    ISSN: 1573-0972
    Keywords: Chloroacetamides ; gene mapping ; herbicide resistance ; yeast
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The herbicide Metolachlor (α-chloroacetamide group) inhibits the growth of Saccharomyces cerevisiae on complete, minimal, and non-fermentative media. Spontaneous and induced resistant mutants showed monogenic segregation patterns. Among the resistant clones, 70% were recessives, 16.4% were partially dominants and 13.4% were dominants. The spontaneous partially dominant mutation Mtc1 was mapped on linkage group XV at 33.3 cM from ade2 and 31.7 cM from his3, in a region that is characterized by the presence of several resistant genes. The recessive mutation mtc2 was located on chromosome IV. Although all the mutants had the ability to grow in the presence of the herbicide, they remained affected in their respiration efficiency, indicating two different mechanism of action of Metholachor on yeast cells.
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  • 2
    Electronic Resource
    Electronic Resource
    Springer
    World journal of microbiology and biotechnology 15 (1999), S. 345-348 
    ISSN: 1573-0972
    Keywords: Filtration ; naturally contaminated samples ; PCR ; sample preparation ; sucrose solutions ; yeast
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract An assay based on PCR was developed for the detection of yeast in naturally contaminated industrial sugar solutions. A number of characterized as well as non-characterized yeast strains, isolated from samples from a sugar refinery, were detected with the PCR assay. Specificity tests showed that the presence of neither bacteria nor mould resulted in false positive results. A concentration step, based on filtration, was employed prior to the PCR detection in order to reach a detection level of 0.1 c.f.u./ml of naturally contaminated sugar solution. The detection method based on PCR was found to be more rapid (〈5 h) and easier to perform than the slower and more labour-intensive, traditional culturing techniques.
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  • 3
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    Electronic Resource
    Springer
    World journal of microbiology and biotechnology 14 (1998), S. 583-585 
    ISSN: 1573-0972
    Keywords: Algae ; bacteria ; chromium resistance ; reduction of chromium ; yeast
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Bacteria, yeasts, protozoa and algae, observed in industrial effluents from tanneries, were checked for their possible use in the detoxification of polluted water. Two bacterial strains were found to be highly resistant to CrVI. Several bacteria, yeasts and algae were observed to be capable of reducing CrVI to CrIII.
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  • 4
    Electronic Resource
    Electronic Resource
    Springer
    World journal of microbiology and biotechnology 14 (1998), S. 809-821 
    ISSN: 1573-0972
    Keywords: Alcohol ; ethanol ; thermophilic ; thermotolerant ; yeast
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract There are a number of process advantages which could be exploited through the use of thermophilic microorganisms for ethanol production. Energy savings through reduced cooling costs, higher saccharification and fermentation rates, continuous ethanol removal and reduced contamination have stimulated a search for routes to thermophilic or thermotolerant yeasts. These routes have included screening existing culture collections, temperature adaptation, mutagenesis and molecular techniques and finally isolating new strains. Varying success has been achieved, however, the most thermotolerant yeasts have come from fresh isolations from environments which experience high temperatures. Thermotolerant yeasts have been investigated for the following potential applications: simultaneous saccharification and fermentation of cellulose, where the high fermentation temperature allows more rapid and efficient enzymatic cellulose hydrolysis; whey fermentation, where high salt and low fermentable substrate concentrations make conditions difficult; and fermentation of D-xylose and cellobiose, which is essential for efficient conversion of woody biomass to ethanol. Ethanol and temperature tolerance are important characteristics for commercial yeast strains. Both characteristics are interactive and generally decrease with increasing temperature and ethanol concentration. Considerable research has been directed towards investigation of fatty acid composition changes in response to these stresses and the role of heat shock proteins in tolerance mechanisms. If thermotolerant yeasts are to be used in commercial processes, bioreactor configuration will play an important part in the design of production processes. Batch and fed-batch systems have been shown to be useful in some circumstances as have continuous flow systems, however, some of the newly isolated thermotolerant yeasts such as Kluyveromyces marxianus do not show the high growth rate under anaerobic conditions that is characteristic of Saccharomyces cerevisiae. Various immobilization techniques appear to offer a means of presenting and maintaining high biomass in anaerobic continuous flow reactors.
