JPH0116478B2 - - Google Patents

Description

[Detailed description of the invention]

INDUSTRIAL APPLICATION FIELD This invention relates to a novel yeast having excellent flocculating properties. In recent years, fermented alcohol, which can be obtained without petrochemistry, has been attracting attention as an energy alternative to petroleum. It is manufactured from sugar cane, molasses extracted from sugar cane, cellulosic or starchy materials such as sweet potatoes, potatoes, and corn, and by fermenting them using the action of microorganisms. Generally, in alcohol fermentation, alcohol productivity is proportional to the bacterial cell concentration in the fermenter. Therefore, as a means to increase the bacterial cell concentration in the fermenter, it is possible to use yeast that has excellent flocculating properties. That is, when yeast has excellent flocculating properties, the sedimentation rate of yeast becomes faster, and therefore solid-liquid separation can be performed quickly and easily. For example, in batch fermentation, the bacterial cells can be deposited by simply allowing the fermentation liquid to stand still, and the fermentation liquid and the bacterial cells can be easily separated and the cells can be reused. In continuous fermentation, a tower-type fermenter is used, which mainly consists of a small-diameter flow section, a large-diameter sedimentation section for bacterial cell sedimentation connected above the flow section, and a bacterial cell sedimentation member built into this. Thereby, even if the amount of culture medium supplied increases, the bacterial cells can be sedimented and their outflow can be prevented. As described above, the use of yeast that has flocculating properties has many advantages over the use of yeast that does not have flocculating properties, and therefore new flocculating yeasts are in demand. Prior art and its problems In the past, attempts have been made to obtain flocculating yeast in order to meet the above demands, but the conventional yeast is a wild strain obtained from the natural world. It was isolated from a specific soil. However, the task of finding and isolating a desired bacterial strain from the natural world is extremely troublesome, and there is little certainty that the desired bacterial strain can be collected. The present invention was made in view of the above-mentioned circumstances, and an object of the present invention is to provide a novel flocculating yeast that has excellent flocculating properties and can be obtained in a laboratory. Means for Solving the Problems This invention: ● has a flocculating property with a DF value of 5; By adding 7 ml of the preculture solution of the strain to 70 ml of the clear solution and performing batch culture, 53.1 g/ and 57.5 g/ml were obtained after 24 and 48 hours, respectively.
Acid mother Saccharomyces cerevisiae (FR _M17 V _M2 -4) that produces g/g of ethanol
S1 (Feikoken Bibori No. 7799) (hereinafter referred to as "the yeast according to this invention"). In this specification, the degree of flocculation of yeast is determined by the Gilliland test (European test) shown below.
Journal of Applied Microbiology and
Biotechnology Vol. 7, pp. 227-234, 1979)
The DF value calculated by is displayed. That is, after culturing the test bacterial strain in YPG medium (Note 1) at 30°C for 16 hours with shaking, the sedimentation rate of the bacterial cells, the volume and hardness of the sedimented bacterial cells were compared with the control strain by visual observation,
The degree of aggregation is displayed in six stages from DF value 0 to 5 shown in Table 1.

