WO2007113127A1

WO2007113127A1 - Process for the production of cadaverine

Info

Publication number: WO2007113127A1
Application number: PCT/EP2007/052783
Authority: WO
Inventors: Oskar Zelder; Weol Kyu Jeong; Corinna Klopprogge; Andrea Herold; Hartwig Schröder
Original assignee: Basf Se
Priority date: 2006-03-30
Filing date: 2007-03-23
Publication date: 2007-10-11
Also published as: EP2013353B1; CN101389765A; JP5745552B2; BRPI0709628A2; KR20090005099A; JP5210295B2; ES2592887T3; US8741623B2; US20090246838A1; CN102732578A; HUE030521T2; CN102732578B; KR101457229B1; CN101389765B; JP2009531042A; JP2013146269A; EP2013353A1

Abstract

Process for the production of cadaverine by constructing a recombinant microorganism which has a deregulated lysine decarboxylase gene and at least one deregulated gene selected from the group (i) which consists of aspartokinase, aspartatesemialdehyde dehydrogenase, dihydrodipicolinate synthase, dihydrodipicolinate reductase, tetrahy- drodipicolinate succinylase, succinyl-amino-ketopimelate transaminase, succinyl- diamino-pimelate desuccinylase, diaminopimelate epimerase, diaminopimelate dehydrogenase, arginyl-tRNA synthetase, diaminopimelate decarboxylase, pyruvate carboxylase, phosphoenolpyruvate carboxylase, glucose-6-phosphate dehydrogenase, transketolase, transaldolase, 6-phosphogluconolactonase, fructose 1,6-biphosphatase, homoserine dehydrogenase, phophoenolpyruvate carboxykinase, succinyl-CoA synthetase, methylmalonyl-CoA mutase, provided that if aspartokinase is deregulated as gene (i) at least a second gene (i) other than aspartokinase has to be deregulated, and cultivating said microorganism.

Description

Process for the production of cadaverine

Field of the Invention

The present invention relates to a process for the production of cadaverine. More particularly, this invention relates to the use of recombinant microorganism comprising DNA molecules in a deregulated form which are essential to produce cadaverine.

Prior Art

JP 2002223770 discloses a method for producing cadaverine by introducing a lysine decarboxylation gene and/or a lysine-cadaverine antiporter gene into a lysine producing microorganism. JP 2004222569 discloses a method for producing cadaverine by culturing recombinant coryneform bacteria having L-lysine decarboxylase activity and homoserine auxotro- phy.

SUMMARY OF THE INVENTION

In one aspect, the present invention provides a process for the production of cadaverine by constructing a recombinant microorganism which has a deregulated lysine decarboxylase and at least one deregulated gene selected from genes which are essential in the lysine biosynthetic pathway, and cultivating said microorganism. In another aspect, the present invention provides a process for the production of poly- amides comprising a step as mentioned above for the production of cadaverine and reacting that cadaverine with a dicarboxylic acid.

DETAILED DESCRIPTION OF THE INVENTION

In the description that follows, a number of terms are utilized extensively. Definitions are herein provided to facilitate understanding of the invention.

The term cadaverine means 1 ,5-diaminopentane.

Promoter. A DNA sequence which directs the transcription of a structural gene to pro- duce mRNA. Typically, a promoter is located in the 5' region of a gene, proximal to the start codon of a structural gene. If a promoter is an inducible promoter, then the rate of transcription increases in response to an inducing agent. In contrast, the rate of transcription is not regulated by an inducing agent, if the promoter is a constitutive promoter.

Enhancer. A promoter element. An enhancer can increase the efficiency with which a particular gene is transcribed into mRNA irrespective of the distance or orientation of the enhancer relative to the start site of transcription.

Expression. Expression is the process by which a polypeptide is produced from a struc- tural gene. The process involves transcription of the gene into mRNA and the translation of such mRNA into polypeptide(s).

Cloning vector. A DNA molecule, such as a plasmid, cosmid, phagemid, or bacteriophage, which has the capability of replicating autonomously in a host cell and which is used to transform cells for gene manipulation. Cloning vectors typically contain one or a small number of restriction endonuclease recognition sites at which foreign DNA sequences may be inserted in a determinable fashion without loss of an essential biological function of the vector, as well as a marker gene which is suitable for use in the identification and selection of cells transformed with the cloning vector. Marker genes typi- cally include genes that provide tetracycline resistance or ampicillin resistance.

Expression vector. A DNA molecule comprising a cloned structural gene encoding a foreign protein which provides the expression of the foreign protein in a recombinant host. Typically, the expression of the cloned gene is placed under the control of (i.e., operably linked to) certain regulatory sequences such as promoter and enhancer sequences. Promoter sequences may be either constitutive or inducible.

Recombinant host. A recombinant host may be any prokaryotic or eukaryotic cell which contains either a cloning vector or expression vector. This term is also meant to include those prokaryotic or eukaryotic cells that have been genetically engineered to contain the cloned gene(s) in the chromosome or genome of the host cell. For examples of suitable hosts, see Sambrook et al., MOLECULAR CLONING: A LABORATORY MANUAL, Second Edition, Cold Spring Harbor Laboratory, Cold Spring Harbor, N.Y. (1989) ["Sambrook"].

