Characteristics of mechanically disrupted bakers' yeast in relation to its separation in industrial centrifuges

The viscosity, density, and sedimentation characteristics of suspensions of whole and mechanically disrupted yeast cells were measured. Mechanical disruption increases the suspension viscosity and its non-Newtonian behavior. Experiments showed a good correlation between laboratory- and industrial-scale centrifugation results.     

Clarification of yeast cell suspensions by depth filtration

Depth filtration can be very attractive for initial clarification because of low capital costs and ease of operation. However, there is currently no fundamental understanding of the effects of the filter pore size and morphology on the overall capacity and filtrate quality. The objective of this study was to examine the flux, capacity, and filtrate turbidity of a series of depth filters with different pore size ratings and multilayer structures for the filtration of yeast cell suspensions. Data were analyzed using available fouling models to obtain insights into the flux decline mechanisms. Filters with small pore size provide high filtrate quality at low capacity, with the reverse being true for the larger pore sizes. The multilayer structure of commercial depth filters leads to improved performance, although the choice of layer properties is critical. The highest capacity was achieved using a multilayer filter in which the upper layer allows significant yeast cell penetration into the filter matrix but still protects the retentive layer that is needed for a high quality filtrate.     

Non-Newtonian behaviour of yeast suspensions

Summary The rheological properties of yeast (Baker's yeast) suspensions in water and in water-methanol-electrolyte solutions have been investigated using a Fann V.G. concentric cylinder viscometer. The resulted rheograms could be described by the power law model for non-Newtonian fluids with the flow behaviour index n<1 indicating pseudo-plastic behaviour. This flow behaviour index was constant under all operating conditions while the consistancy index k increased exponentially with increasing wet yeast volume fraction. The addition of methanol and electrolytes had a negligible effect on the rheological properties. Changing the pH of the suspension acidic to lowered the apparent viscosities.     

A cytogenetic study of development in mechanically disrupted pairs of Tetrahymena thermophila

We examined the nuclear behavior of mating Tetrahymena cells that had been mechanically disrupted at various times throughout conjugation. Disruption was achieved by agitating conjugating Tetrahymena in the presence of 0.1-3 mm glass beads. Two minutes of agitation with 1 mm beads yielded optimal pair disruption (70%) with high viability (92%). Disrupting pairs between 0-4.7 h after the initiation of mating produced mostly disrupted conjugants in which development was aborted. However, as many as 20% of these early disrupted conjugants completed development even without their mating partners. After 5 h the percentage of disrupted conjugants completing development increased dramatically, reaching 80% by 6.7 h. These results support a model suggesting that events associated with nuclear exchange and fusion 5 h into conjugation trigger a commitment to completion of the postzygotic developmental program. The early conjugants that completed development following disruption suggest that development can be sustained even in the absence of a mating partner. This represents a novel method of bringing the micronuclear genome into macronuclear expression with minimal cytoplasmic exchange between partners. We discuss these results in light of a model relating cortical and nuclear signaling events that reciprocally drive conjugal development.     

自絮凝酵母SPSC01悬浮液的流变行为

用旋转黏度计测定了自絮凝颗粒酵母悬浮液的流变特性,并考察了其流变特性的影响因素,如菌体生物量、葡萄糖质量浓度、温度等。结果表明：自絮凝颗粒酵母悬浮液呈假塑性非牛顿流体,其流变特性服从幂律指数模型,随着菌体浓度的增大,稠度系数增大,流动行为指数减小;絮凝悬浮液的表观黏度随着糖浓度的增加有所增加,同一生物量下稠度系数k随着糖浓度的增加而增加,流动行为指数n随着糖浓度的增加变化很小,悬浮液的表观黏度随着温度的升高而降低;相同生物量下的流变指数随温度的升高而升高,而稠度系数随温度升高有所下降。     

Continuous measurement of ethanol production by aerobic yeast suspensions with an enzyme electrode

Summary An alcohol electrode was constructed which consisted of an oxygen probe onto which alcohol oxidase was immobilized. This enzyme electrode was used, in combination with a reference oxygen electrode, to study the short-term kinetics of alcoholic fermentation by aerobic yeast suspensions after pulsing with glucose. The results demonstrate that this device is an excellent tool in obtaining quantitative data on the short-term expression of the Crabtree effect in yeasts.Samples from aerobic glucose-limited chemostat cultures of Saccharomyces cerevisiae not producing ethanol, immediately (within 2 min) exhibited aerobic alcoholic fermentation after being pulsed with excess glucose. With chemostat-grown Candida utilis, however, ethanol production was not detectable even at high sugar concentrations. The Crabtree effect in S. cerevisiae was studied in more detail with commercial baker's yeast. Ethanol formation occurred only at initial glucose concentrations exceeding 150 mg·l^-1, and the rate of alcoholic fermentation increased with increasing glucose concentrations up to 1,000 mg·l^-1 glucose.Similar experiments with batch cultures of certain non-fermentative yeasts revealed that these organisms are capable of alcoholic fermentation. Thus, even under fully aerobic conditions, Hansenula nonfermentans and Candida buffonii produced ethanol after being pulsed with glucose. In C. buffonii ethanol formation was already apparent at very low glucose concentrations (10 mg·l^-1) and alcoholic fermentation even proceeded at a higher rate than in S. cerevisiae. With Rhodotorula rubra, however, the rate of ethanol formation was below the detection limit, i.e., less than 0.1 mmol·g cells^-1·h^-1.     

Antifoam fouling and its reduction by surfactant precoat treatment of polysulphone ultrafilter

Summary Precoat treatment of polysulphone membranes with non-ionic surfactant BRIJ 58 was effective in decreasing antifoam fouling in ultrafiltration of five model process streams such as fermentation media, broth and yeast suspension. The mean flux increase of about 90 % was achieved by the surfactant pretreatment.     

