WO2012108740A2

WO2012108740A2 - Mutant microorganism with enhanced sugar utilization and methods for preparing the same

Info

Publication number: WO2012108740A2
Application number: PCT/KR2012/001059
Authority: WO
Inventors: Sung Kuk Lee; Parisutham VINUSELVI
Original assignee: Unist Academy-Industry Research Corporation
Priority date: 2011-02-11
Filing date: 2012-02-13
Publication date: 2012-08-16
Also published as: WO2012108740A3

Abstract

The present invention relates to a mutant microorganism with enhanced sugar utilization and methods for preparing the same. The mutant strain is capable of effectively utilizing various sugars including cellobiose and xylose, and can thus be useful in the production of biofuels, physiologically active materials, medicinal materials or industrial chemicals from cellulosic biomass. It also reduces the need for addition of one out of the three enzymes used in the saccharification of lignocellulose. It also eliminates the need for separate reactors to ferment pentose and hexose sugar.

Description

DESCRIPTION

MUTANT MICROORGANISM WITH ENHANCED SUGAR UTILIZATION AND METHODS FOR PREPARING THE SAME FIELD OF THE INVENTION

The present invention relates to a mutant microorganism with enhanced sugar utilization and methods for preparing the same, with particular focus to a mutant microorganism obtained by genetic engineering such as promoter replacement in chb operon and/or asc operon or mutation ofyebK gene, or evolutionary adaptation.

BACKGROUND OF THE INVENTION

Due to depletion of petrochemical fuels, development of alternative energy sources has become a hot issue in recent years. As an alternative energy source, ethanol can be produced from cellulosic biomass, which is a renewable and most abundant carbon source stored on earth. Researches have been focused on effective decomposition of cellulose, hemi-cellulose and lignin present in lignocellulosic biomass through screening of novel strains with cellulolytic property as well as improvement of enzymatic saccharification and fermentation process.

Major steps involved in the cellulosic fuel production include i) the enzymatic saccharification of plant biomass into simple carbohydrates carried out by the synergistic action of at least three enzymes (e.g., endoglucanase, exoglucanase and β- glucosidase) and ii) microbial fermentation of these carbohydrates into value-added fuels. Recentl y, many researches are focused on simultaneous saccharification and fermentation (SSF), which combines enzymatic saccharification and microbial fermentation process in a same reactor, significantly enhancing the efficiency of ethanol production by reducing inhibitory action of the saccharifying enzymes and equipment costs. A s enzymatic saccharification is one of the most expensive steps in the overall process, researchers have endeavored to enhance the activity of the enzymes used in the saccharification or to develop novel strains capable of producing these enzymes. Advanced genetic engineering has enabled production of strains for simultaneous saccharification and fermentation by the introduction of genes encoding saccharifying enzymes into the fermentation strain or vice versa. Th e saccharifying enzyme as a heterogenous gene, however, shows considerably low level of expression, and it also has negative effects on cell growth and metabolism when overexpressed. Therefore, modifying the regulation of the endogenous pathway is considered more advantageous than the use of heterogenous genes.

E. coli is one of the most effective microorganisms for lignocellulosic fuel production because of its ability to utilize all sugars derived from hydrolysis of biomass. However, the potential of E, coli is limited due to carbon catabolite repression (CCR), i.e., inhibition of biosynthesis of enzymes involved in catabolism of carbon sources other than the preferred one (e.g., glucose) in hydrolysate. Thus, sugars such as xylose and arabinose cannot be metabolized until the depletion of glucose. T his preference toward glucose utilization impedes fermentation process by reducing the productivity and affects downstream processes due to unused carbon sources. Composition of sugar mixture obtained from lignocellulosic hydrolysate may vary, but glucose and xylose would occupy a significant portion of them. Therefore, there is still need of developing a mutant E. coli with enhanced sugar utilization and capable of utilizing sugars simultaneously without preference in order to improve the cost, efficiency and usability in the cellulosic fuel production.

SUMMARY OF THE INVENTION

It is an object of the present invention to provide a novel mutant microorganism with enhanced sugar utilization.

It is another object of the present invention to provide a method for preparing a mutant microorganism with enhanced sugar utilization.

It is still another object of the present invention to provide a method for producing biofuels, physiologically active materials, medicinal materials or industrial chemicals from biomass by employing the above-mentioned mutant microorganism.

In accordance with one aspect of the present invention, there is provides a mutant microorganism prepared by introducing to a wild-type microorganism a mutation selected from:

(a) replacement of the cryptic promoter of chb operon with an active promoter; (b) replacement of the cryptic promoter of asc operon with an active promoter; and

(c) replacement of the cryptic promoters of chb operon and asc operon with active promoters.

In accordance with another aspect of the present invention, there is provided a method for preparing a mutant microorganism, which comprises:

(a) replacing one or more inactive promoters of chb operon and asc operon with one or more promoters. The mutant microorganism according to the present invention has enhanced capability to utilize various sugars such as cellobiose and xylose, unlike other microorganisms, and can thus be useful in the production of biofuels, physiologically active materials, medicinal materials or industrial chemicals from cellulosic biomass that is mainly composed of glucose and xylose. In addition, the mutant microorganism is advantageous in that there is no need to use β-glucosidase, one of the three hydrolyzing enzymes (endoglucanase, exoglucanase, and β-glucosidase) which catalyzes the last step of the saccharification process. Cellobiose, the substrate for β- glucosidase is an inhibitor against endoglucanase or exoglucanase. In the above- mentioned mutant, cellobiose will be transported into the cells, which would help prevent inhibition of the enzymatic activity of endoglucanase or exoglucanase. Furthermore, the mutant microorganism can utilize various sugars simultaneously, resulting in improved availability of substrate, removal of CCR, shortened fermentation time, and enhanced fermentation productivity. Th e mutant also reduces the need for addition of one out of the three enzymes used in the saccharification of lignocelluloses, and eliminates the need for separate reactors to ferment pentose and hexose sugar.