As used herein, a substantially pure protein means that the desired purified protein is essentially free from contaminating cellular components, as evidenced by a single band following polyacrylamide-sodium dodecyl sulfate gel electrophoresis (SDS-PAGE). The term "substantially pure" is further meant to describe a molecule which is homogeneous by one or more purity or homogeneity characteristics used by those of skill in the art. For example, a substantially pure lysine decarboxylase will show constant and reproducible characteristics within standard experimental deviations for parameters such as the following: molecular weight, chromatographic migration, amino acid composition, amino acid sequence, blocked or unblocked N-terminus, HPLC elution profile, biological activity, and other such parameters. The term, however, is not meant to ex- elude artificial or synthetic mixtures of lysine decarboxylase with other compounds. In addition, the term is not meant to exclude lysine decarboxylase fusion proteins isolated from a recombinant host.

In a first aspect, the present invention provides a process for the production of cadaver- ine by constructing a recombinant microorganism which has a deregulated lysine decarboxylase gene and at least one deregulated gene selected from the group (i) which consists of aspartokinase, aspartatesemialdehyde dehydrogenase, dihydrodipicolinate synthase, dihydrodipicolinate reductase, tetrahydrodipicolinate succinylase, succinyl- amino-ketopimelate transaminase, succinyl-diamino-pimelate desuccinylase, diamino- pimelate epimerase, diaminopimelate dehydrogenase, arginyl-tRNA synthetase, dia- minopimelate decarboxylase, pyruvate carboxylase, phosphoenolpyruvate carboxylase, glucose-6-phosphate dehydrogenase, transketolase, transaldolase, 6- phosphogluconolactonase, fructose 1 ,6-biphosphatase, homoserine dehydrogenase, phophoenolpyruvate carboxykinase, succinyl-CoA synthetase, methylmalonyl-CoA mutase, provided that if aspartokinase is deregulated as gene (i) at least a second gene (i) other than aspartokinase has to be deregulated, and cultivating said microorganism.

The methodologies of the present invention feature recombinant microorganisms, preferably including vectors or genes (e.g., wild-type and/or mutated genes) as described herein and/or cultured in a manner which results in the production of cadaver- ine.

The term "recombinant" microorganism includes a microorganism (e.g., bacteria, yeast cell, fungal cell, etc.) which has been genetically altered, modified or engineered (e.g., genetically engineered) such that it exhibits an altered, modified or different genotype and/or phenotype (e.g., when the genetic modification affects coding nucleic acid sequences of the microorganism) as compared to the naturally-occurring microorganism from which it was derived.

The term "deregulated" includes expression of a gene product (e.g., lysine decarboxylase) at a level lower or higher than that expressed prior to manipulation of the microorganism or in a comparable microorganism which has not been manipulated. In one embodiment, the microorganism can be genetically manipulated (e.g., genetically engineered) to express a level of gene product at a lesser or higher level than that ex- pressed prior to manipulation of the microorganism or in a comparable microorganism which has not been manipulated. Genetic manipulation can include, but is not limited to, altering or modifying regulatory sequences or sites associated with expression of a particular gene (e.g., by removing strong promoters, inducible promoters or multiple promoters), modifying the chromosomal location of a particular gene, altering nucleic acid sequences adjacent to a particular gene such as a ribosome binding site or transcription terminator, decreasing the copy number of a particular gene, modifying proteins (e.g., regulatory proteins, suppressors, enhancers, transcriptional activators and the like) involved in transcription of a particular gene and/or translation of a particular gene product, or any other conventional means of deregulating expression of a particu- lar gene routine in the art (including but not limited to use of antisense nucleic acid molecules, or other methods to knock-out or block expression of the target protein).

The term "deregulated gene activity", e.g. deregulated lysine decarboxylase, also means that a gene activity, e.g. a lysine decarboxylase activity, is introduced into a microorganism where the respective gene activity, e.g. the lysine decarboxylase activity, has not been observed before, e.g. by introducing a heterologous gene , e.g. a lysine decarboxylase gene in one or more copies into the microorganism preferably by means of genetic engineering.

Lysine decarboxylase catalyzes the decarboxylation of L-lysine into cadaverine. The enzyme has been classified as E. C. 4.1.1.18. The enzymes isolated from Escherichia coli having lysine decarboxylase activity are the cadA gene product (Kyoto Encyclopedia of Genes and Genomes, Entry b4131 ) and the IdcC gene product (Kyoto Encyclopedia of Genes and Genomes, Entry JW0181 ). The amino acid sequences of E. coli cadA is disclosed in SEQ ID NO:1 and of E. coli IdcC is disclosed in SEQ ID NO:2.

DNA molecules encoding the E. coli lysine decarboxylase gene can be obtained by screening cDNA or genomic libraries with polynucleotide probes having nucleotide sequences reverse-translated from the amino acid sequence of SEQ ID NO:1 or 2.

