# Patent

## Title
Genetically modified Clostridium saccharoperbutylacetonicum

## Abstract

The present invention provides a means for producing butanol in butanol fermentation with high efficiency. The present invention relates to a genetically modified microorganism of Clostridium saccharoperbutylacetonicum, and a method for producing butanol using the microorganism.

## Background
CROSS-REFERENCE TO RELATED APPLICATIONS
This application is a 371 of PCT/JP2014/055140, filed Feb. 28, 2014, which claims the benefit of Japanese Patent Application Nos. 2013-063347, filed Mar. 26, 2013 and 2014-032953, filed Feb. 24, 2014.
TECHNICAL FIELD
The present invention relates to a genetically modified microorganism of Clostridium saccharoperbutylacetonicum and a method for producing butanol using the microorganism.
BACKGROUND ART
In microorganic butanol fermentation, solvents such as acetone and ethanol and organic acids such as butyric acid, acetic acid and lactic acid are produced as by-products in addition to butanol. These by-products are a factor of lowering butanol yield and an obstacle in constructing a process for collecting butanol.
In butanol fermentation, decreasing by-products (e.g., acetone, ethanol, organic acids) is very useful for improving the yield of butanol in relation to glucose and simplifying a separation/purification step. In the circumstances, studies for decreasing by-products have been made. As a method therefor, disruption of by-product synthetic genes or enhancement of butanol synthetic genes have been frequently adopted and carried out by means using homologous recombination and mutation. For example, in Non Patent Literature 1, a buk (butyrate kinase) gene and a pta (phosphotransacetylase) gene are disrupted by homologous recombination. However, in this method, acetic acid production increases significantly when the butyric acid production pathway is disrupted and butyric acid production increases significantly when the acetic acid production pathway is disrupted. In addition, there is a case where production of a solvent increases as in the case where aad (alcohol/aldehyde dehydrogenase) gene is cloned and thereafter excessively expressed (Non Patent Literature 2). There is another case where gene suppression and introduction are simultaneously performed. In Non Patent Literature 3, thl (acetyl-CoA dimerized enzyme) gene and aad gene are expressed while expression of ctfB (subunit B of CoA transferase) gene is suppressed thereby the concentration of ethanol is increased to about 13 g/L.
As a case in which ethanol and butanol are produced without producing acetone, Non Patent Literature 4 discloses simultaneous disruption of adc (acetoacetate decarboxylase) gene or ctfAB (CoA transferase) gene and pta gene. In that case, butyric acid accumulates significantly whereas production of butanol decreases drastically. Patent Literature 1 describes that a strain in which buk or ptb (phosphotransbutyrylase) gene of Clostridium acetobutyricum is disrupted such that butyric acid production pathway is disrupted is further subjected to adjustment of acetone, lactic acid, acetic acid and hydrogenase production. However, specific numerical values thereof are not disclosed in the literature. In Non Patent Literature 5, ptb and pta genes and buk and pta genes are disrupted in Clostridium acetobutyricum; however, a decreasing effect in production of by-products including butyric acid and acetic acid is not sufficient and an increase in butanol yield has not been achieved.
Accordingly, it has been desired to develop a microorganism capable of producing butanol with high efficiency while suppressing production of by-products such as butyric acid, acetic acid and ethanol.
CITATION LIST
Patent Literature
Patent Literature 1: WO 2008/052596
Non Patent Literature
Non Patent Literature 1: Green et al., Microbiology., 142: 2079, 1996
Non Patent Literature 2: Nair et al., J. Bacteriol., 176: 871, 1994
Non Patent Literature 3: Sillers et al., Biotechnol Bioeng., 102: 38, 2009
Non Patent Literature 4: Lehmann et al., Appl Microbiol Biotechnol., 94: 743, 2012
Non Patent Literature 5: Jang et al., mbio 2012., 23: 00314, 2012
SUMMARY OF INVENTION
Technical Problem
An object of the present invention is to improve the yield of butanol in butanol fermentation by suppressing production of by-products other than butanol.
Solution to Problem
The present inventors succeeded in improving butanol yield by disrupting the pathway leading to production of butyric acid from butyryl-CoA in a microorganism of Clostridium saccharoperbutylacetonicum thereby suppressing production of not only butyric acid but also other by-products in butanol fermentation using the microorganism, and arrived at the present invention.
More specifically, the present invention encompasses the following.
(1) A microorganism of Clostridium saccharoperbutylacetonicum wherein a function of a butyric acid producing enzyme gene involved in a pathway leading to production of butyric acid from butyryl-CoA is disrupted.
(2) The microorganism according to (1), in which the functions of ptb and/or buk as the butyric acid producing enzyme gene are disrupted.
(3) The microorganism according to (1) or (2), in which a function of an acetic acid producing enzyme gene involved in a pathway leading to production of acetic acid from acetyl-CoA is further disrupted.
(4) The microorganism according to (3), in which the functions of pta and/or ack as the acetic acid producing enzyme gene are disrupted.
(5) The microorganism according to any of (1) to (4), in which a function of an acetone producing enzyme gene involved in a pathway leading to production of acetone from acetoacetyl-CoA is further disrupted.
(6) The microorganism according to (5), in which the functions of adc and/or ctfAB as the acetone producing enzyme gene are disrupted.
(7) The microorganism according to any of (1) to (6), in which a function of a lactic acid producing enzyme gene involved in a pathway leading to production of lactic acid from pyruvic acid is further disrupted.
(8) The microorganism according to (7), in which the function of ldh1 as the lactic acid producing enzyme gene is disrupted.
(9) A method for producing butanol, comprising a step of culturing the microorganism according to any of (1) to (8) in a medium containing a carbon source.
(10) The method according to (9), comprising a step of collecting butanol from a culture solution.
Advantageous Effects of Invention
According to the present invention, improvement in butanol yield in butanol fermentation and simplification of separation/purification of butanol from fermentation liquor are achieved, and thereby economically advantageous production of butanol is realized.
This specification incorporates the content of the specification and/or drawings of Japanese Patent Applications Nos. 2013-063347 and 2014-032953, from which priority is claimed to the present application.



BRIEF DESCRIPTION OF DRAWINGS
FIG. 1 illustrates a metabolic pathway of butanol fermentation together with intermediate compounds and enzyme genes involved therein.
FIG. 2 shows a plasmid map of pNS78 plasmid.
FIG. 3 shows a plasmid map of pNS47 plasmid.
FIG. 4 shows a plasmid map of pNS44 plasmid.
FIG. 5 shows a plasmid map of pNS80 plasmid.
FIG. 6 shows a plasmid map of pKNT19-FLP plasmid.