Other features and embodiments of the present invention will be apparent from the following description and the appended claims.

BRIEF DESCRIPTION OF DRAWINGS

Fig. 1 illustrates the replacement process of the cryptic promoter of chb operon with an active promoter.

Fig. 2 illustrates the replacement process of the cryptic promoter of asc operon with an active promoter.

Fig. 3 shows β-glucosidase activities (U/mL) of CP12CHB, CP 12 ASC and CP12CHBASC, and wild-type MG1655 in LB medium.

Fig. 4 shows β-glucosidase activities (U/mL) of CP12CHBASC in different culture media (LB, M9-Glucose and M9-Cellobiose).

Fig. 5 shows growth rates of CP12CHB (▲), CP 12 ASC (■), and wild-type MG1655 (·: when cultured in a cellobiose minimal medium; o: when cultured in a glucose minimal medium).

Fig. 6 shows the concentrations of the remaining cellobiose (♦) and xylose (■) in each medium after culturing CP12CHBASC (A) and CP12CHBASC/CRP* (B).

Fig. 7 shows xylose (A) and cellobiose (B) utilization rates of CP12CHBASC (■) and CP12CHBASC30 (·), where A indicates the concentration of remaining xylose after cultured in a medium containing xylose, and B indicates the concentration of remaining cellobiose after cultured in a medium containing cellobiose.

Fig. 8 shows the concentration of the remaining cellobiose (♦) and xylose (■) after culturing CP12CHBASC30 in various media (A: 2g cellobiose + 2g xylose; B: 3g cellobiose + 2g xylose; C: lg cellobiose + xylose).

Fig. 9 shows a process of deleting yebK gene to produce CP12CHBASCyebK- strain in accordance with the present invention.

Fig. 10 illustrates simultaneous utilization rates of cellobiose and xylose by CP12CHBASC, CP12CHBASC30, CP12CHBASCyebK- and CP12CHBASC30yebK- as prepared in Examples 3, 7, 11 and 12, respectively. F ig. 10A indicates a result for CP12CHBASC, Fig. 10B for CP12CHBASC30, Fig IOC for CP12CHBASCyebK-, and Fig. 10D for CP12CHBASC30yebK-. In each graph, a symbol (♦) represents cellobiose concentration (In %), (■) for xylose concentration and ( A ) for OD, respectively.

Fig. 11 illustrates simultaneous utilization rates of cellobiose and other sugars (glucose, mannose, galactose and arabinose) by CP12CHBASC obtained in Example 3.

Fig. 12 illustrates simultaneous utilization rates of cellobiose and other sugars (glucose, mannose, galactose and arabinose) by CP12CHBASC30 obtained in Example 7. Fig. 13 illustrates simultaneous utilization rates of cellobiose and other sugars (glucose, mannose, galactose and arabinose) by CP12CHBASCyebK- obtained in Example 11.

Fig. 14A and 14B shows growth rates of CP12CHBASC, CP12CHBASC30, CP12CHBASCyebK- and CP12CHBASC30yebK- obtained in Examples 3, 7, 11 and 12, under cellobiose (14A) and xylose (14B) as a carbon source, respectively.

Fig. 15 illustrates a process of promoter replacement to produce CP25XylAB/CP6XylFGH of Example 16.

Fig. 16 shows growth rates of CP12CHBASCyebK-/CP25XylAB/CP6XylFGH and CP12CHBASC/CP25XylAB/CP6XylFGH obtained in Example 16 under xylose as a carbon source.

Fig. 17 illustrates the map of pZB-yebK, a plasmid expressing yebK. The yebK was cloned under the control of tetracycline promoter and in a low copy plasmid to avoid metabolic burden.

Fig. 18 shows growth rate of CP12CHBASC/yebK-/pZB-yebK obtained in

Example 18 on a cellobiose minimal medium supplemented with varying concentrations of tetracycline (measured in TEC AN microplate reader).

Fig. 19 shows the expression levels of all genes present in the chb and asc operons in CP12CHBASC and CP12CHBASC30 by microarray analysis.

Fig. 20 illustrates the RT-PCR analysis to determine ascB expression level.

Lane 1 : Marker; Lanes 2 to 5: 25, 27, 30 and 32 cycles of ascB expression in CP12CHBASC; Lanes 6 to 9: 25, 27, 30 and 32 cycles of ascB expression in CP12CHBASC30; Lanes 10 to 13: 25, 27, 30 and 32 cycles of ascB expression in CP12CHBASC/ yebK-; and Lanes 14 to 17: 25, 27, 30 and 32 cycles of ascB expression in CP12CHBASC30/ yebK-;

Fig. 21 shows growth rate of CP12ASC/yebK- on cellobiose.

Fig. 22 shows specific activities of AscB using p-Nitro Phenyl /^-cellobiose as a substrate. DETAILED DESCRIPTION OF THE INVENTION

Hereinafter, the terms used herein are defined.

The term "operon" as used herein refers to the functioning unit of a genomic DNA containing a cluster of genes under the control of a single regulatory signal or promoter. E ach structure and function of "chb operon" and "asc operon" herein are well known in the art.

