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Applied and Environmental Microbiology, June 2004, p. 3377-3382, Vol. 70, No. 6
0099-2240/04/$08.00+0 DOI: 10.1128/AEM.70.6.3377-3382.2004
Copyright © 2004, American Society for Microbiology. All Rights Reserved.
Laboratorium voor Moleculaire Celbiologie and Vlaams Interuniversitair Instituut voor Biotechnologie, Institute of Botany and Microbiology, Katholieke Universiteit Leuven, B-3001 Leuven-Heverlee, Flanders, Belgium,1
Lesaffre Développement, F-59706 Marcq-en-Bar
ul Cedex, France2
Received 10 September 2003/ Accepted 3 March 2004
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When a cell suspension is cooled to a temperature of 0°C or less, both the suspending medium and the cells initially supercool. Extracellular ice crystal formation precedes intracellular freezing and is determined by the freezing point of the suspending medium and the presence of ice-nucleating agents. Based only on osmolarity, the freezing point of the cytoplasm is predicted to be approximately 1°C. Nevertheless, the cell interior typically remains unfrozen until the temperature is 10 to 15°C. This intracellular supercooling may be due to prevention of growth of ice into the cell interior by the cell membrane and due to the lack of nucleators of supercooled water within the cell (23, 24).
Following external freezing and internal supercooling, a chemical gradient for free water is established between the extracellular ice-containing water and the intracellular supercooled water. This thermodynamically unstable situation can be resolved either by water outflow or by internal freezing. At low cooling rates, ice crystal formation remains mainly extracellular, and water outflow from the cell is sufficient to restore the chemical equilibrium and minimize the intracellular supercooling. If cells are cooled rapidly, extensive intracellular supercooling occurs, and the chemical gradient is eliminated by freezing cellular water. The critical cooling rate at which intracellular ice crystals are formed is determined by the cell type, particularly the surface-to-volume ratio of the cell and the water permeability; larger, spherical cells and cells that are less permeable to water have a lower critical cooling rate (23, 24). Although the characteristics of primary lesions resulting from slow and rapid freezing are different, both processes are detrimental to the cell. This is the so-called two-factor hypothesis of freezing, which postulates that survival after freezing is mainly affected by two factors, cellular dehydration and intracellular ice crystal formation, which depend in opposite ways on the cooling velocity (23, 24).
Several cellular factors affect survival of yeast cells following freezing and thawing (for a review see reference 34). High trehalose levels (1, 6, 12, 13, 36) and high levels of heat shock protein expression (17) largely explain the freeze resistance acquired following exposure to mild forms of other stresses (22) and the influence of growth conditions on yeast freeze tolerance (10, 27, 30, 36). Data on the importance of cold shock proteins (18, 19) for freeze resistance are contradictory (16, 30). Given the oxidative and osmotic stress component of freeze stress, superoxide dismutases (29) and compatible solutes (28, 31, 32) also seem to protect yeast cells upon freezing. The importance of plasma membrane characteristics, such as fluidity and permeability, in relation to yeast freeze resistance has not been resolved (4, 20, 21). Finally, anti-freeze proteins (25) and hydrophylins (14, 15) are known to increase freeze tolerance.
Freeze tolerance and expression of the aquaporin-encoding genes AQY1 and AQY2 have been correlated based on a genome-wide gene expression analysis of the freeze-resistant industrial mutant strain AT25 (33). Overexpression of AQY1-1 or AQY2-1 in this strain increased freeze tolerance, both in cell suspensions and in small doughs, without negatively affecting growth or fermentation characteristics. Thus, the modification of aquaporin expression held promise for improving the freeze tolerance of commercial baker's yeast strains used in frozen dough applications. Unfortunately, aquaporin-overexpressing strains in industrial conditions were no more freeze tolerant than the controls were.
The goal of this work was to identify the cause of the difference between the results obtained with small doughs under laboratory conditions and the results obtained with large doughs under industrial conditions for freeze protection by aquaporin overexpression. We evaluated the cultivation conditions, freezing rate, and thawing rate as possible contributing factors. The results are important for understanding the molecular basis of freeze damage and the protective effect of aquaporin overexpression, as well as for improving industrial baker's yeast strains used in the preparation of frozen doughs.
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his3
1/his3
1 leu2
0/leu2
0 ura3
0/ura3
0) (3) and the industrial strain AT25 (± diploid, probably aneuploid) (35). In these strains, pYX012 KanMX (vector), pYX012 KanMX/AQY1-1 (pAQY1-1), and pYX012 KanMX/AQY2-1 (pAQY2-1) have previously been integrated at the TPI locus, resulting in geneticin-resistant strains (33). In laboratory conditions, cells were routinely grown in YP (1% [wt/vol] yeast extract, 2% [wt/vol] Bacto Peptone [Difco]) with 2% glucose (YPD) at 30°C in an orbital shaker at 200 rpm. In addition, production under pilot-scale conditions was performed in fed-batch mode (20-liter fermentor containing 10 liters of molasses medium) (36).