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  • 5
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    Springer
    World journal of microbiology and biotechnology 14 (1998), S. 719-725 
    ISSN: 1573-0972
    Keywords: Coulter counter ; mechanical properties ; micromanipulation ; osmotic pressure ; Saccharomyces cerevisiae ; yeast
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract A new micromanipulation technique which has previously been used to measure the mechanical properties of single animal cells has now been applied to yeast cells. In this study this technique was used to measure yeast cell strength and cell size across a 2l batch fermentation. Alternatively the cell size could also be determined using a Coulter counter while cell measurement was diluted with a conducting fluid (Isoton II). For the cell strength, it was found that the osmotic pressure of diluents did affect cell strength. However, it was also found that there was no significant effect of osmotic pressure of diluents on cell size whether a Coulter counter or micromanipulation was used for measurement. Micromanipulation has been shown to be a powerful technique for measuring the mechanical properties of yeast cells and it will be very useful for studying their behaviour in cell disruption equipment, e.g. high-pressure homogenizers.
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  • 6
    Electronic Resource
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 60 (1998), S. 492-497 
    ISSN: 0006-3592
    Keywords: yeast ; inulin ; inulase ; fructose ; secretion ; hexokinases ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The gene encoding inulase of the yeast Kluyveromyces marxianus (INU1Km) was cloned and expressed in the inulin-negative yeast Saccharomyces cerevisiae. Cells of S. cerevisiae transformed with the INU1Km gene have acquired extracellular inulase activity and were able to grow in the medium with inulin as a sole carbon source. The S. cerevisiae strain was constructed that is capable of heterologous expression of secreted K. marxianus inulase and is defective in fructose uptake due to null-mutations of the hexokinase structural genes HXK1 and HXK2. When grown in inulin-containing media, this strain is capable of accumulating at least 10% glucose-free fructose in the culture liquid. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 492-497, 1998.
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  • 7
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 58 (1998), S. 445-450 
    ISSN: 0006-3592
    Keywords: on-line control ; pH control ; growth monitoring ; proton titration ; yeast ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The amount of acid or base consumed in yeast cultures has been recently assigned to the pathway of nitrogen assimilation under respiratory conditions with no contribution by carbon metabolism (Castrillo et al., 1995). In this investigation, experiments under respirofermentative conditions have shown that production or consumption of ethanol does not contribute significantly to the specific rate of proton production (qH+), thus extending the previously obtained relationships for all aerobic conditions in which other major acid/base contributions are not involved. Tests in batch and chemostat culture confirm the validity of qH+ as a formal control parameter in aerobic fermentations. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:445-450, 1998.
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  • 8
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    Biotechnology and Bioengineering 59 (1998), S. 647-650 
    ISSN: 0006-3592
    Keywords: biomass separation ; flocculation ; biomass measurement ; yeast ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We introduce the ratio of nonflocculent versus total biomass as a criterion for starting cell separation from the medium. This criterion can be applied for the automation of the process regardless of the process dynamics. Its minimum indicates the optimum period of time for the start of the separation process with regard not only to nonflocculent cell concentration, but also medium attributes. In contrast to the concentration of nonflocculent cells, which has two minima, first at the beginning of the process and another broader one in the period during which maximum flocculation is present, the ratio has a single minimum and can therefore be implemented as a criterion for cell separation. To calculate the ratio value, in addition to an on-line method for nonflocculent biomass measurement described elsewhere, an on-line method for the total biomass of flocculent yeast is proposed. It is based on the absorbency measurement of the cell biomass, previously deflocculated by EDTA. Therefore, it can be applied in bioprocesses with transparent media and yeast that can be deflocculated by EDTA. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:647-650, 1998.