Alternatively, the E. coli lysine decarboxylase genes can be obtained by synthesizing DNA molecules using mutually priming long oligonucleotides. See, for example, Ausubel et al., (eds.), CURRENT PROTOCOLS IN MOLECULAR BIOLOGY, pages 8.2.8 to 8.2.13 (1990) ["Ausubel"]. Also, see Wosnick et al., Gene 60:1 15 (1987); and Ausubel et al. (eds.), SHORT PROTOCOLS IN MOLECULAR BIOLOGY, 3rd Edition, pages 8-8 to 8-9 (John Wiley & Sons, Inc. 1995). Established techniques using the polymerase chain reaction provide the ability to synthesize DNA molecules at least 2 kilobases in length. Adang et al., Plant Molec. Biol. 21 :1131 (1993); Bambot et al., PCR Methods and Applications 2:266 (1993); Dillon et al., "Use of the Polymerase Chain Reaction for the Rapid Construction of Synthetic Genes," in METHODS IN MOLECULAR BIOLOGY, Vol. 15: PCR PROTOCOLS: CURRENT METHODS AND APPLICATIONS, White (ed.), pages 263-268, (Humana Press, Inc. 1993); Holowachuk et al., PCR Methods Appl. 4:299 (1995).

Variants of E. coli lysine decarboxylase can be produced that contain conservative amino acid changes, compared with the parent enzyme. That is, variants can be obtained that contain one or more amino acid substitutions of SEQ ID NO:1 or 2, in which an alkyl amino acid is substituted for an alkyl amino acid in the lysine decarboxylase amino acid sequence, an aromatic amino acid is substituted for an aromatic amino acid in the E. coli lysine decarboxylase amino acid sequence, a sulfur-containing amino acid is substituted for a sulfur-containing amino acid in the E. coli lysine decarboxylase amino acid sequence, a hydroxy-containing amino acid is substituted for a hydroxy- containing amino acid in the E. coli lysine decarboxylase amino acid sequence, an acidic amino acid is substituted for an acidic amino acid in the E. coli lysine decarboxylase amino acid sequence, a basic amino acid is substituted for a basic amino acid in the E. coli lysine decarboxylase amino acid sequence.

Among the common amino acids, for example, a "conservative amino acid substitution" is illustrated by a substitution among amino acids within each of the following groups: (1 ) glycine, alanine, valine, leucine, and isoleucine, (2) phenylalanine, tyrosine, and tryptophan, (3) cysteine and methionine, (4) serine and threonine, (5) aspartate and glutamate, (6) glutamine and asparagine, and (7) lysine, arginine and histidine.

Conservative amino acid changes in the E. coli lysine decarboxylase can be introduced by substituting nucleotides for the nucleotides recited in SEQ ID NO:1 or NO:2. Such "conservative amino acid" variants can be obtained, for example, by oligonucleotide- directed mutagenesis, linker-scanning mutagenesis, mutagenesis using the polymerase chain reaction, and the like. Ausubel et al., supra, at pages 8.0.3-8.5.9; Ausu- bel et al. (eds.), SHORT PROTOCOLS IN MOLECULAR BIOLOGY, 3rd Edition, pages 8-10 to 8-22 (John Wiley & Sons, Inc. 1995). Also see generally, McPherson (ed.), DIRECTED MUTAGENESIS: A PRACTICAL APPROACH, IRL Press (1991 ). The ability of such variants to convert L-lysine to cadaverine can be determined using a standard enzyme activity assay, such as the assay described herein.

Preferred lysine decarboxylases according to the invention are the lysine decarboxylase from E. coli and their equivalent genes, which have up to 80%, preferably 90% and most preferred 95% and 98% sequence identity (based on amino acid sequence) with the corresponding "original" gene product and have still the biological activity of lysine decarboxylase. These equivalent genes can be easily constructed by introducing nucleotide substitutions, deletions or insertions by methods known in the art.

Another preferred embodiment of the invention are the lysine decarboxylases of E. coli ( SEQ ID NO:1 and NO:2) which are retranslated into DNA by applying the codon us- age of Corynebacterium glutamicum. These lysine decarboxylase polynucleotide sequences are useful for expression of lysine decarboxylase in microorganism of the genus Corynebacterium, especially C. glutamicum.

In addition to the deregulated lysine decarboxylase gene the microorganism according to the invention must have at least one deregulated gene selected from the group (i). The group (i) is a group of genes which play a key role in the biosynthesis of lysine and consists of the genes of aspartokinase, aspartatesemialdehyde dehydrogenase, dihydrodipicolinate synthase, dihydrodipicolinate reductase, tetrahydrodipicolinate suc- cinylase, succinyl-amino-ketopimelate transaminase, succinyl-diamino-pimelate de- succinylase, diaminopimelate epimerase, diaminopimelate dehydrogenase, arginyl- tRNA synthetase, diaminopimelate decarboxylase, pyruvate carboxylase, phosphoe- nolpyruvate carboxylase, glucose-6-phosphate dehydrogenase, transketolase, transal- dolase, δ-phosphogluconolactonase, fructose 1 ,6-biphosphatase, homoserine dehydrogenase, phophoenolpyruvate carboxykinase, succinyl-CoA synthetase, methyl- malonyl-CoA mutase.