[Table] The yeast according to the present invention has the following mycological properties. In other words, this yeast has a flocculating property with a DF value of 5, and exhibits a remarkable sedimentation property in liquid culture. - Blackstrap molasses (for example, blackstrap molasses containing 15% total sugar)
is fermented to produce 7 to 9 vol% ethanol. ● Forms somewhat hard colonies on an agar plate. ●Has spore-forming ability. The yeast culture medium according to this invention includes a carbon source,
Conventional media containing nitrogen sources, inorganic ions and, if necessary, organic micronutrients can be used. Carbohydrates such as glucose, galactose, fructose, sucrose, starch hydrolyzate, fruit juice, and cellulose decomposition products are often used as carbon sources. A particularly suitable medium is a medium consisting of 1 g of yeast extract, 2 g of polypeptone, 2 g of glucose, and 100 ml of distilled water, and the pH of this medium is 5.5 without adjustment. Culture at a temperature of 25-40℃, preferably 30-37℃, and a pH of
It is carried out at a pH of 3.0 to 7.0, preferably 3.5 to 6.0. Next, a method for producing yeast according to the present invention will be explained. The yeast according to the present invention is a yeast Saccharomyces having a flocculating property with a DF value of 4.
It is produced by subjecting FR _M17 V _M2-4 (Feikoken Kyoiku No. 7795) to sporulation treatment and culturing the resulting spores. Sporulation treatment is carried out according to conventional methods. Normally, yeast that does not have flocculating properties are grown on YPG agar medium (Note 2).
After culturing on a spore-forming agar medium (Note 3), a method is used. To obtain cells derived from single spores, the asci are lysed using a lytic enzyme for lysing the yeast cell wall, and then the spores are separated using a micromanipulator, or the asci are separated using a lytic enzyme. After dissolving the spores, the spores are dispersed by ultrasonication, and the spores are then cultured on a nutrient agar medium. The above-mentioned yeast FR _M17 V _M2-4 contains the acid mother Saccharomyces cerevisiae RM-17 (Feikoken Bibori No. 7770) (hereinafter simply referred to as RM-17), which has flocculating properties.
Acid mother Saccharomyces cerevisiae (Saccharomyces cerevisiae) VM-2 (Feikoken Bibori No. 7788) (hereinafter simply referred to as VM-2) that does not have aggregating properties
It is produced by performing protoplast fusion treatment and culturing the fused bacterial cells. Protoplast fusion is performed by conventional methods. Usually, each bacterial cell suspension is prepared at a concentration of 10 ⁷ to ^{10 9} cells/ml, and after mixing preferably equal amounts of these suspensions, the mixture is mixed with a protoplast preparation solution containing yeast cell wall lytic enzyme. or, each bacterial cell suspension is treated with the same preparation solution and then mixed. RM-17 is an acid mother Saccharomyces cerevisiae IFO-0224 (hereinafter referred to as
(simply referred to as IFO-0224) is subjected to sporulation treatment, the resulting spores are subjected to mutation treatment, the mutant spores are cultured, the mutant strain is detected from the obtained colony by the replica method, and the mutant strain is isolated. manufactured and also
VM-2 is an acid parent Saccharomyces cerevisiae that does not have aggregating properties.
EY-1 (Feikoken Bacteria No. 7793) was also subjected to sporulation treatment, the resulting spores were subjected to mutation treatment, the mutant spores were cultured, and the mutant strain was detected from the resulting colonies by the replica method. , manufactured by separating this. The sporulation treatment is performed as described above. The mutation treatment is a physical method of irradiating the spores or asci obtained by sporulation treatment with ultraviolet rays, X-rays, γ-rays, ethyl methanesulfonate, N-methyl-N'-nitro- Although this can be carried out by any chemical method in which growth is performed on a selective medium after contact with a mutagenic agent such as N-nitrosoguanidine or 4-nitroquinoline-N-oxide, the method using ethyl methanesulfonate is particularly preferred. In the series of production steps described above, the medium and culture conditions are the same as those of the yeast itself described above. IFO-0224 has a DF value of 0 and shows no cohesiveness. Further, yeast belonging to Satsucamyces cerevisiae has various properties (existence of fermentability and assimilation, physiological properties) as shown in Table 2 below.