DESCRIPTION OF EMBODIMENTS
The microorganism of the present invention can be obtained by disrupting a function of butyric acid producing enzyme gene in Clostridium saccharoperbutylacetonicum (C. saccharoperbutylacetonicum). C. saccharoperbutylacetonicum has a butanol production ability. Specific examples of the strain include, but not particularly limited to, ATCC27021 strain and ATCC13564 strain.
Though introduction of a plasmid to microorganisms of Clostridium genus is difficult, introduction of a plasmid to C. saccharoperbutylacetonicum can be made with comparative ease. In the case of C. acetobutyricum ATCC824 strain and the like, for example, a plasmid cannot be introduced as it is and a methylation treatment must be performed since the plasmid is cleaved by DNA endonuclease. However, C. saccharoperbutylacetonicum does not require such treatment.
The butyric acid producing enzyme gene is a gene encoding an enzyme involved in the pathway leading to production of butyric acid from butyryl-CoA. Examples of the butyric acid producing enzyme gene include ptb gene (gene encoding phosphotransbutyrylase) and buk gene (gene encoding butyrate kinase). Phosphotransbutyrylase is an enzyme catalyzing a reaction of producing butyryl phosphate from butyryl-CoA. Butyrate kinase is an enzyme catalyzing a reaction of converting butyryl phosphate to butyric acid. Disruption of a function of butyric acid producing enzyme gene includes disruption of the function of one of these genes and disruption of the functions of two or more of these genes as well as disruption of one or more functions of genes encoding an enzyme subunit.
The examples where the butyric acid production pathway is disrupted include Non Patent Literature 1, Patent Literature 1 and Non Patent Literature 5. In Non Patent Literature 1, however, a large amount of acetic acid is produced by the disruption of the butyric acid production pathway and the yield of butanol is not improved. Patent Literature 1 describes a disrupted strain but does not describe culture results thereof. Though Non Patent Literature 5 describes the results of disruption of production pathways of both acetic acid and butyric acid, no improvement of butanol yield was obtained unless alcohol dehydrogenase expression is externally performed. These studies are all performed on C. acetobutyricum. 
The bacterial strain used in the present application is C. saccharoperbutylacetonicum. Surprisingly, even if the butyric acid production pathway is disrupted in the strain, a phenomenon as observed in C. acetobutyricum, i.e., increase in acetic acid, was not observed and growth of the bacterial cells was satisfactory and butanol yield was increased.
As described above, it was found that, in contrast to that disruption of the butyric acid production pathway has no significant effect upon butanol production in C. acetobutyricum; in C. saccharoperbutylacetonicum, disruption of the butyric acid production pathway has an effect of reducing by-products and improving butanol yield. It was also found that when the acetic acid production pathway of the strain whose butyric acid production pathway was already disrupted is further disrupted, productions of acetic acid and butyric acid are drastically reduced and butanol yield is drastically improved.
In the microorganism of the present invention, it is preferable that the function of acetic acid producing enzyme gene is disrupted. By disrupting the function, the butanol yield in butanol fermentation can be further improved.
The acetic acid producing enzyme gene is a gene encoding an enzyme involved in the pathway leading to production of acetic acid from acetyl-CoA. Examples of the acetic acid producing enzyme gene include pta gene (gene encoding phosphotransacetylase) and ack gene (gene encoding acetate kinase). Phosphotransacetylase is an enzyme catalyzing a reaction of producing acetyl phosphate from acetyl-CoA. Acetate kinase is an enzyme catalyzing a reaction of converting acetyl phosphate to acetic acid. Disruption of the function of acetic acid producing enzyme gene includes disruption of the function of one of these genes and disruption of the functions of two or more of these genes as well as disruption of one or more functions of genes encoding an enzyme subunit.
In the microorganism of the present invention, the function of acetone producing enzyme gene may further be disrupted. By disrupting the acetone producing enzyme gene, acetone as a by-product is not produced and a separation/purification step is more simplified. Further improvement in yield is expected by combining with a technique of culture using reducing power supply.
The acetone producing enzyme gene is a gene encoding an enzyme involved in the pathway leading to production of acetone from acetoacetyl-CoA. Examples of the acetone producing enzyme gene include ctfA gene (gene encoding subunit A of CoA transferase), ctfB gene (gene encoding subunit B of CoA transferase) and adc gene (gene encoding acetoacetate decarboxylase). CoA transferase, which contains subunit A and subunit B, catalyzes a reaction of converting acetoacetyl-CoA to acetoacetate. The notation of ctfAB refers to both of a gene encoding subunit A and a gene encoding subunit B of CoA transferase. Acetoacetate decarboxylase is an enzyme catalyzing a reaction of producing acetone by decarboxylating acetoacetate. Disruption of the function of the acetone producing enzyme gene includes disruption of the function of one of these genes and disruption of the functions of two or more of these genes as well as disruption of one or more functions of genes encoding an enzyme subunit.
In the microorganism of the present invention, the function of lactic acid producing enzyme gene may further be disrupted. By disrupting the lactic acid producing enzyme gene, lactic acid as a by-product is not produced and a separation/purification step is more simplified. In addition, since reducing power can further be used in butanol production, a further improvement in yield can be expected.
A lactic acid producing enzyme gene is a gene encoding an enzyme involved in the pathway leading to production of lactic acid from pyruvic acid. Lactate dehydrogenase is encompassed in the lactic acid producing enzyme gene. Lactate dehydrogenase is an enzyme catalyzing interconversion between lactic acid and pyruvic acid. At the same time, interconversion between NADH and NAD+ occurs simultaneously. There are four different types of lactate dehydrogenases. Two of them are cytochrome c-dependent types, which act on D-lactic acid (D-lactate dehydrogenase: EC1.1.2.4) or L-lactic acid (L-lactate dehydrogenase: EC1.1.2.3), respectively. The remaining two types are NAD (P)-dependent enzymes, which act on D-lactic acid (D-lactate dehydrogenase: EC1.1.1.28) or L-Iactic acid (L-lactate dehydrogenase: EC1.1.1.27), respectively. Specific examples of the lactate dehydrogenase include ldh1, ldh2, lldD and ldh3. In particular, disruption of the function of ldh1 is preferable. Disruption of the function of lactic acid producing enzyme gene includes disruption of the function of one of these genes and disruption of the functions of two or more of these genes.
In the present invention, a gene includes DNA and RNA, and DNA includes single stranded DNA and double stranded DNA.
Disruption of a function of enzyme gene encompasses partial or whole modification (e.g., substitution, deletion, addition and/or insertion) or disruption of an enzyme gene such that the expression product of the gene loses a function as the enzyme and an enzyme protein is not expressed. For example, a function of enzyme gene can be completely or substantially dysfunctional or disrupted by causing a deletion, substitution, addition or insertion in a part of genomic DNA of the enzyme gene. A partial or whole modification (e.g., substitution, deletion, addition and/or insertion) or disruption of a promoter of enzyme gene is also encompassed. Herein, disruption of a gene refers to the state where the function of the enzyme gene is completely or substantially dysfunctional by deleting a part or whole of the gene sequence; by inserting another DNA sequence in the gene sequence; or by substituting a part of its gene sequence with another sequence.
In the present invention, a transformant of Clostridium saccharoperbutylacetonicum, in which functions of enzyme genes are disrupted, is a knockout microorganism in which the functions of enzyme genes on the genome are disrupted. Such a transformant can be prepared generally by using a gene targeting recombination method (gene targeting method: for example, Methods in Enzymology 225: 803-890, 1993) known in the art, for example, by homologous recombination. The homologous recombination method can be performed by inserting a target DNA into the sequence homologous to the sequence on the genome, introducing the DNA fragment into a cell, and allowing the cell to cause homologous recombination. In the introducing into the genome, a strain in which homologous recombination took place can be easily screened by using a DNA fragment in which a target DNA is ligated to a drug resistant gene. Alternatively, it is also possible to insert a DNA fragment in which a drug resistant gene is ligated to a gene to be lethal under specific conditions by homologous recombination thereafter substituting the drug resistant gene with the gene to be lethal under specific conditions. Furthermore, a method using group II intron found in lactobacillus (Guo et. al., Science 21; 289 (5478): 452-7 (2000)) and a genome processing method such as TALEN technology and CRISPR technology can be used.