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  • 9
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 58 (1998), S. 133-138 
    ISSN: 0006-3592
    Keywords: metabolic modeling ; model selection ; parameter estimation ; identification ; yeast ; stoichiometry ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A metabolic network model is one of the cornerstones of the emerging Metabolic Engineering methodology. In this article, special attention is therefore, given to the phase of model building. A five-stage structured approach to metabolic network modeling is introduced. The basic steps are: (1) to collect a priori knowledge on the reaction network and to build candidate network models, (2) to perform an a priori check of the model, (3) to estimate the unknown parameters in the model, (4) to check the identified model for acceptability from a biological and thermodynamic point of view, and (5) to validate the model with new data. The approach is illustrated with a growth system involving baker's yeast growing on mixtures of substrates. Special attention is given to the central uncertainties in metabolic network modeling, i.e., estimation of energetic parameters in the network and the choice of the source of anabolic reducing equivalents NADPH. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:133-138, 1998.
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  • 10
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    Springer
    World journal of microbiology and biotechnology 13 (1997), S. 711-712 
    ISSN: 1573-0972
    Keywords: Endopolygalacturonase ; pectic enzymes ; Saccharomyces cerevisiae ; yeast
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The laboratory strain of S. cerevisiae, IM1-8b, showed pectolytic activity in the presence of either glucose, fructose, or sucrose as the carbon source, but not with galactose. The enzyme activity was rapidly lost with shaking. The optimum pH and temperature for activity were 4.5 and 45°C, respectively. The enzyme was an endopolygalacturonase, since it preferentially hydrolysed pectate over pectin and decreased the viscosity of a 5% polygalacturonic solution by about 30% in 30min producing oligogalacturonic acid and digalacturonic acid as end-products.
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  • 11
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    Biotechnology and Bioengineering 53 (1997), S. 10-16 
    ISSN: 0006-3592
    Keywords: microfiltration ; fouling ; yeast ; antifoam agents ; depressurization ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The fouling effects of yeast fermentation broths of Candida utilis in the presence of various commercial antifoam agents (PPG2000, B5600, and G832) up to 4.0 mL/L were studied, using Millipore polyvinylidene fluoride 0.22-μm hydrophilic membranes (GVWP), in a stirred-cell system at 50 kPa and 700 rpm. PPG2000, which has a low value of work of adhesion (Wa of 0.81 mN/m), gave a steady flux of broth of 29 L/(h m2) and was found to have no significant fouling effect on the microfiltration of broth. G832, which has a high Wa, (26.0 mN/m) reduced the flux of the broth to 17 L/(h m2); i.e., by 42% when only 1.0 mL/L was used. However, B5600, which has a Wa of 14.3 mN/m, was found to enhance the flux of broth to 54 L/(h m2); i.e., by 86%, due to the preferential adsorption of the B5600 components onto the hydrophobic cell contents released. These results were reinforced by the depressurization experiments performed with both hydrophilic (GVWP) and hydrophobic (GVHP) membranes, using both young and aged broths. B5600 was found to be the optimum antifoam agent in this study in terms of membrane performance and defoaming efficiency. © 1997 John Wiley & Sons, Inc.
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  • 12
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 53 (1997), S. 71-78 
    ISSN: 0006-3592
    Keywords: Zymomonas ; yeast ; acetaldehyde ; ethanol ; stress ; inhibition ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The lag phase of Saccharomyces cerevisiae subjected to a step increase in temperature or ethanol concentration was reduced by as much as 60% when acetaldehyde was added to the medium at concentrations less than 0.1 g/L. Maximum specific growth rates were also substantially increased. Even greater proportional reductions in lag time due to acetaldehyde addition were observed for ethanol-shocked cultures of Zymomonas mobilis. Acetaldehyde had no effect on S. cerevisiae cultures started from stationary phase inocula in the absence of environmental shock and its lag-reducing effects were greater in complex medium than in a defined synthetic medium. Acetaldehyde reacted strongly with the ingredients of complex culture media. It is proposed that the effect of added acetaldehyde may be to compensate for the inability of cells to maintain transmembrane acetaldehyde gradients following an environmental shock. © 1997 John Wiley & Sons, Inc.