[Table] In Table 2, the fermentability of raffinose is expressed by how many sugars it can ferment out of the constituent monosaccharides fructose, glucose, and galactose produced by cleavage of the bond. In other words, fermentability 1/3
"fermentability" means the case where only fructose is fermented, "2/3 fermentability" means the case where fructose and glucose are fermented, and "fermentability 3/3" means the case where all the constituent monosaccharides are fermented. In addition, Saccharomyces
Yeast belonging to the genus are known to have the following mycological properties (J. Lodder, “The
Yeasts, A Taxonomic Study” 2nd edition,
North-Holland Publishing, 1970). In other words, yeast belonging to this genus: ●Proliferate by multipolar budding. ● Forms ascospores. ●Does not assimilate nitrates. ●Lack or form only a few fungal threads. ●Mature asci do not cleave easily. ●The shape of the spores is spherical or oval. ●Ferment glucose well. ●Does not form a film on the wort medium. Effects of the invention Since this invention is configured as described above,
A new yeast having excellent flocculating ability (DF value = 5) can be obtained from yeast having flocculating ability (DF value = 4). Therefore, there is no need for the conventional troublesome work of finding a desired strain from nature and separating it from soil, and the desired flocculating yeast can be reliably produced. By carrying out alcohol fermentation using the flocculating yeast obtained in this way, the bacterial cell concentration in the alcohol fermenter can be maintained at a high level in both batch fermentation and continuous fermentation as explained at the beginning, increasing ethanol productivity. can be significantly improved. Examples Next, examples of the present invention will be shown to demonstrate the above effects. I Production Example (a) Preparation of RM-17 Non-agglomerating acid mother Saccharomyces cerevisiae IFO
-0224 was cultured on a YPG agar medium (Note 2) at 30°C for 24 hours, then spread on a sporulation agar medium (Note 3), and cultured at 30°C for 3 to 5 days. In this way, spores were formed. Next, the asci were suspended in 1 ml of sterile water so that the number of spores was 10 ⁷ /ml, and after collection, the cells were washed with phosphate buffer (Note 4). The ascus was then shaken in 2 ml of lytic enzyme solution (note 5) at 30°C for 1 hour to dissolve the ascus. After bacterial collection, the released spores were washed with 1 ml of sterile water and suspended in 3 ml of phosphate buffer. To this suspension, 0.1 ml of ethyl methanesulfonate was added as a mutagenic agent, and the suspension was shaken at 30°C for 2 hours. The spores were thus mutated. After harvesting, the mutant spores are placed in a phosphate buffer solution.
Add 3 ml of 5% sodium thiosulfate aqueous solution to the suspension and incubate the suspension at 30°C.
Shake for 10 minutes. The mutagen was thus neutralized. After harvesting, the mutant spores are washed twice with 1 ml of phosphate buffer, suspended in 5 ml of the same buffer, and the suspension is sonicated for 3 minutes on ice to remove the mutant spores in the suspension. dispersed into. After collecting the bacteria, dilute the suspension with sterile water to a concentration of 1/10 ⁵ to 1/10 ⁶ and transfer 0.1 ml of the diluted suspension to YPG agar medium (Note 2).
The spores were smeared on the spores and cultured at 30°C for 48 hours to obtain colonies derived from single spores. Using the colony plate thus obtained as a master plate, mutant strains were detected by the replica method. That is, using sterilized velvet cloth, replicate the colony on the master plate onto a minimal medium (Note 6), culture it on the same medium at 30°C for 4 days, and detect strains that cannot grow on the minimal medium on the master plate, This was harvested from the master plate as an auxotrophic mutant strain. As a result, out of the 25 strains on the master plate, a strain of Saccharomyces cerevisiae RM-17 (Feikoken Bacteria Collection No. 7770) with excellent aggregation properties was obtained. This strain was an adenine and histidine auxotrophic strain. (b) Preparation of VM-2 Non-aggregating acid mother Saccharomyces cerevisiae EY-1 (Microbiological Research Institute, Applied Technology Department, Biochemical Engineering Laboratory, Agency of Industrial Science and Technology) Saccharomyces cerevisiae (Saccharomyces cerevisiae) VM-2 (Saccharomyces cerevisiae) was mutated in the same manner as for the preparation of RM-17, and the replica method was used to create an auxotrophic mutant strain auxotrophic for isoleucine and valine. 7788) was obtained. (c) Protoplast fusion of RM-17 and VM-2 RM-17 was cultured with shaking in 10 ml of YPD medium at 30°C for 16 hours, and after harvesting, it was washed with 1 ml of sterile water. Next, add this to approximately 2 ml of protoplast preparation solution (Note 7)