At least one gene of the group (i) has to be deregulated according to the inventive process. Preferably more than one gene of group (i) , e.g. two, three, four, five, six, seven, eight, nine, ten genes are deregulated in the microorganism according to the invention.

The genes and gene products of group (i) are known in the art. EP 1108790 discloses mutations in the genes of homoserinedehydrogenase and pyruvatecarboxylase which have a beneficial effect on the productivity of recombinant corynebacteria in the production of lysine. WO 00/63388 discloses mutations in the gene of aspartokinase which have a beneficial effect on the productivity of recombinant corynebacteria in the production of lysine. EP 1108790 and WO 00/63388 are incorporated by reference with respect to the mutations in these genes described above.

In the table below for every gene / gene product possible ways of deregulation of the respective gene are mentioned. The literature and documents cited in the row "Deregulation" of the table are herewith incorporated by reference with respect to gene deregulation. The ways mentioned in the table are preferred embodiments of a deregulation of the respective gene.

Table. 1

A preferred way of deregulation of the genes of aspartokinase, aspartatesemialdehyde dehydrogenase, dihydrodipicolinate synthase, dihydrodipicolinate reductase, tetrahy- drodipicolinate succinylase, succinyl-amino-ketopimelate transaminase, succinyl- diamino-pimelate desuccinylase, diaminopimelate epimerase, diaminopimelate dehydrogenase, arginyl-tRNA synthetase, diaminopimelate decarboxylase, pyruvate carboxylase, phosphoenolpyruvate carboxylase, glucose-6-phosphate dehydrogenase, transketolase, transaldolase, 6-phosphogluconolactonase, fructose 1 ,6-biphosphatase is an "up"- mutation which increases the gene activity e.g. by gene amplification using strong expression signals and/or point mutations which enhance the enzymatic activity.

A preferred way of deregulation of the genes of homoserine dehydrogenase, phophoe- nolpyruvate carboxykinase, succinyl-CoA synthetase, methylmalonyl-CoA mutase is a "down"- mutation which decreases the gene activity e.g. by gene deletion or disruption, using weak expression signals and/or point mutations which destroy or decrease the enzymatic activity.

If aspartokinase is deregulated as a member of gene (i) group at least a second gene (i) member - other than aspartokinase - has to be deregulated also.

It has been observed that a significant portion of the cadaverine produced in the microorganism according to the inventive process is acetylated. In order to block this acety- lation reaction which is attributed to an acetyl-CoA dependent diamine acetyltrans- ferase and in order to increase the yield of cadaverine it is a preferred embodiment of the invention to deregulate the diamine acetyltransferase of the producing microorganism, especially to decrease its activity, e.g by deletion or disruption of the gene.

To express the deregulated genes according to the invention , the DNA sequence encoding the enzyme must be operably linked to regulatory sequences that control tran- scriptional expression in an expression vector and then, introduced into either a pro- karyotic or eukaryotic host cell. In addition to transcriptional regulatory sequences, such as promoters and enhancers, expression vectors can include translational regula- tory sequences and a marker gene which is suitable for selection of cells that carry the expression vector.

Suitable promoters for expression in a prokaryotic host can be repressible, constitutive, or inducible. Suitable promoters are well-known to those of skill in the art and include promoters capable of recognizing the T4, T3, Sp6 and T7 polymerases, the PR and PL promoters of bacteriophage lambda, the trp, recA, heat shock, lacUVδ, tac, Ipp-lacλpr, phoA, gal, trc and lacZ promoters of E. coli, the α-amylase and the σ²⁸ -specific promoters of B. subtilis, the promoters of the bacteriophages of Bacillus, Streptomyces promoters, the int promoter of bacteriophage lambda, the bla promoter of the β- lactamase gene of pBR322, and the CAT promoter of the chloramphenicol acetyl transferase gene. Prokaryotic promoters are reviewed by Glick, J. Ind. Microbiol. 1 :277 (1987); Watson et al., MOLECULAR BIOLOGY OF THE GENE, 4th Ed., Benjamin Cummins (1987); Ausubel et al., supra, and Sambrook et al., supra.

A preferred promoter for the expression of the E. coli lysine decarboxylase is the sodA promoter of C. glutamicum.

Methods for expressing proteins in prokaryotic hosts are well-known to those of skill in the art. See, for example, Williams et al., "Expression of foreign proteins in E. coli using plasmid vectors and purification of specific polyclonal antibodies," in DNA CLONING 2: EXPRESSION SYSTEMS, 2nd Edition, Glover et al. (eds.), pages 15-58 (Oxford University Press 1995). Also see, Ward et al., "Genetic Manipulation and Expression of Antibodies," in MONOCLONAL ANTIBODIES: PRINCIPLES AND APPLICATIONS, pages 137-185 (Wiley-Liss, Inc. 1995); and Georgiou, "Expression of Proteins in Bacteria," in PROTEIN ENGINEERING: PRINCIPLES AND PRACTICE, Cleland et al. (eds.), pages 101 -127 (John Wiley & Sons, Inc. 1996).