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  • 13
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    Biotechnology and Bioengineering 53 (1997), S. 470-477 
    ISSN: 0006-3592
    Keywords: fluidized bed bioreactor ; recombinant ; yeast ; kinetics ; modeling ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Continuous production of a recombinant murine granulocyte-macrophage colony-stimulating factor (GM-CSF) by Saccharomyces cerevisiae strain XV2181 (a/a, Trp 1) containing plasmid pαADH2 and immobilized on porous glass beads in a fluidized bed bioreactor was studied. Kinetic models for plasmid stability, cell growth, and protein production in the three-phase fluidized bed bioreactor were developed and used to study the effects of solid loading or cell immobilization on plasmid stability and recombinant protein production. With increasing cell immobilization or solid loading in the bioreactor, plasmid stability and protein production improved significantly. The improvements could be attributed to the decreased θ value, which is the plasmid loss probability during cell division and is an indication of segregational instability of the recombinant cell, and the increased α value, which is the ratio of the specific growth rate of a plasmid-carrying cell to that of a plasmid-free cell and is indicative of competitive stability of the recombinant cell culture. θ decreased from 0.552 to 0.042 and α increased from 0.351 to 0.991 when solid loading in the bioreactor was increased from 5% (v/v) to 33%. The model simulation also showed that the specific growth rate of cells in the bioreactor was lower at higher solid loading. This indicated that there was significant mass transfer limitation, particularly for oxygen transfer, when the total cell density in the bioreactor was high at high solid loading. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 470-477, 1997.
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  • 14
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    Biotechnology and Bioengineering 54 (1997), S. 535-542 
    ISSN: 0006-3592
    Keywords: fermentor monitoring ; mass spectrometer ; Pichia stipitis ; carbon dioxide ; yeast ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An in situ sterilizable plug-in membrane inlet mass spectrometer for monitoring dissolved gases and volatiles in fermentors was constructed and tested. The design ensured a minimal distance to be traveled by analyte molecules from the bulk of the fermentation broth to the ionization chamber of the mass spectrometer. Apart from the specific cross talk due to overlapping mass peaks from different compounds, we found that carbon dioxide interfered unspecifically with all the mass peaks of other substances, changing them by the same factor. The interference changed slowly with time and could be positive or negative depending on the history of the mass spectrometer. Also, the general sensitivity of the instrument changed slowly with time. These effects can be neglected or corrected for empirically in short-term measurements. When the fermentor was aerated with a three-component gas mixture including carbon dioxide, a rapid change in the partial pressure of carbon dioxide in the gas mixture gave rise to a transient in the signal of a gas whose partial pressure was kept constant. This effect revealed a transient change in the composition of the gas mixture in the bubbles caused by net import or export of carbon dioxide during equilibration with the new gas mixture. An experimental method to determine the effective partial pressures of gases in the bubbles during steady-state transport of carbon dioxide was designed. The plug-in membrane inlet mass spectrometer was tried as a probe for oxygen and ethanol in an oxystatic culture of the yeast Pichia stipitis. We found that it was possible to keep a steady-state concentration of as little as 0.5 μM throughout the lifetime of the culture. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 535-542, 1997.
