# Patent

## Title
Compositions and methods for enhanced bacterial exopolysaccharide production

## Abstract

The present invention provides nucleic acid sequences and variants thereof capable of modulating exopolysaccharide production in Sphingomonas, and provides methods of using such nucleic acid sequences to generate bacteria that hyper-produce exopolysaccharide in slime form.

## Background
CROSS-REFERENCE TO RELATED APPLICATION
This application is a divisional of U.S. patent application Ser. No. 10/897,981, filed Jul. 23, 2004, now pending, which application is incorporated herein by reference in its entirety.


BACKGROUND OF THE INVENTION
Field of the Invention
The present invention relates generally to the production of exopolysaccharides, and more specifically, to a nucleic acid sequence and variants thereof capable of modulating exopolysaccharide production, and to the use of such nucleic acid sequences to generate bacteria that hyper-produce exopolysaccharide in slime form.
STATEMENT REGARDING SEQUENCE LISTING
The Sequence Listing associated with this application is provided in text format in lieu of a paper copy, and is hereby incorporated by reference into the specification. The name of the text file containing the Sequence Listing is 850136—421D2_SEQUENCE_LISTING.txt. The text file is 13 KB, was created on Dec. 8, 2009, and is being submitted electronically via EFS-Web.
Description of the Related Art
There is an increasing demand for inexpensive and environmentally acceptable gelling agents for industrial applications and for the food industry. Some exemplary industrial applications of gelling agents include oil field drilling, adhesives, paints, animal feed, household products, personal care products (e.g., shampoo, lotion), oral care products (e.g., toothpaste), pharmaceuticals, and the like. Some exemplary uses of gelling agents in the food industry include use in pudding, dairy products, pie filling, dressings, confectionery, sauces, syrups, and the like. The biotechnology industry has responded to this demand for gelling agents by increasing the availability of a variety of bacterial exopolysaccharide products that are acceptable for commercial use.
Bacterial exopolysaccharides are useful compounds as gelling or viscosity increasing agents because of their distinctive rheological properties (e.g., resistance to shear, compatibility with various ionic compounds, stability to extreme temperatures, pH and salt concentrations). A variety of bacteria produce exopolysaccharides particularly useful as thickening or gelling agents. For example, a genus of bacteria that produces many types of exopolysaccharides is Sphingomonas. A few such polysaccharides include gellan, welan, rhamsan, S-7, and S-88 (see, e.g., Pollock, J. Gen. Microbiol. 139:1939, 1993). The exopolysaccharides produced by Sphingomonas are referred to as “sphingans,” and at least three sphingans (gellan, welan, and rhamsan) are commercially produced by large-scale, submerged fermentation.
Many bacterial exopolysaccharide products offer a range of attractive improvements over synthetically produced materials, but they remain relatively expensive to produce because of the costs associated with recovery and purification of a desired product. Furthermore, conditions that allow for higher fermentation yields of exopolysaccharides also result in increased broth viscosity, which thickening ultimately requires higher energy input to effectively disperse oxygen and nutrients to allow sufficient bacterial growth in the fermentation broth. That is, fermentations that provide higher exopolysaccharide yields have also resulted in correspondingly higher production costs.
Hence, a need exists for a better understanding of bacterial biosynthesis of exopolysaccharide to aid in the identification of bacteria that produce more exopolysaccharide, and that produce exopolysaccharide in a form that does not increase the viscosity of a fermentation broth. In addition, a need exists for methods of making or identifying such bacteria, which in turn would allow optimization of exopolysaccharide production and yield under typical, industrial fermentation conditions. The present invention meets such needs, and further provides other related advantages.
BRIEF SUMMARY OF THE INVENTION