An expression vector can be introduced into bacterial host cells using a variety of tech- niques including calcium chloride transformation, electroporation, and the like. See, for example, Ausubel et al. (eds.), SHORT PROTOCOLS IN MOLECULAR BIOLOGY, 3rd Edition, pages 1-1 to 1-24 (John Wiley & Sons, Inc. 1995).

An important aspect of the present invention involves cultivating or culturing the re- combinant microorganisms described herein, such that a desired compound cadaver- ine is produced. The term "cultivating" includes maintaining and/or growing a living microorganism of the present invention (e.g., maintaining and/or growing a culture or strain). In one embodiment, a microorganism of the invention is cultured in liquid media. In another embodiment, a microorganism of the invention is cultured in solid media or semi-solid media. In a preferred embodiment, a microorganism of the invention is cultured in media (e.g., a sterile, liquid media) comprising nutrients essential or beneficial to the maintenance and/or growth of the microorganism.

Carbon sources which may be used include sugars and carbohydrates, such as for example glucose, sucrose, lactose, fructose, maltose, molasses, starch and cellulose, oils and fats, such as for example soy oil, sunflower oil, peanut oil and coconut oil, fatty acids, such as for example palmitic acid, stearic acid and linoleic acid, alcohols, such as for example glycerol and ethanol, and organic acids, such as for example acetic acid. In a preferred embodiment, glucose, fructose or sucrose are used as carbon sources. These substances may be used individually or as a mixture.

Nitrogen sources which may be used comprise organic compounds containing nitrogen, such as peptones, yeast extract, meat extract, malt extract, corn steep liquor, soya flour and urea or inorganic compounds, such as ammonium sulfate, ammonium chloride, ammonium phosphate, ammonium carbonate and ammonium nitrate. The nitrogen sources may be used individually or as a mixture. Phosphorus sources which may be used are phosphoric acid, potassium dihydrogen phosphate or dipotassium hydrogen phosphate or the corresponding salts containing sodium. The culture medium must furthermore contain metal salts, such as for example magnesium sulfate or iron sulfate, which are necessary for growth. Finally, essential growth-promoting sub- stances such as amino acids and vitamins may also be used in addition to the above- stated substances. Suitable precursors may furthermore be added to the culture medium. The stated feed substances may be added to the culture as a single batch or be fed appropriately during cultivation.

Preferably, microorganisms of the present invention are cultured under controlled pH. The term "controlled pH" includes any pH which results in production of the desired fine chemical, e.g., cadaverine. In one embodiment, microorganisms are cultured at a pH of about 7. In another embodiment, microorganisms are cultured at a pH of between 6.0 and 8.5. The desired pH may be maintained by any number of methods known to those skilled in the art. For example, basic compounds such as sodium hydroxide, potassium hydroxide, ammonia, or ammonia water, or acidic compounds, such as phosphoric acid or sulfuric acid, are used to appropriately control the pH of the culture.

Also preferably, microorganisms of the present invention are cultured under controlled aeration. The term "controlled aeration" includes sufficient aeration (e.g., oxygen) to result in production of the desired fine chemical, e.g., cadaverine. In one embodiment, aeration is controlled by regulating oxygen levels in the culture, for example, by regulating the amount of oxygen dissolved in culture media. Preferably, aeration of the culture is controlled by agitating the culture. Agitation may be provided by a propeller or simi- lar mechanical agitation equipment, by revolving or shaking the growth vessel (e.g., fermentor) or by various pumping equipment. Aeration may be further controlled by the passage of sterile air or oxygen through the medium (e.g., through the fermentation mixture). Also preferably, microorganisms of the present invention are cultured without excess foaming (e.g., via addition of antifoaming agents such as fatty acid polyglycol esters).

Moreover, microorganisms of the present invention can be cultured under controlled temperatures. The term "controlled temperature" includes any temperature which results in production of the desired fine chemical, e.g., cadaverine. In one embodiment, controlled temperatures include temperatures between 15 °C and 95 °C. In another embodiment, controlled temperatures include temperatures between 15 °C and 70 °C. Preferred temperatures are between 20 °C and 55 °C, more preferably between 30 °C and 45 ⁰C or between 30 ⁰C and 50 ⁰C.

