Mutant strain <i>Clostridium thermocellum </i>for producing cellulase and xylanase and preparation method thereof

Abstract

The present invention relates to a novel mutant strain Clostridium thermocellum M2_15-C8 and a genetic modification process of said bacteria, wherein the mutant strain according to this invention can produce cellulase and xylanase more than the wild type. Moreover, the obtained enzymes can be used to digest the pretreated bagasse to further produce sugars effectively.

Claims

1. A mutant strain Clostridium thermocellum, wherein said mutant strain Clostridium thermocellum is Clostridium thermocellum M2_15-C8, accession number NITE ABC-02390.

2. A genetic modification process to produce the mutant strain Clostridium thermocellum according to claim 1, wherein said genetic modification process comprises applying an ultraviolet radiation intensity from 40 to 100 microwatts per square centimeter to the wild type Clostridium thermocellum for 10 to 120 minutes.

3. The genetic modification process according to claim 2, wherein said genetic modification process comprises applying an ultraviolet radiation intensity from 40 to 80 microwatts per square centimeter to the wild type Clostridium thermocellum for 15 to 60 minutes.

4. The genetic modification process according to claim 2, wherein said genetic modification process is operated under anaerobic conditions.

5. The genetic modification process according to claim 2, wherein said genetic modification process is operated twice.

6. A production process of cellulase and xylanase comprising a step of cultivating of the mutant strain Clostridium thermocellum according to claim 1 in a carbon source, wherein the bacteria to carbon source ratio is in a range of 0.1 to 1.0 g bacteria to g carbon source under a temperature of 55-65° C. for 24-96 hours.

7. The production process of cellulase and xylanase according to claim 6, wherein the bacteria to carbon source ratio is in the range of 0.2 to 0.5 g bacteria tog carbon source.

8. The production process of cellulase and xylanase according to claim 6, wherein the carbon source is selected from cellulose powder, rice straw, bagasse, or a mixture thereof.

9. The production process of cellulase and xylanase according to claim 8, wherein the carbon source is bagasse.

10. The production process of cellulase and xylanase according to claim 6, wherein said production process is operated at a temperature of 60° C.

11. The production process of cellulase and xylanase according to claim 6, wherein said production process is operated in the range of 48-72 hours.

12. The production process of cellulase and xylanase according to claim 11, wherein said production process is operated for about 72 hours.

13. The production process of cellulase and xylanase according to claim 6, wherein said production process is operated under anaerobic conditions.

14. A method of saccharification of biomass, comprising contacting the biomass with an enzyme produced by the process of claim 6.

15. The method of claim 14 wherein the biomass is bagasse.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 shows the growth characteristic of microorgnaims and the remaining cellulose powder in medium tube of wild type Clostridium thermocellum KK8.3 strain and genetically modified strains.

(2) FIG. 2 shows the stability of cellulase and xylanase production from modified strain Clostridium thermocellum M2_15-C8 after inoculum till the 10.sup.th generations.

(3) FIG. 3 shows the growth characteristic of microorganisms and the remaining cellulose powder in medium tube of wild type Clostridium thermocellum strain and genetically modified M2_15-C8 strains.

(4) FIG. 4 shows the characteristic of proteins and enzymes produced by wild type Clostridium thermocellum strain and genetically modified M2_15-C8 strains: A) protein characters tested by sodium dodecyl sulphate polyacrylamide gel electrophoresis (SDS-PAGE) technique; B) cellulase characters tested by zymogram techniques; and C) xylanase characters tested by zymogram technique, wherein M means standard protein with known molecular weight and kDa means kilodalton.

(5) FIG. 5 shows glucose content obtained from digestion of bagasse treated with different methods using enzymes from mutant strain Clostridium thermocellum M2_15-C8.

DESCRIPTION OF THE INVENTION

Definitions

(6) Technical terms or scientific terms used herein have definitions as by an ordinary person skilled in the art unless stated otherwise.