Group II intron is an intron having a function of forming a complex with a protein of lactobacillus called LtrA and being inserted into a specific region of a genome. By modifying the site of the intron called as a targeting region appropriately, the DNA sequence can be inserted into a desired site of a microorganism genome. If the site at which the DNA is inserted is within a gene, the gene almost loses its function in most cases. This method can be used as a means for disrupting a gene. By inserting an appropriate drug resistant gene within group II intron and inserting within the drug resistant gene a self-splicing DNA region called td intron, the drug resistant gene cannot be expressed in the state of a vector while the drug resistant gene comes to act when the drug resistant gene takes a form of the group II intron and DNA sequence is inserted with the td intron self-spliced. The gene-disrupted strain obtained in this manner can be easily screened by using drug resistance acquired by the drug resistant gene introduced in the genome as a marker.
The site called as a targeting sequence has been analyzed by using Escherichia coli by Perutka et al. (Perutka et al., J. Mol. Biol. 13; 336 (2): 421-39 (2004)). As a result, it became possible to predict which site of a sequence is modified in which way to insert the sequence to a target DNA sequence. For example, by programming excel macro and entering the nucleotide sequence of a target gene that is wished to be disrupted to the macro based on the literature, the DNA insertion site of the target gene and a method of modifying a targeting sequence can be output.
In general, when a drug resistant gene is used for screening a gene disrupted strain, another drug resistant gene is required for disrupting multiples of genes. However, if a drug resistant gene is spliced out by use of e.g., the FLP-FRT method (Schweizer H P, J. Mol. Microbiol. Biotechnol. 5 (2): 67-77 (2003)) or the Cre-loxP method (Hoess et al., Nucleic Acids Res. 11; 14 (5): 2287-300 (1986)), drug resistance can be overcome. FLP and Cre recognize a short DNA sequence consisting of about 25 bases called FRT and loxP, respectively, and have a function of cutting out the region sandwiched between FRTs or loxPs. More specifically, a gene disrupted strain having drug sensitivity can be obtained by conducting a gene disruption using a gene-disruption vector in which an FRT sequence or a loxP sequence is arranged on the side part of a drug resistant gene and thereafter introducing an another vector in which FLP or Cre gene is cloned to the obtained gene disrupted strain having drug resistance and allowing to act thereto. Thereafter, gene disruption can be carried out again in the same manner as mentioned above.
As DNA sequences encoding a butyric acid producing enzyme gene, an acetic acid producing enzyme gene, an acetone producing enzyme gene and a lactic acid producing enzyme gene, sequences known to the public registered in the GenBank may be used. The nucleotide sequences of ctfA, ctfB and adc of C. saccharoperbutylacetonicum ATCC13564 strain are registered under Accession Number AY251646. With respect to ATCC27021 strain used herein, the nucleotide sequences of ptb is shown as SEQ ID NO: 1; the base sequence of pta is shown as SEQ ID NO: 2; the base sequence of ctfB is shown as SEQ ID NO: 3; and the base sequence of ldh1 is shown as SEQ ID NO: 8.
Genes functionally equivalent to the enzyme genes encoded by the above nucleotide sequences are also encompassed in the enzyme genes. Genes functionally equivalent to an enzyme gene consisting of a certain nucleotide sequence include genes consisting of a sequence having 70% or more, preferably 80% or more, more preferably 90% or more, further preferably 95% or more, and most preferably 99% or more of homology (or identity) to said nucleotide sequence and encoding a protein having the same enzymatic activity. For example, as the gene functionally equivalent to ptb consisting of the sequence represented by SEQ ID NO: 1, genes consisting of a nucleotide sequence having 70% or more, preferably 80% or more, more preferably 90% or more, further preferably 95% or more, and most preferably 99% or more of homology (or identity) to the nucleotide sequence represented by SEQ ID NO: 1 and encoding a protein having phosphotransbutyrylase activity can be exemplified. In addition, those skilled in the art can determine equivalent genes in other microorganisms with reference to the reference numbers given to known genes by the GenBank.
A probe (for example, about 30 to 150 bases) prepared based on a known sequence, tagged with a radioactive or fluorescent label can be used for detecting or isolating genomic DNA of each enzyme gene. The open-reading frame (ORF) of a desired enzyme gene can be searched with using the above prove by extracting DNA from microorganism cells in a conventional manner, cleaving with restriction enzymes, and subjecting to hybridization such as Southern hybridization and in-situ hybridization. A targeting vector is designed by preparing a restriction enzyme map as necessary and determining an arbitrary target site for homologous recombination.
A vector for preparing a targeting vector by inserting a recombinant DNA is not particularly limited as long as it is replicable in a microorganism of Clostridium genus. It is favorable if the vector is a shuttle vector of Escherichia coli and a microorganism of Clostridium genus and particularly preference is given to a shuttle vector pKNT19 derived from pIM13 (Journal of General Microbiology, 138, 1371-1378 (1992)).
A vector for obtaining a strain having a disrupted gene by transformation can be obtained by cloning a necessary sequence from a microorganic genomic DNA as a template or synthesizing and, if necessary, ligating sequences appropriately to provide the necessary sequence. A method for obtaining a desired gene or a promoter from microorganic genomic DNA by cloning is commonly known in the art of molecular biology. For example, in the case where the gene sequence is known, an appropriate genomic library can be prepared by restriction endonuclease digestion and a desired gene can be screened by use of a complementary probe to the desired gene. After the sequence is isolated, an amount of DNA suitable for transformation can be obtained by amplifying the DNA using a standard amplification method such as a polymerase chain reaction (PCR) (U.S. Pat. No. 4,683,202). Sambrook, J., Fritsch, E. F., Maniatis, T., Molecular Cloning, Cold Spring Harbor Laboratory Press, 1.21 (1989) discloses methods of preparation of a genomic DNA library used for cloning, hybridization, PCR, preparation of plasmid DNA, cleavage and ligation of DNA, transformation and the like. A DNA sequence can be directly synthesized. Alternatively, a DNA sequence having a longer chain can be obtained via ligation by subjecting the DNA sequence obtained via PCR and the like to a treatment with restriction enzymes and conducting ligation, or conducting PCR reaction with using a sequence in which a probe (primer) complementary to the both ends of the DNA sequence is ligated to a 15 bp length homologous region of another DNA sequence and thereafter ligating by conducting an infusion reaction (U.S. Pat. No. 7,575,860).
Introduction of a targeting vector to a microorganism can be carried out by a method known to the public. Examples of the introduction method include, but not particularly limited to, a microcell method, a calcium phosphate method, a liposome method, a protoplast method, a DEAE-dextran method and an electroporation method. An electroporation method is preferably used.
The obtained transformant is cultured in a medium for butanol production to yield butanol by butanol fermentation. As the medium and culture conditions to be used for culturing, those known in the field of butanol fermentation can be used. The culture medium usually contains a carbon source, a nitrogen source and inorganic ions.
As the carbon source, preferably sugars such as monosaccharides, oligosaccharides and polysaccharides are used. Preference is given to monosaccharides, particularly to glucose. In combination with glucose, other sugars such as lactose, galactose, fructose and starch hydrolysate, alcohols such as sorbitol, or organic acids such as fumaric acid, citric acid and succinic acid may be used.
As the nitrogen source, for example, inorganic ammonium salts such as ammonium sulfate, ammonium chloride and ammonium phosphate, organic nitrogen compounds such as soybean hydrolysate, ammonia gas, ammonium solution and the like can be used.
As the inorganic ion, potassium phosphate, magnesium sulfate, an iron ion, a manganese ion and the like are added. As the organic micronutrient, required substances such as thiamine, p-aminobenzoic acid, vitamin B1 and biotin and yeast extract and the like may be desirably added in an appropriate amount, as needed.
In the present invention, by culturing the transformant preferably in the condition where a reducing power is increased, butanol can be highly efficiently produced while suppressing production of by-products such as acetone, ethanol, acetic acid, butyric acid and lactic acid. An absolute amount of butanol produced can also be increased. The culture in the condition where a reducing power is increased means that an enzyme reaction taking place during culturing is performed in the conditions where a reducing power is increased. The reducing power can be increased by adding, for example, NADH, by introducing hydrogen or by increasing hydrogen partial pressure within a culture vessel. By increasing hydrogen partial pressure within a culture vessel, it is considered that the hydrogen partial pressure of a gas phase in contact with a culture solution increases and hydrogen in the gas phase in contact with the culture solution is immediately taken by hydrogenase.