Microorganisms can be cultured (e.g., maintained and/or grown) in liquid media and preferably are cultured, either continuously or intermittently, by conventional culturing methods such as standing culture, test tube culture, shaking culture (e.g., rotary shaking culture, shake flask culture, etc.), aeration spinner culture, or fermentation. In a preferred embodiment, the microorganisms are cultured in shake flasks. In a more preferred embodiment, the microorganisms are cultured in a fermentor (e.g., a fermentation process). Fermentation processes of the present invention include, but are not limited to, batch, fed-batch and continuous methods of fermentation. The phrase "batch process" or "batch fermentation" refers to a closed system in which the composition of media, nutrients, supplemental additives and the like is set at the beginning of the fermentation and not subject to alteration during the fermentation, however, attempts may be made to control such factors as pH and oxygen concentration to pre- vent excess media acidification and/or microorganism death. The phrase "fed-batch process" or "fed-batch" fermentation refers to a batch fermentation with the exception that one or more substrates or supplements are added (e.g., added in increments or continuously) as the fermentation progresses. The phrase "continuous process" or "continuous fermentation" refers to a system in which a defined fermentation medium is added continuously to a fermentor and an equal amount of used or "conditioned" medium is simultaneously removed, preferably for recovery of the desired cadaverine. A variety of such processes have been developed and are well-known in the art.

The methodology of the present invention can further include a step of recovering cadaverine. The term "recovering" cadaverine includes extracting, harvesting, isolating or purifying the compound from culture media. Recovering the compound can be performed according to any conventional isolation or purification methodology known in the art including, but not limited to, treatment with a conventional resin (e.g., anion or cation exchange resin, non-ionic adsorption resin, etc.), treatment with a conventional adsorbent (e.g., activated charcoal, silicic acid, silica gel, cellulose, alumina, etc.), alteration of pH, solvent extraction (e.g., with a conventional solvent such as an alcohol, ethyl acetate, hexane and the like), distillation, dialysis, filtration, concentration, crystallization, recrystallization, pH adjustment, lyophilization and the like. For example ca- daverine can be recovered from culture media by first removing the microorganisms . The broth removed biomass is then passed through or over a cation exchange resin to remove unwanted cations and then through or over an anion exchange resin to remove unwanted inorganic anions and organic acids having stronger acidities than cadaverine.

In another aspect, the present invention provides a process for the production of poly- amides (e.g. nylon ®) comprising a step as mentioned above for the production of cadaverine. The cadaverine is reacted in a known manner with di-, tri- or polycarboxylic acids to get polyamides. Preferably the cadaverine is reacted with dicarboxylic acids containing 4 to 10 carbons such as succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, and so forth. The dicarboxylic acid is preferably a free acid.

Examples 1. Cloning of the lysine decarboxylase gene PCR primers, WKJ12/WKJ13 and WKJ35/WKJ34, were used with the chromosomal DNA of E. coli as a template to amplify the DNA fragments containing cadA and IdcC gene, respectively. The amplified DNA fragments were purified, digested with restriction enzymes, Asp718/Ndel for cadA and Xhol/Spel for IdcC, and ligated to the pClikδaMCS vector digested with same restriction enzymes resulting in pClikδaMCS cadA and pClikδaMCS IdcC, respectively.

To increase expression of the IdcC gene, C. glutamicum sodA promoter (Psod) was substituted in front of start codon of the gene. The DNA fragments containing the sodA pro- moter and coding region of the IdcC gene were amplified from each chromosomal DNA using PCR primers, WKJ31/OLD47 for Psod and WKJ33/WKJ34 for IdcC, and used as a template for fusion PCR with primers WKJ31/WKJ34. The fused PCR fragment was purified, digested with Xhol and Spel, and inserted between Xhol and Spel cleavage sites of the pClikδaMCS vector to construct pClikδaMCS Psod-ldcC.

Oligonucleotide primers used:

WKJ 12 caagctccttcgagctggca

WKJ 13 gggtaacgtaaaccagagaa

WKJ31 gagagagactcgagtagctgccaattattccggg WKJ33 acgaaaggattttttacccatgaacatcattgccattatg

WKJ 34 ctctctctcactagtgctcaatcacatattgccca

WKJ35 gagagagactcgagccggaagcgatggcggcatc

OLD47 gggtaaaaaatcctttcgtag

2. Construction of cadaverine production strain

To construct a cadaverine production strain, a lysine producer LU 11271 , which was derived from C. glutamicum wild type strain ATCC13032 by incorporation of a point mutation T3111 into the aspartokinase gene, duplication of the diaminopimelate dehydro- genase gene and disruption of the phosphoenolpyruvate carboxykinase gene, was transformed with the recombinant plasmids having the lysine decarboxylase genes.

3. Cadaverine production in shaking flask culture

Shaking flask experiments were performed on the recombinant strains to test the cadaverine production. The same culture medium and conditions as lysine production were employed as described in WO2005059139. For the control host strain and recombinant strain having pClikδaMCS were tested in parallel. The strains were pre-cultured on CM agar overnight at 30 °C. Cultured cells were harvested in a microtube containing 1.5 ml of 0.9 % NaCI and cell density was determined by the absorbance at 610 nm following vortex. For the main culture suspended cells were inoculated to reach 1.5 of initial OD into 10 ml of the production medium contained in an autoclaved 100 ml of Erlenmeyer flask having 0.5 g of CaCO3. Main culture was performed on a rotary shaker (Infers AJ 118, Bottmingen, Switzerland) with 200 rpm for 48-78 hours at 30 °C. The concentrations of cadaverine and lysine were determined using HPLC (Agilent 1100 Series LC system).