(7) Any tools, equipment, methods, or chemicals named here mean tools, equipment, methods, or chemicals being used commonly by an ordinary person skilled in the art unless stated otherwise that they are tools, equipment, methods, or chemicals specific only in this invention.

(8) Use of singular noun or singular pronoun with “comprising” in claims or specification means “one” and including “one or more”, “at least one”, and “one or more than one”.

(9) All compositions and/or methods disclosed and claims in this application aim to cover embodiments from any action, performance, modification, or adjustment without any experiment that significantly different from this invention, and obtain with object with utility and resulted as same as the present embodiment according to an ordinary person ordinary skilled in the art although without specifically stated in claims. Therefore, substitutable or similar object to the present embodiment, including any little modification or adjustment that clearly seen by an ordinary person skilled in the art should be construed as remains in spirit, scope, and concept of invention as appeared in appended claims.

(10) Throughout this application, term “about” means any number that appeared or showed here that could be varied or deviated from any error of equipment, method, or personal using said equipment or method.

(11) Hereafter, the invention embodiments are shown without any purpose to limit any scope of the invention.

(12) The present invention relates to the Clostridium thermocellum M2_15-C8 strain being genetically modified by ultraviolet light induction in order to produce novel strain that capable for producing highly amount of cellulase and xylanase, including method of genetic modification and the use of obtained enzymes in saccharification of biomass.

(13) Clostridium thermocellum M2_15-C8 according to this invention was kept at NITE Patent Microorganisms Depositary (NPMD), Japan under the regulations of Budapest Treaty, wherein said strain was deposited on 19 Dec. 2016 under accession number NITE ABP-02390.

(14) Term “culture” used in this invention means including liquid culture or solid culture but not limited to the said methods as long as the strain according to this invention can be cultured.

(15) Term “saccharification” means the saccharification of cellulose and/or hemicellulose in the biomass to oligosaccharide, disaccharide, monosaccharide, or mixture thereof. In the same way, the saccharification of biomass includes the hydrolysis of glycosidic bond of poly-saccharide by cellulase and/or hemicellulase.

(16) In one embodiment, mutant strain Clostridium thermocellum is produced from ultraviolet light induced genetic modification of wild type Clostridium thermocellum, wherein the said mutant strain is Clostridium thermocellum M2_15-C8.

(17) In one aspect of the invention, the genetic modification process to obtain mutant strain Clostridium thermocellum can be performed by ultraviolet radiation with intensity from 40 to 100 microwatts per square centimeter to the wild type Clostridium thermocellum at the concentration of 0.1-1.0 grams per carbon source for the duration from 10 to 120 minutes.

(18) Preferably, theabove-mentioned genetic modification process may be operated by ultraviolet radiation intensity from 40 to 80 microwatts per square centimeter to the wild type Clostridium thermocellum from 15 to 60 minutes.

(19) In one aspect of the invention, the genetic modification process in order to obtain mutant strain Clostridium thermocellum is operated under anaerobic condition.

(20) In one aspect of the invention, the genetic modification process in order to obtain mutant strain Clostridium thermocellum is operated twice.

(21) In one aspect of the invention, the mutant strain Clostridium thermocellum M2_15-C8 obtained from the said process have nucleotide sequence of relevant gene related to the production of cellulase and xylanase groups and proteins related to transporting proteins and enzymes out of the cells different from the original as gene code: 111, 220, 419, 427, 442, 453, 850, 1252, 1257, 1305, 1456, 1529, 1884, 1902, 2246, 2479, 2611, 2654, 2701, 2854, and 2875.

(22) In one aspect of the invention, the culturing of bacteria for genetic modification process can be performed by culturing bacteria in basic medium having a carbon source concentration in a range of 0.5-1.0% (w/v) under anaerobic condition at the temperature in a range of 55 to 65° C., preferably 60° C., for 24-96 hours.

(23) In one aspect of the invention, the carbon source selected from, but not limited to cellulose powder, rice straw, bagasse, or mixture thereof. Preferably, the carbon source is cellulose powder.