The suspension was shaken at 30°C for 1 hour, and after collecting the bacteria, it was washed twice with 1 ml of isotonic solution (Note 8). VM-2 was also processed using the same operations as above. Next, equal amounts of the RM-17 treated bacterial cells and VM-2 treated bacterial cells obtained in this way (cell number 10 ⁸
After bacterial collection, the mixture was suspended in 0.1 ml of isotonic solution, and 2 ml of polyethylene glycol aqueous solution (Note 9) was added to the suspension. This suspension was allowed to stand at 30°C for 15 minutes to complete protoplast fusion. After collecting the bacteria, the cells were suspended in 1 ml of isotonic solution, and the suspension was allowed to stand at 20°C for 15 minutes. Then, the suspension is made into an isotonic solution with a concentration of 1/10 to 1/1/2.
Dilute the diluted suspension to 10 ^{to 2} in minimal medium (Note 6)
and overlaid with overlay medium (Note 10). In this state, culture was carried out at 30° _C for 4 days, and a fusion strain with a certain degree of flocculation (DF value = 4) was isolated _. (No. 7795). Note that the parental strains (RM-17 and VM-2) used for protoplast fusion could not grow on the above minimal medium. (d) (FR _M17 V _M2 -4) Preparation of S1 The above FR _M17 , which is a protoplast fusion yeast
V _M2-4 was cultured on YPG agar medium (Note 2) at 30°C for 24 hours, then spread on sporulation agar medium (Note 3), and cultured at 30°C for 3 to 5 days. In this way, spores were formed. Next, the asci were suspended in 1 ml of sterile water so that the number of spores was 10 ⁷ /ml, and after collection, the cells were washed with phosphate buffer (Note 4). The ascus was then shaken in 2 ml of lytic enzyme solution (note 5) at 30°C for 1 hour to dissolve the ascus. After collecting the bacteria, the released spores were washed with 1 ml of sterile water, suspended in 5 ml of phosphate buffer, and the suspension was sonicated for 3 minutes on ice to remove the mutant spores into the suspension. Dispersed. After collecting bacteria, the suspension was diluted with sterile water to a concentration of 1/10 ⁵ to 1/10 ⁶ , and 0.1 ml of the diluted suspension was spread on YPG agar medium (Note 2) and cultured at 30°C for 48 hours. A colony derived from a single spore was obtained. Of the 30 strains obtained in this way, 24 strains with excellent agglutination properties were obtained (frequency 80%), and these
One strain out of the 24 strains was designated as Saccharomyces (FR _M17 V _M2-4 ) SI (Feikoken Bacteria No. 7799). Measurement of flocculation and alcohol fermentation ability IFO-0224, RM-17, EY-1, VM-2,
For FR _M17 V _M2-3 and the treated yeast obtained by spore molding it as described above, the DF value indicating the degree of flocculation and the alcohol fermentation ability were measured. The DF value was determined by the method described above. In addition, alcohol fermentation ability was determined by the following method.
That is, after mixing and dissolving 3.4 g of ammonium sulfate and 0.2 g of potassium pyrosulfite in 340 g of blackstrap molasses from Okinawa, the pH was adjusted to 4.5 with sulfuric acid, and the mixed solution was centrifuged at 3000 rpm for 10 minutes. Ta. Take 70 ml of the supernatant liquid obtained in this way, add 7 ml of the preculture solution of the bacterial strain to each liquid, and store them at 30°C.
Batch culture of RM-17 was carried out with intermittent stirring (repetition of stirring for 30 seconds and standing still for 10 minutes), and after 24 hours and
After 48 hours, the amount of ethanol produced in each culture solution was measured by gas chromatography. The measurement results are shown in Table 3 below.

