• Journal of Life Science
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• v.14 no.5
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• pp.840-846
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• 2004

A study for expression of Korean Mistletoe (KM) lectin gene (A,B) in Saccharomyces cerevisiae was done using transforming system of yeast. In order to overexpress the genes efficiently in yeast, two lectin genes (A,B) were re-cloned and modified including Kozak translation initiation sequence using PCR amplification. The constructed plasmids containing modified lectin A and B genes were transformed to S. cerevisea INVSc (MAT G, his3 $\Delta$1, leu2, trpl-289, ura3-52). The transformed cells were identified by DNA sequencing with ABI3700 system and induced with 2% of galactose for recombinant KM lectin (rKM lectin) protein. The rKM lectin A and B proteins were determinated about 29kDa size of protein by SOS-P AGE and western blotting analysis. The expressed recombinant lectin was determinated 1.24∼1.75 $\mu\textrm{g}$ per 1 mg of cytosolic soluble protein by sandwich ELISA method. Moreover the lectin genes were expressed as maximum level at 36 h after galactose induction and lectin A gene was were repressed after 48 h.

• Journal of Microbiology and Biotechnology
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• v.9 no.3
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• pp.340-345
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• 1999

A novel simultaneous saccharification and fermentation (SSF) process from the microcrystalline cellulose to ethanol was developed by using $\delta$-integrated recombinant cellulolytic Saccharomyces cerevisiae L2612$L2612\deltaGC$, which can utilize cellulose as carbon and energy sources. The optimum amount of enzymes needed for the efficient conversion of cellulose to ethanol at $30^{\circ}C$ was determined with commercial cellulolytic enzymes. By fed-batch cultivation, the heterologous cellulolytic enzymes were accumulated up to 42.67% of the total cellulase and 29% of the $\beta$-glucosidase needed for the efficient SSF process. When this $\delta$-integrated recombinant yeast was applied to the successive SSF step for ethanol production, 20.35 g/l of ethanol was produced after 12 h from 50 g/l of microcrystalline cellulose. By using this novel SSF process, a considerable amount of commercial enzymes was reduced.

• Biotechnology and Bioprocess Engineering:BBE
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• v.7 no.1
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• pp.52-55
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• 2002

Flow cytometric techniques were used to investigate cell size, protein content and cell cycle behavior of recombinant Saccharomyces cerevisiae strains producing human lysozyme (HLZ). Two different signal sequences, the native yeast $MF\alpha1$ signal sequence and the rat $\alpha-amylase$ signal sequence, were used for secretion of HLZ. The strain containing the rat $\alpha-amylase$ signal sequence showed a higher level of internal lysozyme and lower specific growth rates. Flow cytometric analysis of the total protein content and cell size showed the strain harboring the native yeast signal sequence had a higher total protein content than the strain containing the rat $\alpha-amylase$ signal sequence. Cell cycle analysis indicated that the two lysozyme producing recombinant strains had an increased number of cells in the $G_2+M$ phase of the yeast cell cycle compared with the host strain SEY2102.

• KSBB Journal
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• v.26 no.5
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• pp.439-442
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• 2011

1,2-propanediol (1,2-PD) is a commodity chemical that is currently produced from petrochemical derivatives. Saccharomyces cerevisiae is well characterized and a successful industrial microorganism to enable the improvement of the 1,2-propanediol production by metabolic engineering. A recombinant S. cerevisiae M3G3 was used to produce 1,2-propanediol. S. cerevisiae M3G3 is the diploid strain that contains 3 copies of mgs (methylglyoxal synthase) and gldA (glycerol dehydrogenase). S. cerevisiae M3G3 was cultivated at various culture conditions by changing culture temperature, glucose concentration, and inducer concentration. Also the effect of induction time was studied to optimize the production of 1,2-propanediol. Batch and fed-batch cultivation of S. cerevisiae M3G3 was performed by using a 5 L jar fermenter. The highest concentration of 1,2-propanediol in batch cultivation was 0.86 g/L and it was further improved to 1.33 g/L in fed-batch cultivation.

• Korean Journal of Microbiology
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• v.27 no.2
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• pp.77-84
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• 1989

The temperature sensitive (ts) mutation on RNA1 gene of Saccharomyces cerevisiae prevents growth at restrictive temperature ($36^{\circ}C$) by accumulation of precursor tRNA, rRNA and mRNA (Hutchison et al., 1969; Shiokawa and Pogo, 1974; Hopper et al., 1978). RNA1 gene was cloned by complementation of the temperature sensitive growth defect of an rna1-1 mutant strain and identified by retransformation and concomitant loss of recombinant plasmid on non-selective condition. By deletion mapping, it was found that RNA1 gene resides within 3.5kb of BgII fragment.