(24) In one aspect of the invention, the air in prepared culturing medium is removed by adding carbon dioxide gas, and being sterilized at the temperature about 110-130° C., pressure of 10-20 psi, for 15-20 minutes before inoculation.

(25) In one aspect of the invention, the isolation of the genetically modified bacteria can be performed by: 1) culturing the genetically modified bacteria in basal medium at the conditions above-described; 2) diluting the cultured genetically modified bacteria; 3) transferring the diluted genetically modified bacteria to basal agar medium containing cellulose powder as carbon source, and then applying roll tube method and incubated at the temperature about 60° C. for about 24-48 hours; and 4) isolating the target colony wherein the isolated mutant strain Clostridium thermocellum M2_15-C8 is further cultured according to the culturing method above-described for further enzyme production.

(26) In one aspect of the invention, the production process of cellulase and xylanase from the mutant strain Clostridium thermocellum M2_15-C8 can be performed by culturing the mutant strain Clostridium thermocellum M2_15-C8 in culturing medium containing carbon source. The ratio of bacteria to carbon source is in a range of 0.1-1.0 g of bacteria to g of carbon source under temperature in a range of 55-65° C. for 24-96 hours.

(27) Preferably, the ratio of bacteria to carbon source is in the range of 0.2-0.5 g of bacteria to g of carbon source.

(28) Preferably, the culturing operation temperature of the mutant strain Clostridium thermocellum M2_15-C8 for enzyme production is 60° C.

(29) Preferably, the suitable culturing duration of the mutant strain Clostridium thermocellum M2_15-C8 for enzyme production is in the range of 48 to 72 hours. Most preferably, the suitable culturing duration is 72 hours.

(30) In one aspect of the invention, the carbon source concentration in the culturing medium is in a range of 1-3% (w/v).

(31) In one aspect of the invention, the culturing process of the mutant strain Clostridium thermocellum M2_15-C8 for enzyme production is operated under anaerobic condition.

(32) In one aspect of the invention, the culturing process of the mutant strain Clostridium thermocellum M2_15-C8 for enzyme production selected from, but not limited to rice straw, bagasse, and mixture of rice straw and bagasse. Preferably, the used carbon source is bagasse.

(33) In one aspect of the invention, bacteria can be isolated from culturing medium containing enzymes produced by bacteria by general isolation methods known by an ordinary person skilled in the art such as centrifugation, filtration, or relevant methods. The culturing liquid containing cellulase and xylanase can be used directly as crude enzyme.

(34) In one aspect of the invention, the culturing liquid containing cellulase and xylanase may be further purified by any methods known by an ordinary person skilled in the art, wherein it may be used two or more purification methods together.

(35) In one aspect of the invention, enzymes produced from the mutant strain Clostridium thermocellum M2_15-C8 comprising: 1) cellulolytic enzyme such as carboxy methyl cellulase, avicelase, cellobiohydrolase, and (3-glucosidase; and 2) xylanolytic enzyme such as xylanase, β-xylosidase, β-galactosidase, arabinofuranosidase, and acetylxylanesterase.

(36) In one aspect of the invention, enzymes produced from the mutant strain Clostridium thermocellum M2_15-C8 can be used in the saccharification of biomass, wherein the preferably biomass is bagasse.

(37) In one aspect of the invention, the biomass for saccharification may be in both wet and dry form.

(38) In one aspect of the invention, the biomass for saccharification may be subjected to the pretreatment process selected from steam explosion using base catalyst method (STEX), organic solvent separation method (FR), sodium hydroxide in acetone method (AC), and sodium methoxide in methanol method (MM), wherein two or more pretreatment methods can be used prior to the enzymatic saccharification.

(39) In one aspect of the invention, enzymes produced from the mutant strain Clostridium thermocellum M2_15-C8 may be used together with other enzymes as mixed enzymes in order to increase the saccharification performance of the biomass.

(40) The following parts aim for describing the embodiments of the invention only, not for limiting the scope of this invention in any way.