[Table] As is clear from Table 3, by sporulating the fusion yeast FR _M17 V _M2-4 , which has a certain degree of flocculation (DF value = 4), excellent flocculation (DF value = 5) was achieved. Yeast with (FR _M17 V _M2-4 ) S1
can be obtained. Usage Example (Continuous Alcohol Fermentation) (FR _M17 V _M2-4 ) Continuous alcohol fermentation was carried out using S1 according to the following procedure, and its alcohol fermentation ability was investigated. As the fermentation apparatus, an alcohol fermentation apparatus shown in FIG. 1 was used. This mainly consists of a glass fluidized bed fermenter 1 with an actual volume of 700 ml, and is configured to be able to control temperature and pH. Then, the fermentation raw material is supplied to the bottom of the tank 1 by pump 2, and the reaction liquid is returned from the top to the bottom of the tank by pump 3.
It is designed to flow out from the bacterial cell sedimentation section 4 at the top of the tank. YPG medium (Note 1) in a 500ml Sakaguchi flask
After adjusting 100 ml and sterilizing it at a temperature of 121°C for 10 minutes, one strain of S1 (FR _M17 V _M2 -4) stored in a YPG agar slant medium (Note 2) was inoculated into an ear of 30°C.
The cells were cultured overnight. Thus active (FR _M17 V _M2 −
4) A preculture solution of S1 was obtained. 100 ml of the above preculture solution was placed in fermenter 1 containing 700 ml of Philippine molasses medium (Note 11), and batch culture was carried out at a fermentation temperature of 30° C. for 8 hours. Next, the molasses medium was continuously supplied to the fermenter 1 at a flow rate of 35 ml/hour (dilution rate = 0.05 hour ^-1 ), and the supply amount of the medium was gradually increased to carry out continuous fermentation. As a result, the medium supply amount was 175ml/hour (dilution rate =
Even if the yeast increases to 0.25 h ^-1 ), flocs with a diameter of 1 to 4 mm are formed in the tank due to the excellent flocculation properties of this yeast, and the bacterial cell concentration (Note 12) in the tank remains at a high value of 47 g/. was maintained. Also, the alcohol produced is 61
The alcohol productivity (Note 13) reached a high value of 16 g/hr as shown in Figure 2. Comparative example As yeast (FR _M17 V _M2 -4) instead of S1
The above operation was repeated using EY-1 and making other matters the same as in the above usage example. As a result, the medium supply amount was 70ml/hour (dilution rate =
If it exceeds 0.1 h ^-1 ), alcohol productivity (Note 13)
As shown in Fig. 2, the amount decreased rapidly from 4 g/h. V Medium and Reagents The medium and reagents are as follows. (Note 1) YPG medium yeast extract 10g/ polypeptone 20g/ glucose 20g/ (note 2) YPG agar medium yeast extract 10g/ polypeptone 20g/ glucose 20g/ agar 20g/ (note 3) Sporulation medium sodium acetate 5g/ agar 20g/ (Note 4) Phosphate buffer 0.1M phosphate buffer PH = 7.5 (Note 5) Lytic enzyme solution 0.05% Zymolyase 20T (manufactured by Seikagaku Corporation) in 0.1M phosphate buffer (PH 7.5) A mixture of 2ml of the dissolved solution and 1.4μ of 2-mercaptoethanol (Note 6) Minimal medium Difco-Yeast Nitrogen Base W/O
Amino acid (manufactured by Difco) 6.7g/ Glucose 20g/ Agar 20g/ (Note 7) Protoplast preparation solution 1.5M potassium chloride 0.8ml, 2/15M phosphate buffer (PH7.5) 1.0ml, 2- Mercaptoethanol 1.4μ and zymolyase
Mixture of 0.2ml of 0.25% solution of 20T (Seikagaku Corporation) in 0.1M phosphorous buffer (PH7.5) (Note 8) Isotonic solution 0.6M potassium chloride aqueous solution (Note 9) Polyethylene glycol aqueous solution Calcium chloride 5.6g/Polyethylene glycol (PEG-600)
300g/ (Note 10) Overlay medium glucose 20g/ Difco‐Yeast Nitrogen Base W/O
Amino acid (manufactured by Difco) 6.7g/ Difco-Bact Agar (manufactured by Difco) 30g/ (Note 11) Philippine molasses medium Philippine molasses 280g/ Ammonium sulfate 2.8g/ Potassium pyrosulfite 0.5g/ Antifoaming agent 0.2g/ (Note 12) Bacterial cell concentration Take a certain amount of the culture solution in the fermenter, collect the microbial cells using a centrifuge, wash them, and adjust the temperature to
Calculated as the amount of bacterial cells burned at 800℃ (Note 13) Alcohol productivity Weight of alcohol produced in 1 hour per 1 culture solution (g)

[Brief explanation of drawings]

Figure 1 is a flow sheet for continuous fermentation, and Figure 2 is a graph showing the relationship between dilution rate and alcohol productivity.

Claims (1)

[Claims] 1 ●Has a flocculating property with a DF value of 5, ●Centrifuges a mixture of 340 g of blackstrap molasses, ammonium sulfate, and potassium pyrosulfite at pH 4.5, and adds 70 ml of the resulting supernatant. By adding 7 ml of the preculture solution of the strain and performing batch culture, 53.1 g/ and 57.5 g/ml were obtained after 24 and 48 hours, respectively.
Yeast Saccharomyces cerevisiae (FR _M17 V _M2 -4) producing g/g of ethanol
S1 (Feikoken Bibori No. 7799).