RGC after freezing.
The residual glucose consumption (RGC) after fermentation and freezing was determined by comparing the average glucose consumption of two frozen samples (FGC) to the average glucose consumption of two control samples (IGC), as described previously [RGC = (FGC/IGC) x 100] (33). Briefly, equal amounts of stationary-phase cells (40-µl cell suspensions at an optical density at 600 nm of 20 for laboratory strains and at an optical density at 600 nm of 15 for industrial strains) were frozen 30 min after the addition of glucose in order to mimic the production of frozen dough, in which the dough is frozen after mixing, kneading, and eventually a short prefermentation period. After thawing, 400 µl of YP containing 33 mM glucose was added to both the control cells and the stressed cells, and after incubation at 30°C for 3 h (laboratory strains) or for 2.5 h (industrial strains) the amount of glucose taken up was measured.
Routinely, cells were frozen in standard 1.5-ml Eppendorf microcentrifuge tubes (VWR International, Leuven, Belgium) (referred to as small tubes or single plastic layer below) in an ethanol bath at 30°C for 1 h, stored in a freezer at 30°C for 1 day, and thawed at room temperature (between 18 and 22°C). To evaluate the effect of several successive rapid freezing treatments, the tubes were frozen in an ethanol bath at 30°C for 1 h and thawed at room temperature for 30 min, and this procedure was repeated up to 10 times.
Occasionally, cells were frozen slowly by putting the small tubes in a standard 50-ml plastic centrifuge tube (Falcon; Becton Dickinson, Erembodegem, Belgium) (referred to as large tube or double plastic layer below) stuffed with paper tissue (to create an insulating layer) or by putting the small tubes in a freezer at 30°C, as individual tubes or in a large tube. To evaluate the effect of several successive slow freezing treatments, the tubes were frozen in a freezer at 30°C for 1 h and thawed at room temperature for 30 min, and this procedure was repeated up to 30 times. Occasionally, cells were frozen very rapidly (by immersion of the small tubes in liquid nitrogen, as individual tubes or in a large tube). Unless indicated otherwise, cells were thawed at room temperature. Occasionally, cells were thawed more slowly (on ice) or more rapidly (in a water bath at room temperature or at 30°C). During freezing, temperature changes for four of these freezing conditions were monitored by using a thermocouple (type PT; diameter, 3 mm; Fisher Bioblock Scientific, Illkirch, France) connected to a data collector (Quick; Bioblock).
Survival in frozen dough. (i) Laboratory conditions.
The level of survival (expressed as a percentage of CFU) after fermentation and freezing was determined by comparing the average number of CFU isolated from two frozen doughs to the average number of CFU isolated from two nonfrozen control doughs, as described previously (33). Most doughs were frozen rapidly at 30°C in an ethanol bath or slowly in a freezer at 30°C; the exceptions were two nonfrozen controls that were analyzed immediately. After 1 h, the samples that were frozen in the ethanol bath were stored in the freezer at 30°C.
(ii) Industrial conditions.
At Lesaffre Développement, lean doughs were prepared by using the following formulation (3,000 g of flour per batch): 100 g of flour (14.5 to 15.0% protein on a 14% moisture basis), 63 g of water (with crushed ice), 2 g of salt (NaCl), 6 g (1.6% on a dry weight basis) of compressed yeast (from pilot-scale production), and 1 g of improver (Ibis Bleu; Lesaffre International Ingrédients, Marquette Lez Lille, France). For sugar-containing doughs, 10% saccharose was added. The target dough temperature was 19°C at all stages of preparation. The dough was kneaded mechanically for 15 min with a spiral mixer (FPI 50; VMI, Montaigu, France) and subsequently divided and molded. After prefermentation for 30 min in an air-conditioned room at 19°C, dough portions were frozen at 35°C with ventilation until the core temperature was 20°C. The temperature profiles in the cores of the dough portions were measured with a thermocouple (type K; diameter, 1.3 mm; Bioblock) connected to a data collector (HotBox; Bioblock). The doughs were subsequently stored at 20°C. At different times a dough portion was thawed at 0°C, the yeast gassing power was measured with a Zymotachigraph at 27°C for 2 h, and the dough proofing time was determined at 35°C.
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FIG. 1. (A and B) Evaluation of yeast gassing power (A) and dough proofing time (B) during frozen storage of large industrial doughs made with AT25 overexpressing AQY1-1 () or AQY2-1 (x) and with AT25 ( ) and a control strain containing an empty plasmid ( ). The means and standard deviations for two independent tests are shown; the standard deviations for data points without error bars are less than 10% of the values of the points. (C) Temperature in the core of large, industrial doughs during freezing at 35°C with ventilation at Lesaffre Développement. The curve represents the average values for 64 measurements (two doughs, eight horizontal positions, and four vertical positions).