Rheological properties of suspensions containing cross-linked starch nanoparticles prepared by spray and vacuum freeze drying methods

The rheological behavior of suspensions containing vacuum freeze dried and spray dried starch nanoparticles was investigated to explore the effect of these two drying methods in producing starch nanoparticles which were synthesized using high pressure homogenization and mini-emulsion cross-linking technique. Suspensions containing 10% (w/w) spray dried and vacuum freeze dried nanoparticles were prepared. The continuous shear viscosity tests, temperature sweep tests, the frequency sweep and creep-recovery tests were carried out, respectively. The suspensions containing vacuum freeze dried nanoparticles showed higher apparent viscosity within shear rate range (0.1-100s(-1)) and temperature range (25-90°C). The suspensions containing vacuum freeze dried nanoparticles were found to have more shear thinning and less thixotropic behavior compared to those containing spray dried nanoparticles. In addition, the suspensions containing vacuum freeze dried particles had stronger elastic structure. However, the suspensions containing spray dried nanoparticles had more stiffness and greater tendency to recover from the deformation.     

Protein transmission during Dean vortex microfiltration of yeast suspensions.

Substantially higher rates of protein and fluid volume transport for microfiltration of yeast suspensions were possible with improved hydrodynamics using centrifugal fluid instabilities called Dean vortices. Under constant permeate flux operation with suspended yeast cells, a helical module exhibited 19 times the filtration capacity of a linear module. For feed containing both BSA and beer yeast under constant transmembrane pressure with diafiltration, about twice as much protein (BSA and other proteins from cell lysis) was transported out of the feed by the helical module as compared with the linear module. The volumetric permeation flux improvements for the helical over the linear module ranged from 18 to 43% for yeast concentrations up to 4.5 dry wt %.     

A new system of selecting yeast mutants with disrupted genetic recombination processes]

A new convenient system for isolation of the yeast mutants deficient in the genetical recombination is proposed. The chimeric plasmids constructed to carry the noncomplimenting mutant copy of the yeast ADE2 gene and different selectable yeast markers (LEU2 or TRP1 genes) are the basis for the system. Interplasmid intragenic recombination of ADE2 gene alleles in yeast cells transformed by two chimeric plasmids results in appearance of the secondary white prototrophic clones covering the primary red colony. The number of the clones reflects the recombination processes and is subject to an easy visual control. The proposed technique allows one to reveal both hypo and hyperrecombination mutants. Crossover or the gene conversion events can be distinguished by the simple genetical analysis of the secondary clones. The collection of mutants deficient in the genetical recombination has been obtained by the proposed technique.     

Improved yeast tolerance to ethanol-induced death by centrifugates of dense cell suspensions incubated with ethanol

Summary Ethanol-induced death rate was higher for cells ofSaccharomyces bayanus orKluyveromyces marxianus in spanse suspensions (2×10⁴ cells/ml) compared with dense suspensions (2×10⁵–2×10⁷ cells/ml). Specific death rates of sparse suspensions decreased to values similar to dense suspensions if ethanol-induced death experiments were undertaken in the media obtained after harvesting the cells previously incubated with the same lethal concentration of ethanol.     

Membranes of Rhodospirillum rubrum: physicochemical properties of chromatophore fractions isolated from osmotically and mechanically disrupted cells.

Isolation of highly purified membrane fractions from phototrophically grown Rhodospirillum rubrum was achieved by velocity and isopyknic sedimentation under carefully controlled ionic conditions. Bacteriochlorophyll-rich and succinic dehydrogenase-rich chromatophores that were essentially devoid of contamination by non-chromatophore protein were separated from a denser fraction in extracts disrupted in a French pressure cell. Highly purified chromatophores and a nearly photopigment-free envelope fraction were also obtained from cells lysed by treatment with ethylenediaminetetraacetate-lysozyme-Brij 58. After lysis with lysozyme and ethylenediaminetetraacetate alone, about 50% of the total photosynthetic pigment was released in chromatophores similar to those isolated by the above procedures. Chromatophores prepared by each method were found to have very similar near-infrared absorption spectra, overall chemical composition, equilibrium buoyant densities in CsCl, and protein patterns in sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The protein profiles of the dense, outer membrane-rich fractions were different from those of the chromatophores. The release of much of the photosynthetic apparatus as discrete chromatophores is osmotically lysed extracts necessitates a reevaluation of the concept that isolated chromatophores arise only from mechanical comminution of a larger membrane structure.     

Application of rotary microfiltration in debittering process of spent brewer's yeast

This study concerns the production of yeast extract from spent brewer's yeast using rotary microfiltration as a means to combine debittering and cell debris separation into a single step, without using a toxic alkali wash. The pH of yeast homogenate was found to affect protein yield and bitterness of the product. Rotary filtration of yeast homogenate at various pHs resulted in different percent protein transmissions. These were found to be 5.05%, 9.83%, and 30.83% for pH 5, 6, and 7.5, respectively. The bitterness concentration in the permeate was also found to be higher at higher pHs. Autolysis of the cell homogenate prior to filtration increased protein yield and decreased bitterness considerably. At pH 5.5, the protein transmission was increased to 60% and debittering efficiency was increased from 59% to 86%. The permeate flux and protein productivity could be further increased by increasing the rotational speed, but this resulted in a decrease in debittering efficiency. Thus, the rotational speed should be carefully selected to compromise between the yield and product quality. Furthermore, for the tested rotational speeds of 600 and 1000 rpm, the change in feed flow rate from 11 to 35 L h(-1) changes the flow behavior from turbulent vortex flow to laminar vortex flow, thus decreasing the flux and protein productivity.