The present invention relates generally to the use of a nucleic acid sequence and variants thereof capable of modulating exopolysaccharide production, and to methods of using such nucleic acid sequences to generate bacteria that hyper-produce exopolysaccharide in slime form.
In one aspect, the present invention provides an isolated nucleic acid molecule comprising a sequence that remains hybridized under highly stringent conditions to a probe, wherein the probe consists of SEQ ID NO:1 or a complement of SEQ ID NO:1. In one embodiment, the aforementioned isolated nucleic acid molecules wherein said nucleic acid molecules encode at least one polypeptide capable of altering exopolysaccharide production in a Sphingomonas species. In related embodiments, the at least one encoded polypeptide comprises an amino acid sequence that is at least 80% identical to SEQ ID NO:2, or the encoded polypeptide comprises an amino acid sequence of SEQ ID NO:2 with conservative amino acid substitutions, or the polypeptide comprises the amino acid sequence of SEQ ID NO:2, or the polypeptide consists of the amino acid sequence of SEQ ID NO:2. In still another embodiment, the invention provides an isolated nucleic acid molecule comprising a nucleotide sequence as set forth in SEQ ID NO:1 or a complement of SEQ ID NO:1. In yet other embodiments, any of the aforementioned nucleic acid molecules are DNA or RNA.
In another embodiment, the invention provides a recombinant expression vector comprising at least one promoter operably linked to anyone of the aforementioned nucleic acid molecules. In still another embodiment, the recombinant expression vector expresses the modulator polypeptide as a fusion protein comprising a polypeptide product encoded by a second nucleic acid sequence, such as a tag or an enzyme. In certain embodiments, the recombinant expression vector has a regulated promoter. In still other embodiments, the recombinant expression vector is a plasmid. In yet another embodiment, the recombinant expression vector is plasmid X026 or plasmid X029 (ATCC PTA-5127). In one embodiment, the recombinant expression vector comprises at least one promoter operably linked to a nucleic acid molecule that comprises a nucleotide sequence as set forth in SEQ ID NO:1.
In still another embodiment, the present invention relates to a host cell comprising any of the aforementioned recombinant expression vectors. In certain embodiments, the host cell is a prokaryotic cell, such as a sphingan-producing bacterium or a Sphingomonas cell or a sphingan-producing Sphingomonas bacterium. In other embodiments, the host cell is a Sphingomonas bacterium capable of producing a sphingan such as gellan, welan, rhamsan, diutan, alcalan, S7, S88, S198, and NW11. In still other embodiments, the host cell produces a sphingan in capsule form or slime form. In certain embodiments, the host cell is Sphingomonas strain α252 (ATCC PTA-5128, Welam Slime), X287 (ATCC PTA-3487, Gellan Slime), X530 (ATCC PTA-3486), Z473 (ATCC PTA-3485), X031 (ATCC PTA-3488), or α27. In a related embodiment, the host cell is a xanthan-producing bacterium, such as a Xanthomonas bacterium and more specifically Xanthomonas strains X59 (ATCC 55298), X55 (ATCC 13951), α287, α300, or α301. In certain embodiments, the polypeptide or fusion protein expressed from the nucleic acid on the recombinant expression vector alters the level of exopolysaccharide production in the host cell.
In yet another aspect, the invention provides an isolated bacterium that produces exopolysaccharide, comprising a bacterium capable of producing exopolysaccharide in slime form even when expressing a polypeptide encoded by any of the aforementioned nucleic acid molecules and wherein the bacteria are any of the aforementioned bacteria, including a mutant of Sphingomonas strain α027; or a mutant of Xanthomonas strains α287, α300, or α301. In other embodiments, the bacterium that produces exopolysaccharide in slime form when expressing at least one polypeptide encoded by any of the aforementioned nucleic acid molecules is strain α062 (ATCC PTA-4426), α063, α065, or α069 or Xanthomonas strains α449 (ATCC PTA-5064), α485, or α525. In yet other embodiments, the invention provides an isolated bacterium selected from Sphingomonas strain α062 (ATCC PTA-4426), α063, α065, or α069 and mutants or derivatives thereof, wherein the bacteria are capable of producing an exopolysaccharide in slime form even when expressing at least one polypeptide encoded by any of the aforementioned nucleic acid molecules, and mixtures thereof of such bacteria. In still other embodiments, the invention provides an isolated bacterium selected from Xanthomonas strain α449 (ATCC PTA-5064), α485, or α525, and mutants or derivatives thereof, wherein the bacteria are capable of producing an exopolysaccharide in slime form even when expressing at least one polypeptide encoded by any of the aforementioned nucleic acid molecules, and mixtures thereof.