In the broth cultured with all recombinant strains containing the lysine decarboxylase genes a significant amount of cadaverine was accumulated. On the contrary, marked decrease in the lysine productivity was observed. Considering complete conversion of lysine to cadaverine the same number of cadaverine molecules as lysine must be pro- duced. However, the amount of cadaverine accumulated was less than that of lysine produced by host strain, on the other hand, a considerable amount of byproduct, acetyl- cadaverine, was concomitantly accumulated resulting in sugar yield decrease. In addition to HPLC analysis, cadaverine and acetylcadaverine were identified by mass spectrometrical method.

4. Identification of the acetylcadaverine-forming enzyme

To identify the acetylcadaverine-forming enzyme protein purification was performed. The C. glutamicum strain ATCC13032 or of some derivatives cultured in CM liquid were har- vested, washed and suspended in 0.5 volume of standard buffer consisting of 50 mM Tris-HCI (pH 7.8), 0.02 % Brij 35, protein inhibitor mix (Complete, Roche) and 20 % glycerol. Cell suspension was disrupted using Microfluidizer (M-110EH, Microfluidics Co.) followed by filtration using Microfiltrater (MF42, Satorius). The enzyme in the filtrate was purified by applying to a series of columns of Q Sepha- rose (Amersham Bioscience, 50 x 300 mm, linear gradient of 0.0-0.5 M-NaCI in 10 mM Tris (pH 7.5) buffer, 10 ml/min of flow rate), Phenyl Sepharose (Amersham Bioscience, 50 x 300 mm, linear gradient of 1.5-0.0 M-ammonium acetate in 10 mM Tris (pH 7.5) buffer, 10 ml/min of flow rate), Superdex (Amersham Bioscience, 26 x 600 mm, 10 mM Tris (pH 7.5) buffer, 4 ml/min of flow rate), Mono-Q (Amersham Bioscience, 5 x 50 mm, linear gradient of 0.0-0.5 M-NaCI in 10 mM Tris (pH 7.5) buffer, 1 ml/min of flow rate) and Superose (Amersham Bioscience, 15 x 300 mm, 10 mM Tris (pH 7.5) buffer, 0.3 ml/min of flow rate). All through the purification steps enzyme activity of the acetyltransferase in the fractions and the presence of acetylcadaverine in the mixture of enzyme reactions were monitored. Enzyme activity was determined by monitoring increase of absorption at 412 nm due to the generation of TNB (thionitrobenzoic acid) in a total volume of 1 ml under the following conditions:

10 mM Tris-HCI (pH 7.8), 0.1 mM DTNB (5,5'-dithiobis-(2-nitrobenzoic acid)), 0.25 mM acetyl CoA, 5 mM cadaverine, enzyme solution

Specific activities were calculated using the molar extinction coefficient of 13.6 mM-¹ x cm-¹ for TNB.

The fractions containing enzyme activity from Superose column were loaded on SDS- PAGE gel. The protein spots were digested with modified trypsin (Roche, Mannheim) as described by Hermann et al. (Electrophoresis (2001 ), 22, 1712-1723) following excising from Coomassie-stained gel. Mass spectrometrical identifications were performed on an LCQ advantage (Thermo Electron) after nano-HPLC separation of the peptides (LC Packings, RP18 column, length 15 cm, i.d. 75 μm), using the MASCOT software (David et al. (1999) Electrophoresis, 20, 3551-3567). Consequently, an acetyltransferase (Genebank accession number: NP_600742) was identified as a potential acetylcadaver- ine-forming enzyme.

5. Plasmid construction and disruption of the acetyltransferase gene

For the chromosomal disruption of the gene encoding the acetyltransferase identified a recombinant plasmid was constructed which allows the marker-free manipulation by two consecutive homologous recombination events. The DNA fragments containing the regions of the up- and the downstream of the gene were amplified from C. glutamicum chromosomal DNA using a sets of PCR primers, WKJ203/WKJ205 for the upstream and WKJ206/WKJ204 for the downstream, and used as a template for fusion PCR with PCR primers WKJ203/WKJ204 to make fused fragment that the middle region of the gene is removed. The product of the fusion PCR was purified, digested with Xhol and Spel, and inserted into the pClikintsacB vector, which makes the integration of sequences at the genomic locus of C. glutamicum (Becker et al (2005), Applied and Environmental Micro- biology, 71 (12), p.8587-8596), digested with same restriction enzymes.

The plasmid was then used to disrupt the native coding region of the acetyltransferase gene. The strain used was LU11271 LdcC in which the IdcC gene was integrated into the bioD locus of the chromosome and which produces both cadaverine and acetylca- daverine. Two consecutive recombination events, one in each of the up- and the downstream region, respectively, are necessary to disrupt the middle sequence of the gene. The disrupted mutants were confirmed by PCR with primers WKJ203/WKJ204 and Southern hybridization analysis.