The hydrogen partial pressure in a culture vessel can be increased, for example, by performing culture in a closed state. In the closed state, external release of hydrogen from microorganisms is limited and thereby hydrogen partial pressure in a culture vessel can be increased. Alternatively, hydrogen may be introduced from the outside. For example, hydrogen may be introduced to a culture solution by bubbling or to a gas-phase portion of a culture vessel, or may also be introduced so as to be in contact with a culture solution. More specifically, the hydrogen partial pressure in a culture vessel in the range of 20 to 40° C. is preferably 0.06 atm or more, more preferably 0.08 atm or more, further preferably 0.10 atm or more, further more preferably 0.12 atm or more, most preferably 0.15 atm or more and preferably 10 atm or less.
Hydrogen partial pressure can be measured by a method known to the public and the measurement method is not particularly limited. For example, the hydrogen partial pressure can be measured by trapping the gas generated in an aluminum bag, determining hydrogen concentration of the gas in the bag by gas chromatography, quantifying the amount of hydrogen generated by multiplying the concentration and the volume, and calculating from the amount of hydrogen generated and the volume of the gas-phase portion in a culture vessel.
In the present invention, production amount of butanol relative to by-products can be improved by performing culture under pH control. The pH of the medium is controlled, if necessary, so as to be preferably 4.6 or more, 4.7 or more, 4.8 or more, 4.9 or more, 5 or more or 5.5 or more, preferably 8 or less, 7.5 or less, 7.0 or less, 6.9 or less, 6.8 or less, 6.7 or less, 6.6 or less or 6.5 or less. To control pH, inorganic or organic substances that are acidic or alkalic such as calcium carbonate, ammonia, sodium hydroxide, potassium hydroxide, potassium phosphate and the like can be used. The pH control encompasses the case where the pH of a culture medium is kept to the target pH without adding alkalic substances as above. For example, in the case where ammonium sulfate is used as a nitrogen source, decrease in pH may be suppressed and growth may be improved by replacing it with ammonium acetate having a high buffer capacity.
Other culture conditions are not particularly limited and conditions conventionally used in the technical field can be employed. For example, when a batch culture is performed, the culture time is usually 5 to 100 hours and preferably 12 to 48 hours. When a continuous culture or feeding culture is performed, the culture time is usually 200 hours or more, preferably 500 hours or more and more preferably 1000 hours or more. The culture temperature is usually 20 to 55° C. and preferably 25 to 40° C. and is controlled to about 30° C. for example.
In the producing method of the present invention, the production ratio of butanol relative to by-products, which is a numerical value obtained by dividing the molar number of the butanol generated by the total molar number of the acetone, ethanol, acetic acid and butyric acid generated, is preferably 2.5 or more, 3.0 or more, 4.0 or more or 5.0 or more.
Furthermore, the production ratio of butanol relative to by-products, which is a numerical value obtained by dividing the molar number of butanol generated by the total molar number of acetone, ethanol, acetic acid, butyric acid and lactic acid generated, is preferably 2.5 or more, 3.0 or more, 4.0 or more or 5.0 or more.
Collection of a fermentation product, i.e., butanol, from culture solution of during or after completion of culture can be carried out by a method known to the public without using any special method. Collection can be made during or after completion of culture by combining methods known in the technical field such as distillation, gas stripping, solvent extraction and other methods. Preferably, butanol is collected during culture by gas stripping or solvent extraction followed by purified via distillation. In the method of the present invention, since production amount of butanol relative to production amount of by-products is large and therefore the yield of butanol is high and separation/purification step of butanol can be simplified, the method of the present invention is advantageous in terms of cost.
Hereinafter, the present invention will be more specifically described by way of examples; however, the scope of the present invention is not limited to the examples.
EXAMPLES
Example 1
Preparation of Transformed Microorganism
Based on Perutka et al., J. Mol. Biol. 13; 336 (2): 421-39 (2004), an excel macro which outputs an insertion site of group II intron and a modification method of targeting sequence in a target gene by entering nucleotide sequence of the target gene was programmed. Then, the nucleotide sequences of a ptb gene, a pta gene, a ctfB gene and a ldh1 gene to be subjected to gene disruption were entered in the macro so as to output modification sites of the targeting sequence. The nucleotide sequence of the ptb gene is shown as SEQ ID NO: 1; the nucleotide sequence of the pta gene is shown as SEQ ID NO: 2; the nucleotide sequence of the ctfB gene is shown as SEQ ID NO: 3; and the nucleotide sequence of ldh1 gene is shown as SEQ ID NO: 8.
Based on the data, pNS78 plasmid, pNS47 plasmid, pNS44 plasmid and pNS80 plasmid, which were disruption vectors for ptb gene, pta gene, ctfB gene and ldh1 gene, were designed. DNA synthesis was used for the construction. The nucleotide sequences of these plasmids are shown as SEQ ID NOs: 4, 5, 6 and 9, respectively and plasmid maps are shown in FIGS. 2, 3, 4 and 5. Furthermore, pKNT19-FLP plasmid containing FLP recombinase was designed and constructed similarly by DNA synthesis. The nucleotide sequence thereof is shown as SEQ ID NO: 7 and the plasmid map thereof is shown in FIG. 6.
C. saccharoperbutylacetonicum ATCC27021 strain was transformed with pNS78 prepared. Specifically, as preculture, a glycerol stock (0.5 ml) of C. saccharoperbutylacetonicum was inoculated in TYA medium (5 ml) and cultured at 30° C. for 24 hours. This preculture solution was inoculated in TYA medium (10 ml) such that OD=0.1 and incubated in a 15 mL-volume falcon tube at 37° C. When OD reached 0.6, a fermentation liquor was centrifuged and the supernatant was removed. 65 mM MOPS buffer (pH 6.5)(10 ml) cooled on ice was added thereto, resuspended by pipetting, and centrifuged. Washing with MOPS buffer was repeated twice. The MOPS buffer was centrifugally removed and the bacterial pellets were resuspended with 0.3 M sucrose (100 μL) cooled on ice to obtain competent cells. The competent cells (50 μL) was transferred to an Eppendorf tube and mixed with a plasmid (1 μg). The mixture was placed in an ice-cooled electroporation cell and voltage was applied at 2.5 kV/cm, 25 μF, 350Ω in exponential decay mode. The electroporation apparatus used was Gene pulser xcell (Bio-rad). Thereafter, the whole amount was inoculated in TYA medium (5 ml), cultured at 30° C. for about 2 hours for rescue. Thereafter, the rescue culture solution was applied onto MASS solid medium containing chloramphenicol (10 ppm), and cultured at 30° C. for several days. Screening was performed from colonies to obtain a strain in which the plasmid was introduced and resistance against chloramphenicol was acquired. The strain harboring pNS78 was further subcultured for a plurality of times and inoculated in MASS solid medium containing erythromycin (200 ppm) to obtain C. saccharoperbutylacetonicum Δptb strain, in which the group II intron functions, DNA sequence was inserted in the target gene, a butyric acid producing enzyme gene ptb was disrupted, and erythromycin resistance was acquired.
Since the strain has erythromycin resistance as it is and therefore disruption of a plurality of genes cannot be conducted, the erythromycin resistance gene was removed by FLP recombinase contained in pKNT19-FLP plasmid. First, C. saccharoperbutylacetonicum Δptb was repeatedly subcultured to obtain a strain missing pNS78 spontaneously. To the strain, pKNT19-FLP plasmid was introduced in the same electroporation method as above and screening was made based on chloramphenicol resistance. The strain having pKNT19-FLP plasmid introduced therein was repeatedly subcultured. An erythromycin sensitive strain, which was obtained by removing an erythromycin resistance gene by FLP action, was screened by a replica plate method. The erythromycin sensitive strain was subcultured to obtain C. saccharoperbutylacetonicum Δptb with losing pKNT19-FLP plasmid itself (non erythromycin resistant). To C. saccharoperbutylacetonicum Δptb having no erythromycin resistance, pNS47 and pNS44 were introduced by repeating the aforementioned method. As a result, C. saccharoperbutylacetonicum ΔptaΔptb strain and C. saccharoperbutylacetonicum ΔctfBΔptaΔptb strain in which pta gene and ctfB gene were also disrupted were successfully obtained. Further to C. saccharoperbutylacetonicum Δptb, pNS47 and pNS80 were introduced by repeating the aforementioned method. As a result, C. saccharoperbutylacetonicum ΔptaΔptbΔldh1 strain in which pta gene and ldh1 gene were also disrupted were successfully obtained. The compositions of the medium and buffer used above are shown below.