The term "promoter" as used herein refers to a region of DNA that facilitates the transcription of a particular gene. In addition, "cryptic promoter" refers to a promoter which is not able to serve transcriptional functions owing to various reasons, whereas "active promoter" refers to a promoter that can serve transcriptional functions. Examples of "active promoter" include "inducible promoter" and "constitutive promoter." "Inducible promoter" refers to a promoter which can be induced by the presence or absence of certain factors, and "constitutive promoter" refers to an unregulated promoter that allows for continuous transcription of its associated gene, which can be used interchangeably with the term "constitutive promoter" or "promoter for constitutive expression." The cryptic promoters of chb operon and asc operon in the present invention are well known in the art.

The present invention provides a mutant microorganism prepared by introducing to a wild-type microorganism a mutation selected from:

(a) replacement of the cryptic promoter of chb operon with an active promoter;

(b) replacement of the cryptic promoter of asc operon with an active promoter; and

In one embodiment of the present invention, there is provided a mutant microorganism which is prepared from a wild-type microorganism by replacing the cryptic promoter of chb operon with an active promoter. The wild-type microorganism may be E. coli or other microorganisms having a genome which shares 70% or more homology with that of E. coli, for example, Salmonella, but not limited thereto.

The replacement process of the cryptic promoter of chb operon with an active promoter, as described in Fig. 1 , can be carried out via Splice Overlap Extension PCR and using λ-Red recombination system, or any other alternative method known to those skilled in the art. The cryptic promoter of chb operon may have the nucleotide sequence of SEQ ID NO: 1 ; the active promoter used in this present invention may be any promoter known in the art to allow inducible or constitutive transcription of specific genes. In an exemplary embodiment of the present invention, the active promoter may have the nucleotide sequence of SEQ ID NO: 2. The promoter having the nucleotide sequence of SEQ ID NO: 2 is CP 12 promoter as disclosed in Jensen PR et al, Appl. Environ. Microbiol. 64(1), 82-87, 1998, and is reported to have β- galactosidase activity of 101 miller units in E. coli. In another embodiment of the present invention, there is provided a mutant microorganism which is prepared from a wild-type microorganism by replacing the cryptic promoter of asc operon with an active promoter. The replacement process of the cryptic promoter of asc operon with a well-known active promoter, as described in Fig. 2, can be carried out via Splice Overlap Extension (SOE) PCR and using λ-Red recombination system, or any other alternative method known to those skilled in the art. The cryptic promoter of asc operon may have the nucleotide sequence of SEQ ID NO: 3; the active promoter used in the present invention may be any promoter known in the art to allow inducible or constitutive transcription of specific genes. In an exemplary embodiment of the present invention, the active promoters may have the nucleotide sequence of SEQ ID NO : 2.

In another embodiment of the present invention, there is provided a mutant microorganism which is prepared from a wild-type microorganism by replacing the cryptic promoters of chb operon and asc operon with active promoters.

The active promoters of mutant microorganism allow activation of one or more cryptic genes in chb operon and/or asc operon, conferring an efficient cellobiose utilization phenotype. The mutant microorganism of the present invention can be further modified by:

(d) mutation of yebK gene, wherein an intact protein is not expressed from the mutated yebK gene. The yebK gene is also known as hexR and was registered in GenBank under Accession No. NC_000913.2 (EG12860; EcoCyc; M853; ECK1854). Th e nucleotide sequence of yebK gene is set forth in SEQ ID NO: 7, and the amino acid sequence of YebK protein is set forth in SEQ ID NO: 8.

The mutant microorganism of the present invention exhibits improved cellobiose utilization and simultaneous utilization of other sugars (such as xylose, mannose, galactose and arabinose) owing to the mutation of yebK gene from which an intact protein is not expressed. The mutation may include any mutation whereby no YebK protein is expressed. In an exemplary embodiment of the present invention, such mutation may be carried out by one or more point mutations. Further, in another exemplary embodiment of the present invention, such mutation may be carried out by one or more deletions. Examples of point mutations include CP12CHBASC30 strain in accordance with the present invention. In the CP12CHBASC30 strain, a 240^th nucleotide in the yebK gene represented by SEQ ID NO: 7 is substituted with a A instead of a T (see SEQ ID NO: 9), forming a termination codon and consequently producing only N-terminal region of YebK protein. Thus, yebK gene point mutation improves cellobiose utilization of microorganisms and also allows them to utilize both cellobiose and xylose simultaneously (see Fig. 3). Meanwhile, examples of deletion mutation in the present invention include CP12CHBASCyebK- and CP12CHBASC30yebK- strains. The yebK genes in these strains are completely deleted and thereby the strains can have improved cellobiose utilization and simultaneous utilization of other sugars (e.g., xylose, mannose, galactose and arabinose) (see Figs. 5 and 8). Therefore, the mutation of yebK gene activates metabolic pathway of cellobiose, pentose phosphate pathway and metabolic pathway of hexose. The term "sugar" as used herein refers to cellobiose, xylose, glucose, mannose, galactose, arabinose, etc.

In another embodiment of the present invention, the mutant microorganism may be subjected to evolutionary adaptation by being cultured in a cellobiose minimal medium for at least 30 days. The term "cellobiose minimal medium" refers to a medium containing cellobiose as the only carbon source. Preferably, it may be an M9 minimal medium supplemented with 2 mM MgS0₄, 0.1 mM CaCl₂ and 1 g/L to 8 g/L of cellobiose, but not limited thereto. Moreover, the adaptation period shall be minimal adaptation period that may affect utilization of sugars including xylose and cellobiose, which may exceed 30 days. In an exemplary embodiment, the adaptation period may be 10 to 90 days.