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FIG. 2. Freeze tolerance of AT25 and AT25 overexpressing AQY2-1 in small frozen doughs, either cultured under laboratory conditions and harvested from liquid medium ( and , respectively) or produced at a pilot scale and resuspended from yeast cake ( and , respectively), frozen in an ethanol bath at 30°C (A) or in a freezer at 30°C (B). Survival is expressed as the percentage of CFU isolated from two frozen doughs based on the number of CFU in two nonfrozen control doughs. The standard deviations for replicate samples are indicated; the standard deviations for data points without error bars are less than 10% of the values of the points.
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TABLE 1. Freeze tolerance of laboratory strain BY4743 and industrial strain AT25, with and without AQY1-1 or AQY2-1 overexpression, grown under laboratory conditions and tested in different freezing conditionsa
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FIG. 3. Temperature courses in cell suspensions during freezing in the ethanol bath (single plastic layer [ ] or double plastic layer [ ]) and in the freezer at 30°C (single plastic layer [ ] or double plastic layer [x]) (average of two measurements). For comparison, the first 10 min of the temperature course in the core of large, industrial dough during freezing at 35°C with ventilation at Lesaffre Développement (Fig. 1C) also is shown.
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TABLE 2. Freeze tolerance of laboratory strain BY4743 and industrial strain AT25, with and without AQY1-1 or AQY2-1 overexpression, grown under laboratory conditions and tested after successive rapid or slow freezing treatmentsa
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Our results for the effect of different freezing rates on yeast survival in the range of cooling rates that we studied are consistent with the results of other workers (7, 8, 23, 24). The levels of survival (expressed as RGC) generally remained high at cooling rates of 10 to 15°C per min but decreased dramatically at cooling rates of 30 to 35°C per min or higher (Table 1 and Fig. 3). The cooling rate for samples frozen in liquid nitrogen could not be determined with the thermocouple used, although it was presumed to be very high (7, 8). Aquaporin overexpression was somewhat advantageous when small tubes were put directly in liquid nitrogen, but it was even more advantageous when the cooling rate was slowed by use of a double plastic layer (Table 1).
When the survival after different consecutive slow freezing treatments was compared with the survival after the same number of rapid freezing treatments, it became clear that the increased freeze tolerance of aquaporin-overexpressing strains of S. cerevisiae seems to be restricted primarily to rapid freezing conditions (Table 2). Aquaporins mediate the rapid transport of water across the plasma membrane (2, 26). Our hypothesis is that higher levels of aquaporins in the plasma membrane allow rapid water efflux, especially at freezing temperatures, when water diffusion through the phospholipid layer of the membrane is limiting. Since the water permeability of the plasma membrane increases greatly at temperatures above the freezing point, the water flow probably is not limiting and the presence of excess aquaporins is not advantageous at low cooling rates.
This reasoning is consistent with the two-factor hypothesis of freezing injury. This hypothesis states that cells are mainly liable to cellular dehydration and exposure to solution effects at low freezing rates but that at high freezing rates mainly intracellular ice crystal formation occurs (23, 24). The observation that aquaporin-mediated improvement of freeze tolerance is restricted to rapid freezing conditions strengthens the hypothesis that improved freeze tolerance in baker's yeast overexpressing aquaporin implies that there is water export activity and results from a reduction in intracellular ice crystal formation (33). The results which we obtained with small doughs that were rapidly (Fig. 2A) or slowly (Fig. 2B) frozen and subsequently stored in the freezer also are consistent with this hypothesis. Dumont and coworkers relied on the same water permeability hypothesis that we relied on to explain the effects of cooling rate on yeast viability observed for the range of cooling rates that we studied (8).
If aquaporins effectively improve freeze tolerance only at high rates of freezing, then this limitation might help explain why aquaporin overexpression does not affect the leavening capacity of yeast cells in large, industrial frozen doughs (Fig. 1A and B). These industrial doughs usually are cooled at a rate of 0.6 to 0.8°C per min in the core of the dough (Fig. 1C and 3), which is much lower than the cooling rates used under laboratory conditions (Fig. 3). It is unlikely that the industrial freezing process could be adjusted in such a way that all cells in the dough undergo rapid enough freezing for aquaporins to be beneficial. Moreover, rapid freezing generally results in lower survival. Hence, the results described in this paper indicate that aquaporin overexpression is less useful for improvement of the maintenance of dough rising capacity in frozen doughs than originally thought (33).
Use of aquaporin overexpression for improvement of freeze tolerance might still have other potential applications (e.g., cryopreservation). The recent finding that artificial expression of an aquaporin improves the survival of mouse oocytes (5, 9) and fish embryos (11) after cryopreservation is particularly interesting in this respect. Finally, the fact that aquaporin overexpression is advantageous only for freeze tolerance in rapid freezing conditions also seems to limit the physiological importance of aquaporin-mediated freeze resistance of microorganisms under natural conditions.
We thank Renata Wicik and Kris Vandezande for technical assistance.
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