TABLE 1







Composition of TYA medium










Component
Content (g/L)














D-glucose
40



Tryptone (Difco)
6



Yeast extract (Difco)
2



Ammonium acetate
3



Magnesium sulfate monohydrate
0.3



Potassium dihydrogen phosphate
0.5



Ferric sulfate (II)
0.01

















TABLE 2







Composition of MASS medium










Component
Content (g/L)














D-glucose
10



Soluble starch
10



Potassium dihydrogen phosphate
0.5



Ammonium sulfate
1



Magnesium sulfate heptahydrate
0.1



Ferric sulfate (II) heptahydrate
0.01



Biotin
0.00002

















TABLE 3







Composition of MOPS buffer










Component
Content (g/L)







MOPS
209



Sodium hydroxide
(added until pH reaches 6.5)










Example 2
Butanol Fermentation by Δptb
A transformed microorganism C. saccharoperbutylacetonicum (Δptb strain) prepared in Example 1 was cultured and the performance of the microorganism was evaluated. 500 μL of glycerol stock of the transformed microorganism was inoculated in TYA medium and cultured in a test tube at 30° C. for 24 hours. 50 μL of the obtained preculture solution was inoculated in fresh TYS medium (5 ml) and cultured in a test tube at 30° C. for about 24 hours in open conditions.
After completion of culture, the culture solution was taken and subjected to liquid chromatography to perform quantitative analysis of butanol, other alcohols, ketones and organic acids. Aminex HPX-87H Column (Bio-Rad) was used as the column. The results are shown in Table 4. In the table, “B/(A+E+AA+BA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM) and butyric acid (mM), and is referred to as by-product parameter 1. In the table, “B/(A+E+AA+BA+LA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM), butyric acid (mM) and lactic acid (mM) and is referred to as by-product parameter 2. In addition, by-product parameter 1 and by-product parameter 2 are collectively referred to as “by-product parameter”.

