Conventional wild-type microorganisms, including wild-type E. coli cannot utilize cellobiose, and publicly known mutant microorganisms cannot also utilize cellobiose and xylose simultaneously due to carbon catabolite repression (CCR), causing difficulties in production of various chemicals such as, amino acids, biofuels, biopolymers, bioalcohols, recombinant proteins, and the others. On the contrary, the mutant microorganism of the present invention is capable of utilizing cellobiose (one of major saccharides of lignocelluloses biomass) and other sugars (such as xylose, mannose, galactose and arabinose) simultaneously, which is advantageous in production of aforementioned chemicals, because it can improve fermentation efficiency, production yield and costs.

Meanwhile, the present invention provides a method for preparing a mutant microorganism, which comprises:

(a) replacing one or more cryptic promoters of chb operon and asc operon with one or more active promoters.

The replacement process of promoter is the same as stated above.

In one embodiment of the present invention, the method may further comprise:

(b) mutating yebK gene, wherein an intact protein is not expressed from the mutated yebK gene.

The mutation process of yebK gene is the same as stated above.

In another embodiment of the present invention, the method may further comprise:

(c) culturing the mutant microorganism in a cellobiose minimal medium for at least 30 days.

Furthermore, the present invention provides a method for producing biofuels, physiologically active materials, medicinal materials or industrial chemicals by employing the mutant microorganism according to the present invention. Biomass as stated above may preferably be a cellulosic biomass, more preferably lignocellulosic biomass. Processes of biofuel production from biomass are well known to those skilled in the art, and the present invention includes using the mutant microorganism of the present invention in enzymatic saccharification and fermentation process. In one aspect of the present invention, the mutant microorganism according to the present invention can be used in the saccharification process instead of saccharifying enzyme (β-glucosidase) in the saccharification process. Further, in another aspect of the present invention, the mutant microorganism of the present invention can be used in the fermentation process. Moreover, the mutant microorganism according to the present invention can be used in simultaneous saccharification and co-fermentation (SSF) which carry out both saccharification and fermentation in one reactor especially fermentation of both pentose and hexose sugars in the same reactor.

Furthermore, the mutant microorganism according to the present invention can be used to produce various chemicals such as amino acids, biofuels, biopolymers, bioalcohols and recombinant proteins. EXAMPLES

Hereinafter, the present invention is described in more detail. The following Examples are given for the purpose of illustration only, and are not intended to limit the scope of the invention.

Example 1 : Preparation of modified E. coli whose cryptic promoter of chb operon is replaced with active promoter

As described below, a mutant E. coli was prepared from wild-type E. coli by replacing the cryptic promoter of chb operon with a constitutive promoter (CP 12), a kind of active promoter, and the mutant E. coli was designated "CP12CHB".

The only cryptic promoter (SEQ ID NO: 1) of chb operon on E. coli MG1655 chromosome was replaced with a synthetic constitutive promoter, CP 12 promoter (SEQ ID NO: 2) by using λ-Red recombination system (Datsenko et al, Proceedings of the National Academy of Sciences of the United States of America, 97(12), 6640- 6645, 2000). The CP 12 promoter is described in Jensen PR et al, Appl. Environ. Microbiol. 64(1), 82-87, 1998), and is reported to have β-galactosidase activity of 101 miller unit in E. coli.

Specifically, for promoter replacement, two overlapping fragments were amplified via Splice Overlap Extension (SOE) PCR to allow the CP 12 promoter to be connected with the kanamycin cassette, as described in Datsenko et al. Fragment 1 has the constitutive CP 12 promoter in the downstream region of chb operon by using three SOEing CP12 promoters (SEQ ID NOs: 4 to 6) listed in the TABLE 1 and carrying a homologous sequence that can be connected to Fragment 2 in the front region of the CP 12 promoter. Fragment 2 has the kanamycin cassette from pKD13 with an overhang that is homologous to the upstream region of the endogenous promoter in chb operon and it has a homologous sequence that can be connected to Fragment 1. Th e SOE PCR was conducted under the following conditions: 98 ^°C for 3 min; 30 cycles of 95 ^°C for 30 sec, 50~60^°C for 30 sec and 72 ^°C for 2 min. The process is briefly described in Fig. 1, and SOEing CP promoters and plasmids used in the process are listed in the Table 1.

[Table 1 ]

Cells carrying the λ-Red system under araBAD promoter (pKD46) were induced with 10 mM arabinose, made electrocompetent and transformed with the PCR products. Colonies carrying kanamycin resistance were selected, then PCR-amplified and sequenced to confirm site specific insertions and deletions. The strain constructed via aforementioned process was designated "CP12CHB". Example 2: Preparation of modified E. coli whose cryptic promoter of asc operon is replaced with active promoter As described below, a mutant E. coli was prepared from wild-type E. coli by replacing the cryptic promoter of asc operon with a constitutive promoter (CP 12), a kind of active promoter, and the mutant E. coli was designated "CP 12 ASC".

The only cryptic promoter (SEQ ID NO: 3) in asc operon found on chromosome of E. coli MG1655 was replaced with the synthetic constitutive promoter, CP 12 promoter (SEQ ID NO: 2), in a similar manner with Example 1.

Specifically, for promoter replacement, two overlapping fragments were amplified via Splice Overlap Extension (SOE) PCR to allow the CP 12 promoter to be connected with the kanamycin cassette, as described in Datsenko et al. Fragment 1 has the constitutive CP 12 promoter in the downstream region of asc operon by using three SOEing CP12 promoters (SEQ ID NOs: 4 to 6) listed in the TABLE 1 and carrying a homologous sequence that can be connected to Fragment 2 in the front region of the CP 12 promoter. The SOE PCR was conducted under the following conditions: 98 ^°C for 3 min; 30 cycles of 95 ^°C for 30 sec, 50-60 ^"C for 30 sec and 72 ^°C for 2 min. The process is briefly described in Fig. 2, and SOEing CP promoters and plasmids used in the process are listed in the Table 1.