Example 1: The Genetic Modification of Clostridium thermocellum by Ultraviolet Induction and the Selection of the Mutant Strain that Produce High Amount of Cellulase and Xylanase

(41) Basal medium containing 0.045% (w/v) of dipotassium phosphate (K.sub.2 HPO.sub.4) and 0.045% (w/v) of potassium dihydrogen phosphate (KH.sub.2PO.sub.4), 0.09% (w/v) ammonium sulfate ((NH.sub.4).sub.2SO.sub.4), 0.09% (w/v) sodium chloride (NaCl), 0.018% (w/v) magnesium sulfate heptahydrate (MgSO.sub.4. 7H.sub.2O), 0.012% (w/v) calcium chloride hydrate (CaCl.sub.2. 2H.sub.2O), 0.4% (w/v) sodium carbonate (Na.sub.2CO.sub.3), and 0.4% (w/v) yeast extract was prepared in Hungate tube containing about 0.5-1.0% (w/v) cellulose powder as a carbon source. Then, the air in said culturing medium was removed by adding carbon dioxide and being sterilized at the temperature about 120-125° C., at the pressure of 15 psi for about 15-20 minutes. The wild type Clostridium thermocellum KK8. 3 was cultured in prepared culturing medium and incubated at the temperature of 60° C. for 24-72 hours until cellulose powder was digested more than 90% (w/v). The obtained cells were kept for further mutation.

(42) The obtained bacterium cells were placed under ultraviolet lamp at the intensity of 40-100 microwatts per square centimeter, with the distance from lamp of 10-30 cm for different durations from 10-120 min. Then, the radiated bacterium cells were transferred into basal medium tube containing 0.5-1.0% (w/v) cellulose powder as the carbon source and incubated at 60° C. for 24-48 hours. The obtained supernatant was tested for cellulase activity and xylanase activity and calculated for the increased enzyme activities comparing to the wild type.

(43) From table 1, it was found that the mutant strain Clostridium thermocellum M1_60 could produce cellulase and xylanase higher than wild type strain about 2 and 2.5 times, respectively. Moreover, the mutant strain Clostridium thermocellum M1_60 had stability and were able to retain their effectiveness for the production of cellulase and xylanase after 10 generations.

(44) Then, the mutant strain Clostridium thermocellum M1_60 were cultured in liquid basic medium containing cellulose powder as the carbon source and genetically modified with ultraviolet light according to conditions as above-described again. The growth of microorganisms and decreasing ratio of cellulose powder was shown in FIG. 1. The obtained supernatant was tested for cellulase activity and xylanase activity and calculated for the increased enzyme activities comparing the wild type and M1_60 strains. From table 1, it was found that the mutant strain Clostridium thermocellum M2_15 still capable of producing cellulase and xylanase higher than the wild type strain for 2 and 2.5 times respectively and were able to retain their effectiveness for the production of cellulase and xylanase after 10 generations.

(45) TABLE-US-00001 TABLE 1 Comparison of cellulase activity and xylanase activity of the Clostridium thermocellum KK8.3 wild type and genetically modified by UV light at different conditions UV radiation Enzyme activity Increase of enzyme UV time (unit/mL) production (times) radiation (min) Strain Generation Cellulase Xylanase Cellulase Xylanase No — KK8.3 — 0.29 0.43 1 1 radiation Cycle 1 60 M1_60 10 0.59 1.09 2.03 2.53 Cycle 2 15 M2_15 1 0.60 1.11 2.07 2.58 Cycle 2 30 M2_30 1 0.49 0.81 1.69 1.88 Cycle 2 45 M2_45 1 0.31 0.73 1.07 1.70 Cyc;e 2 60 M2_60 1 0.21 0.39 0.72 0.91

(46) For the isolation of the mutant strain, the mutant strain Clostridium thermocellum M2_15 were diluted under anaerobic condition. The diluted bacteria were transferred into basal medium agar containing cellulose powder as carbon source subjected to air removal according to the methods as above-described and subjected to roll tube method to form a thin film all over the tubes. Then, the obtained culturing tubes were incubated at the temperature of 60° C. for about 24-48 hours. Then, single colony was isolated and cultured in liquid basal medium under the conditions as above-described and the colony capable of fast digestion of cellulose resulting in lower cellulose than the wild type at the same culturing time was selected.