TABLE 4















B/(A + E +






Acetic
Butyric
Lactic
Butanol/
B/(A + E +
AA + BA +



Acetone
Butanol
Ethanol
acid
acid
acid
Glucose
AA + BA)
LA)



(mM)
(mM)
(mM)
(mM)
(mM)
(mM)
(g/g)
(mM/mM)
(mM/mM)

























TYS medium,
45
137
22
9
0
5
0.27
1.81
1.69


open system,


Δptb strain


TYS medium,
69
113
17
10
0
10
0.21
1.18
1.07


open system,


Wild strain









Compared to the results of the wild strain, by-product parameter and the yield from glucose were improved in Δptb strain. Furthermore, even if CaCO3 was not added, culture was successfully carried out, and the growth rate was as fast as that of the wild strain such that glucose was completely consumed at the time point of about 24 hours. Moreover, unlike the case of a precedent literature where the butyric acid production pathway for C. acetobutyricum was disrupted, no metabolic change such as abnormal elevation of acetic acid was observed.
Example 3
Butanol Fermentation Using ΔptaΔptb Strain
A transformed microorganism C. saccharoperbutylacetonicum (ΔptaΔptb strain) prepared in Example 1 was cultured and the performance of the microorganism was evaluated. 500 μL of glycerol stock of the transformed microorganism was inoculated in TYA medium (5 ml) and cultured in a test tube at 30° C. for 24 hours. 50 μL of the obtained preculture solution was inoculated in fresh TYA, TYS or TYS-CaCO3 medium (5 ml) and cultured in a test tube at 30° C. The composition of TYS medium is shown below. TYS-CaCO3 medium refers to a medium prepared by adding CaCO3 (5 g/l) to TYS medium.







TABLE 5







Composition of TYS medium










Component
Content (g/L)














D-glucose
40



Tryptone (Difco)
6



Yeast extract (Difco)
2



Ammonium sulfate
2.58



Magnesium sulfate monohydrate
0.3



Potassium dihydrogen phosphate
0.5



Ferric sulfate (II)
0.01










Culture was performed for about 96 hours in open conditions or closed condition. In TYS-CaCO3 medium, the pH value is maintained at 5 or more so as not to be lowered by the action of CaCO3. The wild strain was cultured in the same manner.
After completion of culture, the culture solution was taken and subjected to liquid chromatography to perform quantitative analysis of butanol, other alcohols, ketone and organic acids. Aminex HPX-87H Column (Bio-Rad) was used as the column. The results are shown in Tables 6 and 7. In the table, “B/(A+E+AA+BA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM) and butyric acid (mM), and is referred to as by-product parameter 1. In the table, “B/(A+E+AA+BA+LA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM), butyric acid (mM) and lactic acid (mM) and is referred to as by-product parameter 2. In addition, by-product parameter 1 and by-product parameter 2 are collectively referred to as “by-product parameter”.







TABLE 6







Δpta Δptb strain


























B/(A + E +
Lowest pH






Acetic
Butyric
Lactic
Butanol/
B/(A + E +
AA + BA +
during



Acetone
Butanol
Ethanol
acid
acid
acid
Glucose
AA + BA)
LA)
culture



(mM)
(mM)
(mM)
(mM)
(mM)
(mM)
(g/g)
(mM/mM)
(mM/mM)
(—)





















TYS medium.
0
0
0
0
0
6
0.21
—
—
4.5


open system


TYS-CaCO3
6
175
25
0
0
5
0.29
5.65
4.86
5.2


medium,


open system


TYS-CaCO3
3
184
10
0
0
6
0.31
14.15
9.68
5.7


medium,


closed system
















TABLE 7







Wild strain

























B/(A + E +






Acetic
Butyric
Lactic
Butanol/
B/(A + E +
AA + BA +



Acetone
Butanol
Ethanol
acid
acid
acid
Glucose
AA + BA)
LA)



(mM)
(mM)
(mM)
(mM)
(mM)
(mM)
(g/g)
(mM/mM)
(mM/mM)




















TYS medium,
69
113
17
10
0
5
0.21
1.18
1.12


open system


TYS-CaCO3
68
118
52
12
4
3
0.21
0.87
0.85


medium,


open system


TYS-CaCO3
39
156
32
3
1
13
0.28
2.08
1.77


medium,


closed system









The results of Table 6 show that, when pH was not controlled with CaCO3, ΔptaΔptb strain hardly grew. Since pH decreased to about 4.5, it was found that maintaining of pH to a certain level or more is necessary for growth.
Incidentally, ΔptaΔptb strain cultured in TYA medium grew well since pH was maintained at 5 or more and no pH control with CaCO3 was required.
When culture was performed in TYS-CaCO3 medium, the highest butanol concentration in the wild strain was 156 mM or less, whereas, in ΔptaΔptb strain, the concentration of butanol accumulated in the open system was 175 mM and the concentration of butanol accumulated in the closed system was 184 mM. In addition, no production of butyric acid and acetic acid was confirmed in ΔptaΔptb strain. Further, in the closed system, acetone concentration and ethanol concentration were suppressed as low as 3 mM and 10 mM, respectively. As a result, the by-product parameter increased up to 13.92. Although the by-product parameter increased up to 2.08 in the wild strain by performing culture in a closed-system, the parameter was still low compared to that of ΔptaΔptb strain.
When pH was controlled with CaCO3, the yield of butanol relative to by-products was higher in ΔptaΔptb strain than that in the wild strain in both of the open system and the closed system.
Example 4
Butanol Fermentation at Various Hydrogen Partial Pressures
A transformed microorganism C. saccharoperbutylacetonicum (ΔptaΔptb strain) prepared in Example 1 was cultured at various hydrogen partial pressures. 500 μL of glycerol stock of the transformed microorganism was inoculated in TYS-CaCO3 medium and cultured in a test tube at 30° C. for 24 hours. 50 μL of the obtained preculture solution was inoculated in fresh TYS-CaCO3 medium (5 ml) and cultured in a test tube at 30° C. The pH of the medium was controlled so as not to be lower than 5.0 by adding CaCO3 (5 g/L)
Culture was performed for 96 hours in open conditions or closed condition. In closed conditions, the hydrogen partial pressure was controlled by changing the ratio of the gas-phase portion to the culture solution portion in the test tube.
After completion of culture, the culture solution was taken and subjected to liquid chromatography to perform quantitative analysis of butanol, other alcohols, ketones and organic acids. Aminex HPX-87H Column (Bio-Rad) was used as the column. The results are shown in Table 8. In the table, “B/(A+E+AA+BA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM) and butyric acid (mM), and is referred to by-product parameter 1. In the table, “B/(A+E+AA+BA+LA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM), butyric acid (mM) and lactic acid (mM) and is referred to as by-product parameter 2. In addition, by-product parameter 1 and by-product parameter 2 are collectively referred to as “by-product parameter”.

