• Microbiology and Biotechnology Letters
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• v.20 no.4
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• pp.417-421
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• 1992

The expression pattern of the cloned SUC2 gene in recombinant Saccharomyces cerevisiae was investigated in a two-stage culture. The recombinant yeast grown in a glucose medium where the SUC2 gene was repressed was harvested and then resuspended in a sucrose medium to induce invertase expression. The maximum activity of 10 units was obtained in a medium containing 2 $g/\ell$ sucrose as a carbon source at $30^{\circ}C$ . The oscillatory behavior of invertase activity in response to glucose concentrations in the second stage was observed. This effect can be attributed to a series of events: invertase expression from the SUC2 gene. sucrose hydrolysis to glucose and fructose by invertase, SUC2 repression by high glucose concentration, invertase induction as a result of depletion of glucose used for the yeast growth. The invertase activity was increased by 72.5% when growth temperature changed from $30^{\circ}C$: to $35^{\circ}C$.

• Microbiology and Biotechnology Letters
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• v.47 no.4
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• pp.662-666
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• 2019

In this study, the NABH558 gene expression system was constructed to efficiently produce neoagarobiose hydrolase (NABH) in Saccharomyces cerevisiae strain. The ADH1 and GAL10 promoters of the pAMFα-NABH and pGMFα-NABH plasmids were examined to determine the suitable promoter for the NABH558 gene expression, respectively. The effect of promoter and carbon sources on NABH558 gene expression was investigated by transforming each plasmid into the S. cerevisiae 2805 strain. The NABH activity in the 2805/pAMFα-NABH strain was 0.069 unit/ml/DCW in YPD medium, whereas that in the 2805/pGMFα-NABH strain was similar (0.02-0.027 unit/ml/DCW) irrespective of the medium composition. The higher NABH activity in the YPD medium was due to the increased NABH558 gene transcription. NABH produced in the recombinant strains could degrade agarose to galactose and AHG. This indicated that ADH1 promoter was a more optimal promoter for the expression of NABH558 gene than the GAL10 promoter. The NABH activity induced by the ADH1 promoter was about 3-fold higher than that induced by the GAL10 promoter.

• Microbiology and Biotechnology Letters
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• v.40 no.4
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• pp.348-355
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• 2012

In the present study, we investigated the overexpression and characterization of bovine pancreatic (bp)- DNase I in Saccharomyces cerevisiae and Pichia pastoris. The bp-DNase I gene was fused in frame with the GAL10 promoter, $MF{\alpha}$, and GAL7 terminator sequences, resulting in the plasmid, pGAL-$MF{\alpha}$-DNaseI (6.4 kb). Also, the bp-DNase I gene was fused in frame with the AOX1 promoter, $MF{\alpha}$, and AOX1 terminator sequences, resulting in the plasmid, pPEXI (8.8 kb). The recombinant plasmids, pGAL-$MF{\alpha}$-DNaseI and pPEXI were introduced into S. cerevisiae and P. pastoris host cells, respectively. When the transformed yeast cells were cultured at $30^{\circ}C$ for 48 h in galactose or methanol medium, bp-DNase I was overexpressed and the most of activity was found in the extracellular fraction. P. pastoris transformant activity showed 45.5 unit/mL in the culture medium at 48 h cultivation, whereas S. cerevisiae transformant revealed 37.7 unit/mL in the extracellular fraction at 48 h cultivation. The enzymatic characteristics, such as DNA cleavage and half life were investigated. Treatment of the recombinant DNase I from P. pastoris induced degradation of the calf thymus DNA within 1 minute, and this DNA degradation rate was higher than that of commercial bp-DNase I (SIGMA) and the recombinant DNase I from S. cerevisiae.

• 한국생물공학회:학술대회논문집
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• 2000.04a
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• pp.41-44
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• 2000

Fermentation characteristics of recombinant Saccharomyces cerevisiae containing the xylose reductase gene from Pichia stipitis were analyzed in an attempt to convert xylose to xylitol, a natural five-carbon sugar alcohol used as a sweetener. Xylitol was produced with a maximum yield of 0.95 (g xylitol/g xylose consumed) in the presence of glucose that is used as a cosubstrate for cofactor regeneration. However addition of glucose caused inhibition of xylose transport and accumulation of ethanol. Such problems were solved by adopting glucose-limlted fed-batch fermentation. This process done with S, cerevisiae EHl3.15:pY2XR at$30\;^{\circ}C$ resulted in 105.2g/L xylitol concentration with maximum productivity of 1.69 g $L^{-1}$ $hr^{-1}$.

• Journal of Microbiology and Biotechnology
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• v.1 no.4
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• pp.266-273
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• 1991

Hirudin, a 65-amino acid protein isolated from the salivary gland of the bloodsucking leech, Hirudo medicinalis, is a potent thrombin-specific inhibitor and blocks the thrombin-mediated conversion of fibrinogen to fibrin in clot formation. We have studied the gene expression and secretion of hirudin in yeast. Saccharomyces cerevisiae. A gene coding for hirudin was synthesized based on the amino acid sequence and cloned into a yeast expression vector $YEG{\alpha}-1$ containing the ${\alpha}-mating$ factor pre-pro leader sequence and galactose-inducible promoter, GALl0. Recombinant S. cerevisiae was found to secrete biologically active hirudin into the extracellular medium. The secreted recombinant hirudin was recovered from the culture medium and purified with ultrafiltration and reverse phase high performance liquid chromatography. Approximately 1 mg of hirudin per liter was produced under suboptimal culture conditions and brought to about 90% purity in two steps of purification.