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  • 15
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    Biotechnology and Bioengineering 56 (1997), S. 62-70 
    ISSN: 0006-3592
    Keywords: osmotic shock ; water permeability ; mixing time constant ; mathematical model ; yeast ; leukemia K562 cells ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Water permeability (Lp), calculated from the volume variations of cells subjected to an osmotic shock, is classically used to characterize cell membrane properties. In this work, we have shown the importance of the kind of mixing reactor used to measure the Lp parameter. A mathematical model including the mixing time constant has been proposed allowing an accurate Lp estimation even though the mixing time constant is higher than the cell time constant obtained in response to a perfect shock. The estimated Lp values of human leukemia K562 cells were found to be the same whatever the mixing time constant. The Lp value of Saccharomyces cerevisiae could not be exactly estimated. However, S. cerevisiae has unexpectedly high water permeability, implying that this yeast may contain water channels in the membrane. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 62-70, 1997.
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  • 16
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    Springer
    World journal of microbiology and biotechnology 12 (1996), S. 415-416 
    ISSN: 1573-0972
    Keywords: Ethanol ; fed-batch fermentation ; yeast
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The efficiency of ethanol yield increased from 61% to 88% of the theoretical value as the filling-up time was approached in fed-batch fermentation with Saccharomyces cerevisiae. Temporary accumulation of ethanol within the yeast cells may explain the above variation.
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  • 17
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    Biotechnology and Bioengineering 49 (1996), S. 667-674 
    ISSN: 0006-3592
    Keywords: yeast ; threonine biosynthesis ; gene amplification ; amino acid production ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In this work, we have studied the effect of amplifying different alleles involved in the threonine biosynthesis on the amino acid production by Saccharomyces cerevisiae. The genes used were wild-type HOM3, HOM2, HOM6, THR1, and THR4, and two mutant alleles of HOM3 (namely HOM3-R2 and HOM3-R6), that code for feedback-insensitive aspartate kinases. The results show that only the amplification of the HOM3 alleles leads to threonine and, in some instances, to homoserine overproduction. In terms of the regulation of the pathway, the data indicate that the main control is exerted by inhibition of the aspartate kinase and that, probably, a second and less important regulation takes place at the level of the homoserine kinase, the THR1 gene product. However, amplification of THR1 in two related Hom3-R2 strains does not increase the amount of threonine but, in one of them, it does induce accumulation of more homoserine. This result probably reflects differences between these strains in some undetermined genetic factor/s related with threonine metabolism. In general, the data indicate that the common laboratory yeast strains are genetically rather heterogeneous and, thus, extrapolation of conclusions must be done carefully. © 1996 John Wiley & Sons, Inc.
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  • 18
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    Biotechnology and Bioengineering 50 (1996), S. 248-256 
    ISSN: 0006-3592
    Keywords: yeast ; Saccharomyces ; flotation ; batch culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A fast flotation assay was used to select new floating yeast strains. The flotation ability did not seem to be directly correlated to total extracellular protein concentration of the culture. However, the hydrophobicity of the cell was definitely correlated to the flotation capacity. The Saccharomyces strains (FLT strains) were highly hydrophobic and showed an excellent flotation performance in batch cultures without additives (flotation agents) and with no need for a special flotation chamber or flotation column. A stable and well-organized structure was evident in the dried foam as shown by scanning electron microscopy which revealed its unique structure showing mummified cells (dehydrated) attached to each other. The attachment among the cells and the high protein concentration of the foams indicated that proteins might be involved in the foam formation. The floating strains (strains FLT) which were not flocculent and showed no tendency to aggregate, were capable of growing and producing ethanol in a synthetic medium containing high glucose concentration as a carbon source. The phenomenon responsible for flotation seems to be quite different from the flocculation phenomenon. © 1996 John Wiley & Sons, Inc.