(47) From table 2, it was found that colony M2_15-C8 could digest cellulose powder faster than the wild type and produced cellulase and xylanase higher than the wild type for about 2 times and 4 times, respectively. Moreover, the Clostridium thermocellum M2_15-C8 were stable and could retain their productivity of cellulase and xylanase after 10 generations as shown in FIG. 2.

(48) TABLE-US-00002 TABLE 2 Comparison of cellulase and xylanase activities of Clostridium thermocellum KK8.3 wild type and mutant strains Enzyme activity Increase of enzyme production (unit/mL) (times) Strain Generation Cellulase Xylanase Cellulase Xylanase Original — 0.29 0.43 1 1 M1_60 10 0.59 1.09 2.03 2.53 M2_15 10 0.61 1.13 2.44 2.62 M2_15-C8 1 0.53 1.86 2.12 4.33 M2_15-C8 2 0.55 1.85 2.20 4.30 M2_15-C8 3 0.57 1.88 2.28 4.37 M2_15-C8 4 0.55 1.87 2.20 4.35 M2_15-C8 5 0.55 1.87 2.20 4.35 M2_15-C8 6 0.56 1.85 2.24 4.30 M2_15-C8 7 0.55 1.85 2.20 4.30 M2_15-C8 8 0.57 1.88 2.28 4.37 M2_15-C8 9 0.55 1.85 2.20 4.30 M2_15-C8 10 0.57 1.88 2.28 4.37

Example 2: Physical Characters of the Mutant Strain Clostridium thermocellum M2_15-C8

(49) The mutant strain Clostridium thermocellum M2_15-C8 were compared their physical characters with Clostridium thermocellum wild type. It was found that the mutant strain Clostridium thermocellum M2_15-C8 have a cream-yellow in colour whereas the wild type bacteria have a strong yellow as shown in FIG. 3. Moreover, the cellulose digestion rate of the mutant strain Clostridium thermocellum M2_15-C8 was faster than the wild type. The mutant strain could digest 1% (w/v) cellulose powder in basic medium for more than 90% within 48 hours, whereas the wild type took more than 48 hours for digestion under the same conditions.

Example 3: Study of Proteins and Cellulase and Xylanase Characters Produced from the Wild Type and Mutant Strain Clostridium thermocellum M2_15-C8

(50) The cellulase and xylanase were produced by culturing of the wild type and the mutant strain Clostridium thermocellum M2_15-C8 in liquid basal medium containing 1-3% (w/v) of bagasse as carbon source under anaerobic condition as above-described, following by the incubation at the temperature of 60° C. for 24-72 hours. The obtained supernatant was centrifuged at the speed higher than 8,000 rpm at the temperature of 4-10° C. for 10-20 minutes. Only the clear supernatant was concentrated by filtering through 3-10 kilodaltons membrane (Quix Stand Systems; GE life sciences) in order to obtain concentrate enzyme for further studies.

(51) From table 3, it was found that enzymes produced from wild type and the mutant strain Clostridium thermocellum M2_15-C8 containing cellulolytic enzymes such as 10.21 unit/mL carboxy methyl cellulase, 2.55 unit/mL avicelase, 4.34 unit/mL cellobiohydrolase, and 2.30 unit/mL β-glucosidase, and xylolytic enzymes such as 36.85 unit/mL xylanase, 0.17 unit/mL β-xylosidase, 0.31 unit/mL β-galactosidase, 0.36 unit/mL arabinofuranosidase, and 0.31 unit/mL acetylxylanesterase. Moreover, it was found that all of the mutant strains produced all enzymes higher than the wild type. Especially, xylanase can be produced at least 4 times higher and carboxy methyl cellulase and avicelase can be produced at least 2 times higher.