Cells carrying the λ-Red system under araBAD promoter (pKD46) were induced with 10 mM arabinose, made electrocompetent and transformed with the PCR products. Colonies carrying kanamycin resistance were selected, then PCR-amplified and sequenced to confirm site specific insertions and deletions. The strain obtained by transformation with the PCR product was designated "CP 12 ASC".

Example 3: Preparation of modified E. coli whose cryptic promoters of chb operon and asc operon are replaced with active promoters As described in Example 1 and 2, a mutant E. coli was prepared from wild-type

E. coli by replacing the cryptic promoters of chb operon and asc operon with constitutive promoters, and the mutant E. coli was designated "CP12CHBASC". Comparative Example 1: Preparation of modified E. coli with mutated cAMP- CRP*

In order to obtain strains with crp* gene (a mutated form of crp gene), the crp gene of the "CP12CHBASC" strain from Example 3 was deleted according to Datsenko et ah, and the crp* gene was generated by SOE-PCR (127^th amino acid ' in CRP gene of E. coli strain W3110 was replaced with T). Then, the crp* gene was inserted to the site where the crp gene were removed via the aforementioned replacement method as in Examples 1 or 2. Strains with crp* were isolated based on the fact that mutant strains with crp* exhibit high growth rate compared to strains with crp gene deleted, and were confirmed by PCR amplification and sequencing of DNA. The confirmed strain was designated "CP12CHBASC/CRP*".

Example 4: Constitutive expression of modified E. coli (1) β-Glucosidase assay was performed on the modified E. coli CP12CHB, CP12ASC and CP12CHBASC prepared in Examples 1 to 3 to confirm constitutive expression. In brief, the strains were cultured in LB medium at 37^°C overnight, respectively. Then, 2 ml of the cell was lysed and suspended in 200 μΐ. of 50 mM sodium phosphate buffer (pH 7.0). 100 μ]_, of this crude cell extract was incubated with 400 of 10 mM /?-nitrophenyl- -glucopyranoside (PNPG) at 37 ^°C for 2 hours. 1 ml of 1M Na₂C0₃ was added thereto to stop the reaction and the absorbance was measured at 410 nm. One unit of the enzyme was defined as the amount of enzyme that liberated 1 μΜ of 7-nitrophenol per minute. The absorbance was measured using a Biochrom Libra S22 spectrophotometer. The measurement was repeated three times and the results are shown in Fig. 3.

As shown in Fig. 3, it was confirmed that the strains with promoter replacement can constitutively express β-glucosidase differently from wild-type MG1655. In particular, the strain whose cryptic promoters of both chb and asc operons are replaced showed the highest constitutive expression.

Example 5: Constitutive expression of modified E. coli (2) β-Glucosidase assay was performed on the modified E. coli "CP12CHBASC" prepared in Example 3 to compare constitutive expression in different media. Th e experiment was the same as in Example 4, and as media, LB medium, M9 medium supplemented with glucose, and M9 medium supplemented with cellobiose were used. The results are shown in Fig. 4.

As shown in Fig. 4, it was confirmed that β-glucosidase is constitutively expressed with the aid of the constitutive promoter, regardless of types of media.

Example 6: Growth rate of modified E. coli

The "CP12CHB" and "CP12CHBASC" prepared in Examples 1 and 3, and wild type MG1655 were tested for their growth rates. The "CP12CHB", "CP12CHBASC" and wild-type MG1655 were cultured in a cellobiose minimal medium containing 4 g/L of cellobiose, and another wild-type MG1655 was cultured in a glucose minimal medium containing 4 g/L of glucose, and the growth rates were assayed according to the culture period.

The results are shown in Fig. 5. As shown in Fig. 5, the wild-type MG1655 could not grow in a cellobiose minimal medium, whereas the strains with promoter replacement showed steady growth according to the culture period. The results indicate that the promoter replacement of chb and/or asc operon can contribute to enhance the utilization of cellobiose.

Example 6: Cellobiose and xylose utilization of modified E. coli The "CP12CHBASC" obtained in Example 3 and "CP12CHBASC/CRP*" obtained in Comparative Example 1 were assayed for cellobiose and xylose utilization. Each strain was seeded into 50 ml of a M9-minimal medium containing cellobiose (1 g/L) and xylose (1 g/L). The cultured medium was collected at a predetermined time intervals and the residual concentrations of cellobiose and xylose were measured using a Shimadzu HPLC station equipped with HPX-87P (Bio-Rad) column and refractive index detector (Shimadzu). HPLC-grade water was used as mobile phase at the flow rate of 0.6 mL/min. The oven temperature was set to 80 ^°C . A standard curve was determined based on the measurements on different concentration of xylose and cellobiose.

The results are shown in Fig. 6. The results of strains CP12CHBASC and CP12CHBASC/CRP* are found in Figs. 6A and 6B, respectively where residual concentrations of cellobiose (diamond) and xylose (rectangle) are reported.

As shown in Fig. 6 A, the CP12CHBASC strain was unable to utilize cellobiose in the presence of xylose, which indicates that carbon catabolite repression is still maintained in spite of constitutive expression of chb and asc operons. Meanwhile, when wild-type crp gene of CP12CHBASC was replaced with modified crp {crp*), as shown in Fig. 6B, the utilization rate of xylose was reduced, making cellobiose more preferred carbon source.