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  • 19
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    Biotechnology and Bioengineering 51 (1996), S. 33-39 
    ISSN: 0006-3592
    Keywords: yeast ; fuel ethanol ; flocculation ; glucose conversion ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: By recycling the contents of a 14 L fermentor through a stripping column to continuously remove ethanol and reduce product inhibition, continuous complete conversion of nutrient feed containing 600 g/L glucose was achieved in a small pilot plant. Ethanol was recovered from the carbon dioxide stripping gas in a refrigerated condenser, and the gas was reheated with steam and recycled by a blower. Productivity of ethanol in the fermentor as high as 15.8 g/L/h and condensate production of up to 10 L/day of almost 50% by volume ethanol were maintained for up to 60 days of continuous operation. Weekly washing of the column packing in situ was required to prevent loss of performance caused by attached growth of yeast cells, which restricts the gas flow rate through the stripping column. © 1996 John Wiley & Sons, Inc.
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  • 20
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    Biotechnology and Bioengineering 51 (1996), S. 679-690 
    ISSN: 0006-3592
    Keywords: yeast ; dimorphism ; morphology ; image analysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A semiautomatic image analysis method has been developed to characterize the morphology of the dimorphic yeast Kluyveromyces marxianus var. marxianus (formerly fragilis) NRRLy2415 undergoing alcoholic fermentation of cheese whey permeate. The method is capable of separating cells into six defined categories, varying from simple ovoid yeast cells to branched mycelial cells. A sample size of 300 cells was found to be sufficient to obtain a statistically significant categorization. The processing time for a sample was found to be approximately 90 min. In addition to qualitative characterization, the method permits the measurement of geometric properties such as the width, length, and volume of individual cells or clusters of cells. When the cells analyzed by the automatic method were categorized on a manual basis, the error level in the automatic routine was found to be less than 3%.
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  • 21
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    Biotechnology and Bioengineering 52 (1996), S. 161-165 
    ISSN: 0006-3592
    Keywords: yeast ; signaling ; regulation ; catabolite repression ; metabolism ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In this article, knowledge concerning the relation between uptake of and signaling by glucose in the yeast Saccharomyces cerevisiae is reviewed and compared to the analogous process in prokaryotes. It is concluded that (much) more fundamental knowledge concerning these processes is required before rational redesign of metabolic fluxes from glucose in yeast can be achieved. © 1996 John Wiley & Sons, Inc.
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  • 22
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    World journal of microbiology and biotechnology 11 (1995), S. 508-511 
    ISSN: 1573-0972
    Keywords: Alcohol fermentation ; flocculation ; Lactobacillus fermentum ; yeast
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The effect of treatment of Lactobacillus fermentum with several protein- and carbohydrate-modifying reagents on the bacterium's ability to flocculate Saccharomyces cerevisiae was investigated. The proteinaceous nature of the cell-surface components of L. fermentum which are responsible for floc formation was confirmed by inactivation of floc formation following photo-irradiation, with Methylene Blue or Rose Bengal as sensitizer, or acylation with acetic anhydride, maleic anhydride or acetylimidazole, and by the reaction of the components with nitrous acid, I2 and performic acid. The phenolic hydroxyl group of tyrosine and the indole group of tryptophan appear essential for flocculation. Proteinaceous components of the yeast cell surface and carbohydrate components on the bacterial cell surface were not required for flocculation but carbohydrate residues on the yeast surface were essential.
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  • 23
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    World journal of microbiology and biotechnology 11 (1995), S. 567-571 
    ISSN: 1573-0972
    Keywords: Geotrichum ; lactic acid bacteria ; maize fermentation ; pozol ; yeast
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Mexican fermented maize dough, pozol, including traditional banana leaf-wrapped samples and material in plastic bags, was purchased. All samples were pH 4.7 to 5.7 approx. 12 h after preparation, pH declining to 3.6 to 3.9 after 6 to 9 days storage at ambient temperature. These latter samples had dry matter contents of 31% to 48% (w/w), 0.35% to 0.75% titratable acidity as lactic acid and lactic acid bacteria as predominant microbial flora at about 108 c.f.u./ml. The lactic acid bacteria included strains of Leuconostoc mesenteroides, Lactobacillus plantarum, Lactobacillus confusus, Lactococcus lactis and Lactococcus raffinolactis. Fungi were not found in the samples stored in plastic bags. The samples wrapped in banana leaf, however, developed a large surface mycoflora within 2 days. This included Geotrichum candidum, yeasts and moulds. The majority of the lactic acid bacteria and approx. 50% of yeasts hydrolysed starch to some extent. No Geotrichum isolate hydrolysed starch. Lactate was assimilated by all the Geotrichum isolates and by 17 of 39 yeast strains.