(52) FIG. 4 shows the comparison of protein characters produced by the wild type and the mutant strain Clostridium thermocellum M2_15-C8 using sodium dodecyl sulphate polyacrylamide gel electrophoresis (SDS-PAGE) method. It was found that at 20-250 kDa, enzymes produced by both strains had similar characters, which contain 14 proteins at 20, 22, 30, 35, 45, 50, 60, 70, 75, 80, 100, 125, 150, and 250 kDa. However, the intensity of proteins produced by both strains was different, which showed that protein amounts were different. FIG. 4a shows that the mutant strain Clostridium thermocellum M2_15-C8 produced more proteins at 30, 35, 45, 50, 60, 70, 100, and 125 kDa than the wild type.

(53) Moreover, from the comparison of cellulase and xylanase characters using zymogram method as shown in FIG. 4b, cellulase characters at 20-250 kDa were similar in both strains, but some cellulase produced by the mutant strain Clostridium thermocellum M2_15-C8 showed higher digestion activities e.g. cellulose at 60, 70, 75, and 80 kDa. From FIG. 4c, in xylanase at 20-250 kDa, it was found that enzymes produced by both strains were similar but some xylanase produced by the mutant strain Clostridium thermocellum M2_15-C8 showed higher digestion activities e.g. xylanase at 35, 45, 60, 70, and 75 kDa.

(54) TABLE-US-00003 TABLE 3 Enzyme activities in cellulolytic enzymes and xylolytic enzymes produced by wild type and mutant strain Clostridium thermocellum M2_15-C8 Enzymes Wild type Mutant (unit/mL) (KK8.3) (M2_15-C8) Cellulolytic enzymes Carboxy methyl cellulose 4.64 10.21 Avicelase 1.24 2.55 Cellobiohydrolase 3.64 4.34 β-glucosidase 1.27 2.30 Xylolytic enzymes Xylanase 9.05 36.85 β-xylosidase 0.13 0.17 β-galactosidase 0.16 0.31 Arabinofuranosidase 0.17 0.36 Acetylxylanesterase 0.29 0.31

Example 4: Comparison of Nucleotide Sequence of Genetic Materials of Wild Type and Mutant Strain Clostridium thermocellum M2_15-C8

(55) The comparison of nucleotide sequence of genetic materials of wild type and mutant strain Clostridium thermocellum M2_15-C8 could be done by modified CTAB method. Then, about 5 μg of extracted genetic materials were searched for DNA sequencing by ion torrent sequencing method using ion personal genome machine (PGM). The obtained DNA sequencing of wild type and mutant strain Clostridium thermocellum M2_15-C8 were analyzed for their differences by bioinformatics method using information of Clostridium thermocellum ATCC27405 strain as reference genetic materials.

(56) From the comparison of genetic materials of wild type and mutant strain Clostridium thermocellum M2_15-C8, it was found that cellulolytic and xylolytic enzymes producing genes and proteins related to transportation of proteins and enzymes outside their cells were mutated for at least 21 genes as shown in table 4. Two mutation areas were at 500 bases before CDS and at coding sequence (CDS).

(57) From table 4, according to the mutation at 500 bases before CDS, the nucleotide sequences of gene codes 220, 427, 453, 850, 1252, 1257, 1305, 1884, and 1902 were missing, whereas the nucleotide sequences of gene code 2701 were increased. This was because the 500 bases before CDS contained regulator gene, promoter gene, and operator gene. Therefore, mutations at this area affected the different expression of proteins and enzymes.

(58) Moreover, according to the mutation at the CDS, the nucleotide sequences of gene codes 111, 419, 442, 1456, 1529, 2246, 2479, 2611, 2654, 2854, and 2875 were missing. Because the CDS is the area that responded for the production of proteins or enzymes, the mutations at this area affected the different expression of proteins and enzymes.