The results show that constitutive expression of chb and asc operons or mutation of crp gene was not sufficient enough to eliminate carbon catabolite repression completely. Example 7: Preparation of modified E. co/i via evolutionary adaptation

The strain prepared in the Example 3 was serially sub-cultured every day in a cellobiose minimal medium while shaking at 200 rpm at 37 ^°C fo r 30 days. When the culture medium reached OD₆₀₀ of 1.0, the cells were transferred into a fresh medium and cultured. The strain prepared above was designated "CP12CHBASC30".

Example 8: Cellobiose and xylose utilization of modified E. coli

The utilization rate of xylose and cellobiose of "CP12CHBASC" strain obtained in Example 3 was compared with "CP12CHBASC" strain obtained in Example 7. In compliance with theoretical yields of intracellular metabolites, xylose was used at a concentration of 10 g/L whereas cellobiose was used at a concentration of 4 g/L. The residual concentrations of xylose and cellobiose were determined with varying incubation periods, as in Example 6.

The results are shown in Fig. 7. The utilization rate of xylose and cellobiose are found in Figs. 7A and 7B, respectively where strains of CP12CHBASC (rectangle) and CP 12CHB ASCK30 (circle) are reported.

As shown in Fig. 7, xylose utilization rate of both strains were similar. However, cellobiose utilization rate of CP12CHBASC30 was remarkably higher than that of CP12CHBASC. The results indicate that cellobiose utilization of E. coli can be enhanced through evolutionary adaptation as shown in Example 7. Example 9: Cellobiose and xylose utilization of modified E. coli

In order to test simultaneous utilization of cellobiose and xylose in CP12CHBASC30 obtained in Example 7, the strain was cultured in media containing different concentrations of cellobiose and xylose and its utilization rate was measured. Three different media were used for the test: A) 2 g/L cellobiose and 2 g/L xylose; B) 3 g/L cellobiose and 2 g/L xylose; C) 1 g/L cellobiose and 1 g/L xylose. The residual concentrations of xylose and cellobiose were determined with varying incubation periods, as in Example 6.

The results are shown in the Fig. 8. The residual concentrations of xylose (rectangle) and cellobiose (diamond) in three different media were reported: Fig. 8A cellobiose 2 g/L, xylose 2 g/L; Fig. 8B cellobiose 3 g/L, xylose 2 g/L, Fig. 8C cellobiose 1 g/L, xylose 1 g/L.

As shown in Fig. 8, the CP12CHBASC30 of the present invention was shown to be capable of utilizing xylose and cellobiose simultaneously regardless of the concentrations of xylose and cellobiose

Example 10: Gene analysis of modified E. coli CP12CHBASC30

The modified strain CP12CHBASC30 of Example 7 was subjected to whole genome resequencing in Macrogen Inc. (Korea) and its gene sequence was compared with that of wild type E. coli MG1655.

It was found in the analysis that base 240 of gene yebK of the wild-type E. coli was changed from T to A via a point mutation {see SEQ ID NO: 9) which caused a codon change from TAT (codon for tyrosine) to TAA (end codon). Thi s leads to a formation of a small protein consists of 79 amino acids {see SEQ ID NO: 10) instead of a YebK protein (SEQ ID NO: 8) with approximately 3,190 Da. The above result suggests that mutation of yebK gene can affect carbon metabolism in E. coli. Example 11: Preparation of modified E. coli with promoter replacement and yebK deletion (CP12CHBASCyebK-)

Based on the result of Example 10, a modified E. coli strain was obtained from the strain CP12CHBASC of Example 3, by deleting entire yebK gene (Accession Numbers: EG12860 (EcoCyc), M853, ECK1854) in order to examine the effect of mutation in yebK gene on carbon metabolism. The new strain thus obtained was designated "CP12CHBASCyebK-".

Specifically, yebK delFP (forward primer, SEQ ID NO: 11) complementary to a part starting from base 52 and yebK delRP (reverse primer, SEQ ID NO: 12) complementary to a part starting from base 948 were constructed, and PCR amplification, as described in Fig. 9, was carried out to replace yebK gene with kanamycin cassette. This gene substitution was confirmed by sequence analysis using forward primer (SEQ ID NO: 13) and reverse primer (SEQ ID NO: 14). The resulting E. coli with kanamycin cassette was then transformed with plasmid DNA pCP20, which expresses FLP recombinase, thereby removing kanamycin cassette via FLP recombination.

Example 12: Preparation of modified E. coli with promoter replacement, adaptation in cellobiose minimal medium and yebK deletion (CP12CHBASCyebK-)

The process of Example 11 was repeated except for using CP12CHBASC30 strain instead of CP12CHBASC strain to obtain strain "CP12CHBASC30yebK-" whose yebK gene is deleted.

The modified E. coli strains obtained in Examples 3, 7, 1 1 and 12 and their descriptions are summarized in Table 2 below.

Modified CP12CHBASC strain adapted in a

7 CP12CHBASC30

cellobiose minimal medium for 30 days

Modified CP12CHBASC strain with yebK gene

1 1 CP12CHBASCyebK- deletion

Modified CP12CHBASC30 strain withyebK

12 CP12CHBASC30yeb - gene deletion

Example 13: Cellobiose and xylose utilization of modified E. coli Utilization rates of cellobiose and xylose of modified E. coli strains

CP12CHBASC, CP12CHBASC30, CP12CHBASCyebK-, and

CP 12CHBASC30yebK- obtained in Examples 3, 7, 11 and 12, respectively, were examined and compared. Based on the theoretical yield of cellular metabolites, concentration of 2 g L xylose and 1 g/L cellobiose were used. Residual concentrations of xylose and cellobiose were measured based on incubation time.