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  • 24
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    Electronic Resource
    Springer
    World journal of microbiology and biotechnology 11 (1995), S. 307-309 
    ISSN: 1573-0972
    Keywords: Immobilization ; Saccharomyces ; wall proteins ; yeast
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The time course of changes in the capacity of synchronized yeast cells to be covalently immobilized was determined and interpreted as an indication of chronological changes in the cell's outer-wall proteins. Corroborative evidence was obtained indicating that these transient changes are dependent on protein synthesis and connected with the progression of the cell cycle through the late S and/or early G2 phases.
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  • 25
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 48 (1995), S. 108-117 
    ISSN: 0006-3592
    Keywords: microfiltration ; hydrulic resistance ; fouling ; yeast ; depressurization ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The hydraulic resistance and membrane fouling effects of Candida utilis in fermentation broth were investigated using Millipore PVDF 0.22-μm membranes (GVWP and GVHP) in a stirred-cell system at 50 kPa and 700 rpm. With the various components of broth, spent medium, which contains colloidal particles and macromolecules having sizes (0.32 to 2.67 μm) comparable with the membrane pores (actual range 0.26 to 0.63 μm), was found to be the major contributing factor to the membrane fouling by broth through pore plugging. This led the spent medium to exhibit the highest hydraulic resistance (Rsm of 5.8E + 12 m-1) and percentage flux loss (81.0%) when compared with either intact cells alone in buffer or to whole broth. Intact cells appeared to physically block and protect the pores without significant adhesion, because of the relatively hydrophilic nature of their cell walls (hydrophobicity of 5.9% at hour 36), resulting in the lowest hydraulic resistance (Rsbc of 7.5E + 11m-1) and percentage flux loss (19.3%).However, the hydraulic resistance and percentage flux loss of broth increased as cells aged. This was attributed to the increase in particle loading (intact cells by 15.37%, released cell contents and cell fragments) and in the hydrophobicity of cell walls. Autoclaved broth, lysed broth and aged broth, which contained a larger portion of colloidal particles and released cell contents caused a more pronounced fouling effect. This was revealed by the absence of flux recovery after depressurization with continuous stirring, even when a hydrophilic membrane was used. Furthermore, the hydrophobicity of C. utilis was found to increase with yeast extract present in medium, and use of hydrophobic membranes helped enhance the fouling effect. Overall, the degree of irreversible membrane fouling could be revealed by the value of Rsm/Rt′ and the hydraulic resistance, which resulted from concentration polarrzation, could be revealed by the value of Rc/Rt′ where Rt = Rm + Rsm + Rc′ and Rm is the clean membrane resistance. © 1995 John Wiley & Sons, Inc.