TABLE 8















B/(A + E +






Acetic
Butyric
Lactic
Butanol/
B/(A + E +
AA + BA +



Acetone
Butanol
Ethanol
acid
acid
acid
Glucose
AA + BA)
LA)



(mM)
(mM)
(mM)
(mM)
(mM)
(mM)
(g/g)
(mM/mM)
(mM/mM)

























Open system
6
175
25
0
0
5
0.29
5.65
4.86


Closed system
4
175
13
0
0
10
0.29
10.29
6.48


Hydrogen partial


pressure 0.06 atm


Closed system
4
182
10
0
0
9
0.3
13.00
7.91


Hydrogen partial


pressure 0.08 atm


Closed system
5
186
10
0
0
7
0.31
12.40
8.45


Hydrogen partial


pressure 0.10 atm


Closed system
3
184
10
0
0
6
0.31
14.15
9.68


Hydrogen partial


pressure 0.15 atm


Closed system
4
184
11
0
0
5
0.31
12.27
9.20


Hydrogen partial


pressure 0.20 atm


Closed system
5
177
10
0
0
5
0.31
11.80
8.85


Hydrogen partial


pressure 0.25 atm









As seen from the results of Table 8, in the case where pH was controlled with CaCO3, the ethanol accumulation amount in the open system was larger than that in the closed system and the accumulation amount was about 25 mM. As the result, the by-product parameter was higher in the closed system. It demonstrates that higher hydrogen partial pressure is advantageous for performing culture with a small amount of by-products in a condition the hydrogen partial pressure is 0.25 atm or less.
Example 5
Butanol Fermentation by ΔctfBΔptaΔptb
A transformed microorganism C. saccharoperbutylacetonicum (ΔctfBΔtaΔptb strain) prepared in Example 1 was cultured and the performance of the microorganism was evaluated. 500 μL of glycerol stock of the transformed microorganism was inoculated in TYS-CaCO3 medium and cultured in a test tube at 30° C. for 24 hours. 50 μL of the obtained preculture solution was inoculated in fresh TYS-CaCO3 medium (5 ml) and cultured in a test tube at 30° C.
Culture was performed for 96 hours in open conditions or closed condition. In pH control conditions, the pH of the medium was controlled so as not to be lower than 5 by adding CaCO3 (5 g/L).
After completion of culture, the culture solution was taken and subjected to liquid chromatography to perform quantitative analysis of butanol, other alcohols, ketone and organic acids. Aminex HPX-87H Column (Bio-Rad) was used as the column. The results are shown in Table 9. In the table, “B/(A+E+AA+BA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM) and butyric acid (mM), and is referred to as by-product parameter 1. In the table, “B/(A+E+AA+BA+LA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM), butyric acid (mM) and lactic acid (mM) and is referred to as by-product parameter 2. In addition, by-product parameter 1 and by-product parameter 2 are collectively referred to as “by-product parameter”.

















TABLE 9















B/(A + E +






Acetic
Butyric
Lactic
Butanol/
B/(A + E +
AA + BA +



Acetone
Butanol
Ethanol
acid
acid
acid
Glucose
AA + BA)
LA)



(mM)
(mM)
(mM)
(mM)
(mM)
(mM)
(g/g)
(mM/mM)
(mM/mM)

























TYS medium,
0
0
0
0
0

—
—



open system


TYS-CaCO3
0
164
19
3
0
7
0.29
7.45
5.66


medium,


open system


TYS-CaCO3
0
168
16
2
0
2
0.34
9.33
8.40


medium,


closed system









As is similar to the results of Example 3, in the culture where pH was not controlled with CaCO3, a phenomenon where pH falls down and the microorganism was not grown was observed. In the case where pH was controlled, the butanol yield and by-product parameter were higher in ΔctfBΔptaΔptb strain than those of the wild strain of Example 2. In ΔctfBΔptaΔptb strain, acetone was not produced and instead acetic acid was slightly produced as compared to the case of ΔptaΔptb strain.
Example 6
Butanol Fermentation by ΔptaΔptbΔldh1
A transformed microorganism C. saccharoperbutylacetonicum (ΔptaΔptbΔldh1 strain) prepared in Example 1 and the wild strain were cultured and the performance of the microorganisms was evaluated. 500 μL of glycerol stock of the transformed microorganism was inoculated in TYS-CaCO3 medium and cultured in a test tube at 30° C. for 24 hours. 50 of the obtained preculture solution was inoculated in fresh TYS-CaCO3 medium (5 ml) and cultured in a test tube at 30° C.
Culture was performed for 96 hours in open conditions or closed condition. The pH of the medium was controlled so as not to be lower than 5 by adding CaCO3 (5 g/L)
After completion of culture, the culture solution was taken and subjected to liquid chromatography to perform quantitative analysis of butanol, other alcohols, ketone and organic acids. Aminex HPX-87H Column (Bio-Rad) was used as the column. The results are shown in Table 10. In the table, “B/(A+E+AA+BA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM) and butyric acid (mM), and is referred to as by-product parameter 1. In the table, “B/(A+E+AA+BA+LA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM), butyric acid (mM) and lactic acid (mM) and is referred to as by-product parameter 2. In addition, by-product parameter 1 and by-product parameter 2 are collectively referred to as “by-product parameter”.
















TABLE 10














B/(A + E +






Acetic
Butyric
Lactic
Butanol/
B/(A + E +
AA + BA +



Acetone
Butanol
Ethanol
acid
acid
acid
Glucose
AA + BA)
LA)



(mM)
(mM)
(mM)
(mM)
(mM)
(mM)
(g/g)
(mM/mM)
(mM/mM)















Wild strain
















TYS-CaCO3
68
118
52
12
4
3
0.21
0.87
0.85


medium,


open system


TYS-CaCO3
39
156
32
3
1
13
0.28
2.08
1.77


medium,


closed system







ΔptaΔptbΔldh1
















TYS-CaCO3
4
169
7
0
2
5
0.32
13.00
9.39


medium,


open system


TYS-CaCO3
5
179
15
0
1
3
0.34
8.52
7.46


medium,


closed system









It was found from the results of Table 10 that the yield of butanol relative to by-products was higher in ΔptaΔptbΔldh1 strain than that of the wild strain in both of the open system and the closed system. By comparing with the results of ΔptaΔptb strain shown in Table 6, it is clear that production of lactic acid is suppressed in ΔptaΔptbΔldh1 strain, particularly in the closed system and the yield of butanol relative to by-products was further improved.
Example 7
Butanol Fermentation in Different Medium Conditions
Transformed microorganisms C. saccharoperbutylacetonicum strains (Δpta strain, Δptb strain, ΔptaΔptb strain, ΔptaΔptbΔldh1 strain) prepared in Example 1 were cultured and the performance of the microorganisms was evaluated. 500 μL of glycerol stock of the transformed microorganism was inoculated in TYS medium (5 ml) and cultured in a test tube at 30° C. for 24 hours. 50 μL of the obtained preculture solution was inoculated in fresh TYS-KH2PO4 medium (5 ml) and cultured in a test tube at 30° C. The composition of TYS-KH2PO4 medium are shown below.