The measurement results are shown in Fig. 10. Figs. 10A, 10B, IOC, and 10D show the results of strain CP12CHBASC, CP12CHBASCyebK-, CP12CHBASC30, and CP12CHBASC30yebK-, respectively. In each figure, -♦- denotes concentration of cellobiose (In %); xylose; and - A-, optical density (OD).

As can be seen in Fig. 10, xylose and cellobiose utilization rates were higher in strains CP 12CHB ASC30, CP12CHBASCyebK- and CP12CHBASC30yebK- than in strain CP12CHBASC.

Example 14: Cellobiose and other sugars utilization of modified E. coli

Utilization rates of cellobiose and other sugars of CP12CHBASC, CP12CHBASC30 and CP12CHBASCyebK- obtained in Examples 3, 7 and 1 1 , respectively, were examined and compared. Experimental method was the same as in Example 13; and residual concentrations of cellobiose and other sugars were measured based on incubation time.

The results of simultaneous utilization rates of CP12CHBASC, CP12CHBASC30 and CP12CHBASCyebK- are shown in Figs. 1 1, 12 and 13, respectively. As can be seen in the above results, the simultaneous utilization rate of cellobiose and other sugars (glucose, mannose, galactose and arabinose) were remarkably enhanced in strains CP12CHBASC30 and CP12CHBASCyebK- than in strain CP12CHBASC. Test result proves that activation of cellobiose metabolism, pentose phosphate pathway and hexose phosphate pathway by a mutation of yebK gene allowed enhanced simultaneous utilization rate of cellobiose and other sugars.

Example 15: Growth rate of modified E. coli under cellobiose and xylose as carbon sources

In order to test growth rates under cellobiose and xylose as carbon sources, modified strains CP12CHBASC, CP12CHBASC30, CP12CHBASCyebK- and CP12CHBASC30yebK- obtaine d in Examples 3, 7, 11 and 12, respectively, were cultured separately on a medium containing either cellobiose or xylose. Culture process was conducted in the same way as in Example 13.

Growth curves on cellobiose and xylose were shown in Fig. 14A and Fig. 14B, respectively. A s shown in Fig. 14 A, when cellobiose was used as a carbon source, CP12CHBASCyebK- strains grew faster than CP12CHBASC strains and CP12CHBASC30yebK- strains grew faster than CP12CHBASC30 strains. Similarly, as shown in Fig. 14B, when xylose was used as a carbon source, strains CP12CHBASC and CP12CHBASC30 showed similar growth as wild-type, whereas growth of strains CP12CHBASCyebK- and CP12CHBASC30yebK- began after a long lag phase, indicating the direct role of yebK in regulating pentose utilization pathway or even the central carbon metabolism.

The results above demonstrate enhanced utilization rate of cellobiose as well as simultaneous utilization rate of cellobiose and xylose is achievable via deletion of yebK gene.

Example 16: Growth rate of JET. coli under xylose as a carbon source

In order to examine the effect of yebK gene deletion on metabolism of xylose, a modified E. coli "CP12CHBASC/CP25XylAB/CP6XylFGH" was prepared by replacing inducible promoter XylAB/XylFGH (SEQ ID NO: 15) in E. coli with a constitutive promoter CP25XylAB/CP6XylFGH (SEQ ID NO: 16) which is related with xylose transport and metabolism. Promoter replacement process was conducted in the same way as Example 1, and the specific position of gene replacement is illustrated in Fig. 15. Forward primer (SEQ ID NO: 17) and reverse primer (SEQ ID NO: 18) were used for the above replacement. Meanwhile, the strain CP12CHBASCyebK- prepared in Example 1 1 was subjected to the same process of promoter replacement to prepare modified E. coli "CP12CHBASCyebK- /CP25XylAB/CP6XylFGH". In order to test the growth rates of two above-mentioned strains under xylose as a carbon source, the strains were cultured on media containing 4 g/L of xylose. The results are shown in Fig. 16. As shown in Fig. 16, the growth rate of the strain whose yebK gene was deleted (CP12CHBASCyebK-/CP25XylAB/CP6XylFGH) was faster than the strain CP12CHBASC/CP25XylAB/CP6XylFGH. Thus, the increased growth rate caused by yebK gene deletion shows that yebK gene activates pentose phosphate pathway and involved in xylose transport and metabolism. Furthermore, it can be concluded that the deletion of yebK gene allowed an increase of cellobiose and xylose metabolism through the regulation of pentose phosphate pathway, which eventually lead to simultaneous utilization of cellobiose and xylose.

Example 17: Construction of plasmid expressing yebK

In order to perform a complementation test, a plasmid was constructed that expresses YebK from a tetracycline promoter. T o do that, yebK gene was amplified from the genomic DNA of MG1655 with the primers set forth in SEQ ID NOs: 19 and 20. It was then cloned into the pZB plasmid using the restriction enzymes Pstl and Nhel. The plasmid thus obtained was designated "pZB-yebK," and represented in Fig. 17. Example 18: Complementation of yebK

The plasmid "pZB-yebK" constructed in Example 17 was transformed into the mutant microorganism CP12CHBASC/yebK-. The cells (CP12CHBASC/yebK-/pZB- yebK) were grown on a cellobiose minimal medium supplemented with varying concentrations of tetracycline ranging from 0 ng/mL to 10 ng/mL. Growth on cellobiose was reduced with increasing concentration of tetracycline, indicating that yebK was directly regulating cellobiose metabolism (Fig. 18).