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 48 (1995), S. 386-400 
    ISSN: 0006-3592
    Keywords: microfiltration ; yeast ; filtration ; Saccharomyces cerevisiae ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: To develop a highly efficient cell harvest step under time constraint, a novel rotating disk dynamic filtration system was studied on the laboratory scale (0.147-ft.2 nylon membrane) for concentrating recombinant yeast cells containing an intracellular product. The existing cross-flow microfiltration method yielded pseudo-steady state flux values below 25 LMH (L/m2. h) even at low membrane loadings (10 L/ft.2). By creating high shear rates (up to 120,000-1) on the membrane surface using a rotating solid disk, this dynamic filter has demonstrated dramatically improved performance, presumably due to minimal cake buildup and reduced membrane fouling. Among the many factors investigated, disk rotating speed, which determines shear rates and flow patterns, was found to be the most important adjustable parameter. Our experimental results have shown that the flux increases with disk rotating speed, increases with transmembrane pressure at higher cell concentrations, and can be sustained at high levels under constant flux mode. At a certain membrane loading level, there was a critical speed below which it behaved similarly to a flat sheet system with equivalent shear. Average flux greater than 200 LMH has been demonstrated at 37-L/ft.2 loading at maximum speed to complete sixfold concentration and 15-volume diafiltration for less than 100 min. An order of magnitude improvement over the crossflow microfiltration control was projected for large scale production. This superior performance, however, would be achieved at the expense of additional power input and heat dissipation, especially when cell concentration reaches above 80 g dry cell weight (DCW)/L. Although a positive linear relationship between power input and dynamic flux at a certain concentration factor has been established, high cell density associated with high viscosity impacted adversely on effective average shear rates and, eventually, severe membrane fouling, rather than cake formation, would limit the performance of this novel system. © 1995 John Wiley & Sons, Inc.
    Additional Material: 16 Ill.
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  • 27
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 46 (1995), S. 285-290 
    ISSN: 0006-3592
    Keywords: yeast ; ethanol ; amylases ; strain development ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A procedure was developed for construction of industrial strains of distiller's yeast (Saccharomyces cerevisiae). It includes several steps: construction of congenic genetically marked haploid strains of opposite mating types starting from an industrial strain of hybrid nature, integrative transformation of the above haploid strains with a DNA fragment containing an expression cassette responsible for new technological facilities, and hybridization of transformants and isolation of final industrial homozygous strains under experimental conditions simulating commercial fermentation processes. This strategy permits the generation of strains that have desirable characteristics of traditional races of distiller's yeast along with new technological facilities determined by the particular expression cassette. Using this procedure, we have constructed an industrial strain with improved amylolytic activity. © 1995 John Wiley & Sons, Inc.
    Additional Material: 5 Ill.
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  • 28
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 48 (1995), S. 375-385 
    ISSN: 0006-3592
    Keywords: membrane microfiltration ; self-cleaning spiral vortices ; fouling ; concentration polarization ; yeast ; colloidal suspension ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel method of producing controlled vortices was used to reduce both concentration polarization and membrane fouling during microfiltration of Saccharomyces cerevisiae broth suspensions. The method involves flow around a curved channel at a sufficient rate so as to produce centrifugal instabilities (called Dean vortices). These vortices depolarize the build-up of suspended particles such as yeast cells at the membrane-solution interface and allow for increased membrane permeation rates. Various operating conditions under which such vortices effectively reduced cake build-up of suspended particles such as yeast cells at the membrane-solution interface and allow for increased membrane permeation rates. Various operating conditions under which such vortices effectively reduced cake build-up during microfiltration of 0 to 0.55 dry wt% yeast broth were investigated. Flux improvements of over 60% for 0.25 dry wt% yeast broth for flow with over that without Dean vortices were observed. This beneficial effect increased with increasing retentate flow rate and increasing transmembrane pressure and decreased with increasing concentration of suspended matter. Similar behavior was observed whether the cells were viable of killed. the improvement in flux in the presence over that in the absence of vortices correlated well with centrifugal force or azimuthal velocity squared. The relative cake resistances increased with reservoir yeast concentration. These values with vortices increased from 62% to 75% of that without vortices with increasing yeast concentration. The ratio of the cake thicknesses in the limiting case (at high feed concentration) was 3.25. These results suggest that self-cleaning spiral vortices could be effective in maintaining good and steady microfiltration performance with cell suspensions other than those tested. © 1995 John Wiley & Sons, Inc.
    Additional Material: 11 Ill.
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