Oligonucleotide primers used: WKJ203 gctcctcgaggcattgtatactgcgaccact WKJ204 cggtactagtgtagtgagccaagacatgg WKJ205 cgattccgtgattaagaagcgcttcaaccagaacatcgac WKJ206 gtcgatgttctggttgaagcgcttcttaatcacggaatcg

6. Effect on acetylcadaverine formation and cadaverine productivity

To analyze the effect of the disruption of the acetyltransferase gene on acetylcadaverine formation and cadaverine productivity, shaking flask experiments were performed on the disrupted mutants. The same culture medium and conditions as cadaverine production were used (vide supra). The disrupted mutants showed no accumulation of acetylcadaverine. This indicates that only the acetyltransferase identified is responsible for the acetylcadaverine formation. Consequently, cadaverine productivity was improved by disruption of the gene resulting in elimination of acetylcadaverine formation.

The gene sequence and the polypeptide sequence of acetyltransferase is disclosed below:

Acetyltransferase gene sequence

ATGAGTCCCACCGTTTTGCCTGCTACACAAGCTGACTTCCCTAAGATCGTC- GATGTTCTGGTTGAAGCATTCGCCAACGATCCAGCATTTTTACGATGGATCCCG- CAGCCGGACCCCGGTTCAGCAAAGCTTCGAGCACTTTTCGAACTGCAGATTGAGAAG- CAGTATGCAGTGGCGGGAAATATTGATGTCGCGCGTGATTCTGAGGGAGA- AATCGTCGGCGTCGCGTTATGGGATCGGCCAGATGGTAATCACAGTGCCAAAGAT- CAAGCAGCGATGCTCCCCCGGCTCGTCTCCATTTTCGGGATCAAGGCTGCG- CAGGTGGCGTGGACGGATTTGAGTTCGGCTCGTTTCCACCCCAAATTCCCCCATTGG- TACCTCTACACCGTGGCAACATCTAGTTCTGCCCGTGGAACGGGTGTTGG-

CAGTGCGCTTCTTAATCACGGAATCGCTCGCGCGGGTGATGAAGCTATCTATTTG- GAGGCGACGTCGACTCGTGCGGCTCAACTATATAACCGTCTGG- GATTTGTGCCCTTGGGTTATATCCCCTCAGATGATGATGGCACTCCTGAACTGGC- GATGTGGAAACCGCCAGCGATGCCAACTGTTTAA Protein sequence

MSPTVLPATQADFPKIVDVLVEAFANDPAFLRWIPQPDPGSAKLRALFELQIEKQYA- VAGNIDVARDSEGEIVGVALWDRPDGNHSAKDQAAMLPRLVSIFGIKAAQVAWTDLS- SARFHPKFPHWYLYTVATSSSARGTGVGSALLNHGIARAGDEAIYLEATSTRAAQ- LYNRLGFVPLGYIPSDDDGTPELAMWKPPAMPTV

Claims

1. Process for the production of cadaverine by constructing a recombinant microorganism which has a deregulated lysine decarboxylase gene and at least one deregulated gene selected from the group (i) which consists of aspartokinase, aspartatesemialdehyde dehydrogenase, dihydrodipicolinate synthase, dihydro- dipicolinate reductase, tetrahydrodipicolinate succinylase, succinyl-amino- ketopimelate transaminase, succinyl-diamino-pimelate desuccinylase, dia- minopimelate epimerase, diaminopimelate dehydrogenase, arginyl-tRNA syn- thetase, diaminopimelate decarboxylase, pyruvate carboxylase, phosphoe- nolpyruvate carboxylase, glucose-6-phosphate dehydrogenase, transketolase, transaldolase, 6-phosphogluconolactonase, fructose 1 ,6-biphosphatase, ho- moserine dehydrogenase, phophoenolpyruvate carboxykinase, succinyl-CoA synthetase, methylmalonyl-CoA mutase, provided that if aspartokinase is de- regulated as gene (i) at least a second gene (i) other than aspartokinase has to be deregulated, and cultivating said microorganism.

2. Process according to claim 1 , wherein the microorganism belongs to the genus Corynebacterium.

3. Process according to claim 1 , wherein the microorganism is Corynebacterium glutamicum.

4. Process according to claim 1 , wherein the deregulated lysine decarboxylase is heterologous to that microorganism.

5. Process according to claim 1 , wherein the recombinant microorganism has a lysine decarboxylase from Escherichia.

6. Process according to claim 1 , wherein the lysine decarboxylase has the polypeptide sequence of SEQ ID NO: 1 or 2 or a polypeptide sequence with a lysine decarboxylase activity which is at least 80% identical to SEQ ID NO: 1 or 2.

7. Process according to claim 1 , wherein the diamine acetyltransferase activity of the MO is deregulated.

8. Process for the production of a polyamide comprising the production of cadaverine according to claim 1 and the reaction of that cadaverine with a dicar- boxylic acid.