TABLE 11







Composition of TYS-KH2PO4 medium










Component
Content (g/L)














D-glucose
40



Tryptone (Difco)
6



Yeast extract (Difco)
2



Ammonium sulfate
2.58



Magnesium sulfate heptahydrate
0.3



Potassium dihydrogen phosphate (KH2PO4)
0.5/1.0/2.0



Ferric sulfate (II) heptahydrate
0.01










Culture was performed for 96 hours in closed conditions in which two conditions of initial pH: 6.5 and 7.0 were employed. The wild strain was cultured in the same manner.
After completion of culture, the culture solution was taken and subjected to liquid chromatography to perform quantitative analysis of butanol, other alcohols, ketones and organic acids. Aminex HPX-87H Column (Bio-Rad) was used as the column. The results are shown in Tables 12 to 17. In the tables, “B/(A+E+AA+BA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM) and butyric acid (mM), and is referred to as by-product parameter 1. In the tables, “B/(A+E+AA+BA+LA)” represents a numerical value obtained by dividing butanol (mM) by the total of acetone (mM), ethanol (mM), acetic acid (mM), butyric acid (mM) and lactic acid (mM) and is referred to as by-product parameter 2. In addition, by-product parameter 1 and by-product parameter 2 are collectively referred to as “by-product parameter”.







TABLE 12







KH2PO4(0.5 g/L), Initial pH 6.5

























B/(A + E +






Acetic
Butyric
Lactic
Butanol/
B/(A + E +
AA + BA +



Acetone
Butanol
Ethanol
acid
acid
acid
Glucose
AA + BA)
LA)


Strain
(mM)
(mM)
(mM)
(mM)
(mM)
(mM)
(g/g)
(mM/mM)
(mM/mM)



















Wild strain
13
33
5
1
0
0
0.23
1.74
1.74


Δpta
19
113
25
0
0
0
0.29
2.57
2.57


Δptb
15
145
19
0
0
1
0.31
4.26
4.14


ΔptaΔptb
5
111
0
0
0
0
0.34
22.20
22.20


ΔptaΔptb
4
109
7
0
0
0
0.33
9.91
9.91


Δldh1
















TABLE 13







KH2PO4(0.5 g/L), Initial pH 7.0

























B/(A + E +






Acetic
Butyric
Lactic
Butanol/
B/(A + E +
AA + BA +



Acetone
Butanol
Ethanol
acid
acid
acid
Glucose
AA + BA)
LA)


Strain
(mM)
(mM)
(mM)
(mM)
(mM)
(mM)
(g/g)
(mM/mM)
(mM/mM)



















Wild strain
12
31
5
2
0
0
0.22
1.63
1.63


Δpta
21
110
29
0
0
0
0.28
2.20
2.20


Δptb
9
114
30
0
0
0
0.30
2.92
2.92


ΔptaΔptb
7
127
8
0
0
0
0.34
8.47
8.47


ΔptaΔptb
4
119
8
0
0
0
0.33
9.92
9.92


Δldh1
















TABLE 14







KH2PO4(1.0 g/L), Initial pH 6.5

























B/(A + E +






Acetic
Butyric
Lactic
Butanol/
B/(A + E +
AA + BA +



Acetone
Butanol
Ethanol
acid
acid
acid
Glucose
AA + BA)
LA)


Strain
(mM)
(mM)
(mM)
(mM)
(mM)
(mM)
(g/g)
(mM/mM)
(mM/mM)



















Wild strain
13
33
19
2
0
0
0.23
0.97
0.97


Δpta
20
102
25
1
0
0
0.28
2.22
2.22


Δptb
11
106
20
1
0
0
0.31
3.31
3.31


ΔptaΔptb
5
120
0
0
0
0
0.35
24.00
24.00


ΔptaΔptb
3
109
3
0
0
0
0.34
18.17
18.17


Δldh1
















TABLE 15







KH2PO4(1.0 g/L), Initial pH 7.0

























B/(A + E +






Acetic
Butyric
Lactic
Butanol/
B/(A + E +
AA + BA +



Acetone
Butanol
Ethanol
acid
acid
acid
Glucose
AA + BA)
LA)


Strain
(mM)
(mM)
(mM)
(mM)
(mM)
(mM)
(g/g)
(mM/mM)
(mM/mM)



















Wild strain
21
51
8
1
0
0
23.3
1.70
1.70


Δpta
36
141
22
0
0
0
26.1
2.43
2.43


Δptb
18
150
21
0
0
0
27.1
3.85
3.85


ΔptaΔptb
4
117
0
0
0
0
33.7
29.25
29.25


ΔptaΔptb
4
129
7
0
0
0
32.6
11.73
11.73


Δldh1









From Tables 12 to 15, it was found that butanol yield in relation to by-products is higher in the results of Δpta strain, Δptb strain, Δptaptb strain, Δptaptbldh1 strain than that in the wild strain when pH was controlled by KH2PO4.
The contents of all publications, patents and Japanese Patent Applications cited in the specification are incorporated in their entirety by reference.

## Claims

1. A Clostridium saccharoperbutylacetonicum strain ATCC 27021 microorganism, wherein the phosphotransbutyrylase (ptb) gene and the phosphotransacetylase (pta) gene are disrupted in the microorganism,
optionally wherein the acetoacetate decarboxylase (adc) gene or the coA transferase (ctfAB) gene is disrupted in the microorganism,
optionally wherein the lactate dehydrogenase 1 (ldh1) gene is disrupted in the microorganism, and
wherein the microorganism has an increased butanol yield as compared to a wild-type C. saccharoperbutylacetonicum strain ATCC 27021 microorganism.

2. The microorganism according to claim 1, wherein the adc gene or the ctfAB gene is disrupted in the microorganism.

3. The microorganism according to claim 1, wherein the ldh1 gene is disrupted in the microorganism.

4. A method for producing butanol, comprising a step of culturing the microorganism according to claim 1 in a medium containing a carbon source under conditions for butanol fermentation to thereby produce butanol.

5. The method according to claim 4, further comprising a step of collecting the butanol from the medium.

6. The microorganism according to claim 1, wherein the ptb gene, before disruption, comprises the nucleotide sequence of SEQ ID NO: 1.

7. The microorganism according to claim 1, wherein the pta gene, before disruption, comprises the nucleotide sequence of SEQ ID NO: 2.