(59) Therefore, the mutation in genes responded for the production of cellulolytic and xylolytic enzymes, including proteins related to transportation of proteins and enzymes outside their cells affected different expressions, activities, and characters of cellulolytic and xylolytic enzymes as shown in example 3.

(60) TABLE-US-00004 TABLE 4 Genes related to the production of cellulolytic and xylolytic enzymes and proteins related to transportation of proteins and enzymes outside their cells of the wild type and mutant strain Clostridium thermocellum Mutated nucleotide characters Mutation Gene Wild Mutant area code type M2_15-C8 Role of expression proteins 500 bases 220 GT G β-glucosidase enzymes and related to digestion before of cellulose CDS 427 CA C Cellulose enzymes and related to digestion of polysaccharides 453 AT A Hydrolase enzymes with bonding site with bacterium cell wall 850 ATT A Cellulase, mannanase, and β-mannosidase enzymes and related to digestion of polysaccharides 1252 TTA T MFS transporter, bacterium cell wall protein, related to transporting proteins and enzymes outside their cells 1257 CT C Bacterium cell wall proteins 1305 GT G β-glucosidase enzymes and related to digestion of cellulose 1884 CT C ABC transporter, bacterium cell wall protein, related to transporting proteins and enzymes outside their cells 1902 TA T Xylanase, β-xylosidase enzymes and related to digestion of xylan 2701 A AGAT Xylanase enzymes and related to digestion of xylan Coding 111 AT A Dockerin, binding protein of digesting sequence enzymes and bacterium cell wall, supporting (CDS) polysaccharide digestion of enzymes 419 TA T Cellulase and β-cellobiosidase enzymes 442 CT C Dockerin, binding protein of digesting enzymes and bacterium cell wall, supporting polysaccharide digestion of enzymes 1456 AT A β-glucosidase enzymes and related to digestion of cellulose 1529 CT C ABC transporter, bacterium cell wall protein, related to transporting proteins or enzymes outside their cells 2246 TC T Proteins related to binding of carbohydrates 2479 CT C Proteins related to binding of cellulose 2611 CA C α-L-arabinofuranosidase enzymes and related to digestion of arabinan 2654 CA C Xylanase enzymes and related to digestion of xylan 2854 AT A ABC transporter, bacterium cell wall protein, related to transporting proteins and enzymes outside their cells 2875 GA G Cellulase enzymes and related to digestion of polysaccharides

Example 5: The Use of Enzymes Produced by the Mutant Strain Clostridium thermocellum M2_15-C8 in the Saccharification of Bagasse

(61) Bagasse pretreated with several methods such as: 1) steam explosion using base catalyst method (STEX); 2) organic solvent separation method (FR); 3) sodium hydroxide in acetone method (AC); and 4) sodium methoxide in methanol method (MM) was saccharified at the concentration of 5.0-10.0% (w/v) and pH about 6.0 to 7.0 was added with enzymes produced by the mutant strain Clostridium thermocellum M2_15-C8 according to example 3. The concentration of enzymes was about 10-20 mg/g bagasse. The recombinant f3-glucosidase were also added at the concentration about 10-30 unit/g bagasse into the mixture. The mixture was incubated at the temperature 50-60° C. for 12-48 hours. Then, the obtained glucose was subjected to quantitative analysis. It was found that enzymes produced by mutant strain, together with recombinant β-glucosidase could saccharify bagasse pretreated by steam explosion method and produced glucose more than 590 mg/g substrate, could saccharify bagasse pretreated by composition separation with organic solvent method and produced glucose more than 600 mg/g substrate, and could saccharify bagasse pretreated by sodium hydroxide in acetone method and produced glucose more than 500 mg/g substrate. Moreover, they could saccharify bagasse pretreated by sodium methoxide in methanol method and produced glucose more than 530 mg/g substrate as shown in FIG. 5.

Preferred Embodiment of the Invention

(62) Preferred embodiment of the invention is as provided in the description of the invention.