Example 19: Microarray analysis of CP12CHBASC and CP12CHBASC30

Microarray analysis was performed to understand the global gene expression changes between the mutant microorganisms CP12CHBASC and CP12CHBASC30. The GE microarray, 3*20K (E. coli strain K12 MG1655) platform was used to analyze the mRNAs isolated from CP12CHBASC and CP12CHBASC30 grown on cellobiose minimal media. The results are shown in Fig. 19. Microarr ay data indicate that there was no huge difference in the expression of chb operon proteins between the two mutant strains. However , there was a huge difference in the expression level of AscB protein.

Example 20: RT-PCR for determination of ascB expression level

RT-PCR for ascB was performed with the cDNA made from the total RNA isolated from the mutant organisms CP12CHBASC, CP12CHBASC/yebK-, CP12CHBASC30 and CP12CHBASC30/yebK- growing on cellobiose minimal media and using the primers in SEQ. ID NOs: 21 and 22. T otal RNA was isolated from the mutant strains CP12CHBASC, CP12CHBASC30, CP12CHBASC/yebK- and CP12CHBASAC30/yebK-. Then, cDNA was synthesized from the total RNA using random hexamers and MuMLV reverse transcriptase. PCR was performed for the cDNA obtained as above and samples were withdrawn at 25, 27, 30 and 32 PCR cycles and run on 0.7% agarose gel.

Consistent with the microarray data, RT-PCR analysis indicates that the ascB expression level was higher in the mutant microorganisms CP12CHBASC/yebK-, CP12CHBASC30 and CP12CHBASC30/yebK- than in the mutant microorganism CP12CHBASC (Fig. 20). This might indicate that YebK is directly or indirectly regulating ascB expression. Y ebK might be directly controlling the promoter of ascB or might be controlling global RNAses and sRNAs, which in turn would be controlling ascB.

Example 21: Growth rate of CP12ASC/yebK- on cellobiose Since ascB expression level was found to be higher in yebK deleted strains, it was assumed that deletion of yebK would help CP12ASC mutants to grow on cellobiose. Henc e, yebK gene was deleted in the mutant microorganism CP12ASC in a manner similar to that described in example 11, and the resulting CP12ASC/yebK- and CP12ASC was compared for their growth rates (Fig. 21). The CP12ASC/yeb - was capable of growing on cellobiose minimal medium.

Example 22: Specific activity of ascB

The expression level of ascB in CP12ASC was very low and hence the enzyme specificity could not be determined without strain as in example 4. Ho wever, ascB expression level was several folds higher in j>e6A>deleted strains and hence the strain CP12ASC/yebK- was used to determine the enzyme activity, β -Glucosidase assay was performed on the modified E. coli CP12ASC and CP12ASC/yebK- similar to that in Example 4. Exoglucanase assay was performed with p-Nitro phenyl cellobioside as a substrate. In brief, the strains were cultured in LB medium at 37 ^°C overnight, respectively. Then, 2 ml of the cell was lysed and suspended in 200 ih of 50 mM sodium phosphate buffer (pH 7.0). 100 \L of this crude cell extract was incubated with 400 \L of 10 mM p-Nitro phenyl cellobioside (PNPG) at 37 ^°C for 2 hours. 1 ml of 1M Na₂C0₃ was added thereto to stop the reaction and the absorbance was measured at 410 nm. One unit of the enzyme was defined as the amount of enzyme that liberated 1 μΜ of /7-nitrophenol per minute. The absorbance was measured using a Biochrom Libra S22 spectrophotometer.

Enzyme from CP12ASC/yebK- had activity against both PNPG and PNPC indicating that apart from the assigned /?-glucosidase activity the strain might also have an exoglucanase activity capable of cleaving cellulo-oligosaccharides (Fig. 22).

Claims

What is claimed is:

1. A mutant microorganism prepared by introducing to a wild-type microorganism a mutation selected from:

(a) replacement of the cryptic promoter of chb operon with an active promoter;

2. The mutant microorganism of claim 1, further modified by:

(d) a mutation of yebK gene, wherein an intact protein is not expressed from the mutated yebK gene.

3. The mutant microorganism of claim 1, wherein the wild-type microorganism is E. coli.

4. The mutant microorganism of claim 1, wherein the cryptic promoter of chb operon has the nucleotide sequence of SEQ ID NO: 1 and the cryptic promoter of asc operon has the nucleotide sequence of SEQ ID NO: 3.

5. The mutant microorganism of claim 1, wherein the active promoter is an inducible promoter or a constitutive promoter.

6. The mutant microorganism of claim 1, wherein the active promoter has the nucleotide sequence of SEQ ID NO: 2.

7. The mutant microorganism of claim 2, wherein the mutation of yebK gene is a point mutation or a deletion of entire yebK gene.

8. A method for preparing a mutant microorganism, which comprises:

9. The method of claim 8, which further comprises:

10. The method of claim 8, which further comprises:

(c) culturing the mutant microorganism in a cellobiose minimal medium.

11. The method of claim 8, wherein the cryptic promoter of chb operon has the nucleotide sequence of SEQ ID NO: 1 and the cryptic promoter of asc operon has the nucleotide sequence of SEQ ID NO: 3.

12. The method of claim 8, wherein the active promoter is an inducible promoter or a constitutive promoter.

13. The method of claim 8, wherein the active promoter has the nucleotide sequence of SEQ ID NO: 2.

14. The method of claim 9, wherein the mutation of yebK gene is a point mutation or a deletion of entire yebK gene.

15. A method for producing biofuels, physiologically active materials, medicinal materials or industrial chemicals from biomass by employing a mutant microorganism of any one of claims 1 to 7.