It is another aspect of the invention to provide a method for hyper-producing exopolysaccharide, comprising culturing bacteria under conditions and for a time sufficient to permit exopolysaccharide production, wherein the bacteria hyper-produce exopolysaccharide in slime form when expressing at least one polypeptide encoded by any of the aforementioned nucleic acid molecules; and separating the exopolysaccharide in slime form from such a culture. In certain embodiments, the bacteria are Sphingomonas bacteria, such as those capable of hyper-producing an exopolysaccharide selected from gellan, welan, rhamsan, diutan, alcalan, S7, S88, S198, and NW11, including Sphingomonas strains α062 (ATCC PTA-4426), α063, α065 and α069. In certain other embodiments, the bacteria are Xanthomonas bacteria, such as those capable of hyper-producing xanthan, including Xanthomonas strains α449 (ATCC PTA-5064), α485, and α525. Also provided are any of the aforementioned methods wherein the culturing comprises fermentation, or wherein the bacteria produce from about 20 grams to about 60 grams of exopolysaccharide per liter of culture. In some embodiments, the fermentation is conducted from about 48 hours to about 96 hours at a temperature ranging from about 25° C. to about 35° C. In still other embodiments, the invention provides any of the aforementioned methods wherein the separating of exopolysaccharide from the bacteria is by alcohol precipitation, such as by adding about 1 to about 1.5 culture volumes of alcohol to the culture. In other embodiments, the fermentation culture will have a viscosity ranging from about 15,000 cp to about 40,000 cp.
Turning to another aspect, the invention provides a method for making bacteria capable of hyper-producing an exopolysaccharide in slime form, comprising contacting bacteria suppressed for production of an exopolysaccharide in slime form with a mutagen, wherein the bacteria (i) contain a recombinant expression vector comprising at least one promoter operably linked to a nucleic acid molecule that encodes a polypeptide encoded by a nucleic acid molecule according to any one of claims 2 to 4, and (ii) express a polypeptide of part (i) such that exopolysaccharide production is suppressed; and identifying there from bacteria capable of hyper-producing exopolysaccharide in slime form in the presence of a polypeptide capable of suppressing exopolysaccharide production. In certain embodiments, there is provided a method for making bacteria that are capable of hyper-producing an exopolysaccharide in slime form, comprising (A) contacting (a) a mutagen with (b) bacteria that are capable of producing an exopolysaccharide in slime form, wherein the bacteria (i) contain a recombinant expression vector comprising at least one promoter operably linked to a nucleic acid molecule that encodes at least one polypeptide, wherein the nucleic acid molecule is any of the aforementioned nucleotide sequences, and (ii) express said at least one polypeptide of (i) such that exopolysaccharide production is suppressed, under conditions and for a time sufficient to produce mutagenized bacteria; and (B) identifying among said mutagenized bacteria one or a plurality of bacteria that are capable of hyper-producing exopolysaccharide in slime form. In one embodiment, the mutagen used in this method is ethylmethane sulfonate and the bacteria are Sphingomonas bacteria, such as those capable of producing an exopolysaccharide selected from gellan, welan, rhamsan, diutan, alcalan, S7, S88, S198, and NW11, including Sphingomonas strain α027.
In another aspect, the invention provides a bacterium produced by any one of the aforementioned methods, including a mutant of Sphingomonas strain α027, such as α062 (ATCC PTA-4426), α063, α065, or α069, and a mutant of xanthomonas strain α300, such as α449 (ATCC PTA-5046), α485, or α525.



BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 shows the relation between living cell number and OD600 of Sphingomonas strain α449 culture.
FIG. 2 shows α449 42 L production fermentation using SEB-022-SF+MSP medium.



DETAILED DESCRIPTION OF THE INVENTION
As described herein, the present invention provides nucleic acid molecules that encode a modulator of exopolysaccharide biosynthesis, and methods of making and using the same to identify bacteria that no longer respond to the modulator and, therefore, are capable of producing higher levels of exopolysaccharide. Use of genetic techniques to create improved exopolysaccharide producing bacteria is desired for the ease of large-scale production of biopolymers, such as sphingan polysaccharides. However, the synthesis of biopolymers is highly regulated because bacterial survival will be compromised if an unnecessary expenditure of metabolic energy synthesizing such large molecules occurs at a time, for example, when energy must be directed to growth. Moreover, the regulation of exopolysaccharide synthesis and assembly is very complex because a large number of proteins are required to create and export these macromolecules. The present invention solves these problem by identifying and using a nucleic acid sequence that encodes a negative regulator of sphingan biosynthesis to generate Sphingomonas derivatives that no longer respond to the negative regulator and that, consequently, are capable of producing higher than normal amounts of sphingan exopolysaccharide.
In the present description, any concentration range, percentage range, or integer range is to be understood to include the value of any integer within the recited range and, when appropriate, fractions thereof (such as one tenth and one hundredth of an integer), unless otherwise indicated. As used herein, “about” or “comprising essentially of” mean±15%. The use of the alternative (e.g., “or”) should be understood to mean either one, both or any combination thereof of the alternatives. When a term is provided in the singular, the inventors also contemplate the plural of that term. In addition, it should be understood that the individual compounds, or groups of compounds, derived from the various combinations of the structures and substituents described herein, are disclosed by the present application to the same extent as if each compound or group of compounds was set forth individually. Thus, selection of particular structures or particular substituents is within the scope of the present invention.
Sphingan Polysaccharides
The term “sphingan” and the phrase “sphingan exopolysaccharide,” as used herein, refer to a group of related, but distinct, polysaccharides secreted by members of the genus Sphingomonas (Pollock, J. Gen. Microbiol. 139:1939-1945, 1993). Common members of the genus Sphingomonas, and the sphingans they produce, include Sphingomonas paucimobilis (ATCC 31461, formerly Pseudomonas elodea), which produces exopolysaccharide S-60 (gellan) (see, e.g., U.S. Pat. Nos. 4,377,636; 4,326,053; 4,326,052 and 4,385,123); Sphingomonas sp. ATCC 21423, which produces exopolysaccharide S-7 (see, e.g., U.S. Pat. No. 3,960,832); Sphingomonas sp. ATCC 31554, which produces exopolysaccharide S-88 (see, e.g., U.S. Pat. Nos. 4,331,440 and 4,535,153); Sphingomonas sp. ATCC 31555, which produces exopolysaccharide S-130 (welan) (see, e.g., U.S. Pat. No. 4,342,866); Sphingomonas sp. ATCC 31961, which produces exopolysaccharide S-194 (rhamsan) (see, e.g., U.S. Pat. No. 4,401,760); Sphingomonas sp. ATCC 31853, which produces exopolysaccharide S-198 (see, e.g., U.S. Pat. No. 4,529,797); Sphingomonas sp. ATCC 53159, which produces exopolysaccharide S-657 (diutan) (see, e.g., U.S. Pat. No. 5,175,278); Sphingomonas sp. ATCC 53272, which produces exopolysaccharide NW11 (see, e.g., U.S. Pat. No. 4,874,044); Sphingomonas sp. FERM BP-2015 (previously Alcaligenes latus B-16), which produces biopolymer B-16 (alcalan) (see, e.g., U.S. Pat. No. 5,175,279); and the like.
The structures of the sphingans are all somewhat related. The main chain of each sphingan consists of a related sequence of four sugars, including D-glucose, D-glucuronic acid, L-mannose, and L-rhamnose. Polysaccharide members of the sphingan group are distinguishable from each other by virtue of the carbohydrates that form the polymer backbone, the presence or absence of acyl substituents (e.g., acetyl, glyceryl, pyruvyl, hydroxybutanoyl), and the presence or absence of side-chains. For example, sphingan polysaccharides may contain carbohydrate side-chains, and acetyl or pyruvyl groups attached to the polymer backbone carbohydrate. See, e.g., Mikolajczak et al., Appl. Env. Microbiol. 60:402, 1994. In certain embodiments, members of the sphingan exopolysaccharide family may be represented by the following general repeating chemical structure:




wherein Glc is glucose; GlcA is glucuronic acid or 2-deoxy-glucuronic acid; Rha is rhamnose; Man is mannose; X may be Rha or Man; Z is attached to Glc residue 2 and may be α-L-Rha-(1-4)-α-L-Rha, α-L-Man, or α-L-Rha; Y is attached to Glc residue 1 and may be β-D-Glc-(1-6)-α-D-Glc, β-D-Glc-(1-6)-β-D-Glc, or α-L-Rha, subscripts m and n may be independently from 0 to about 1, and wherein the “reducing end” of the polymer is toward the X residue of the backbone. In standard practice, the reducing end of an oligosaccharide or polysaccharide is placed on the right. As used herein, the term “backbone” or “main chain” refers to that portion of the structure that excludes chains Y and Z (i.e., when m and n are equal to 0). For example, the main chain of gellan (S-60) comprises the sugars D-glucose, D-glucuronic acid and L-rhamnose in a 2:1:1 molar ratio, which are linked together to form a tetrasaccharide repeat unit with the following subunit order: glucose, glucuronic acid, glucose, rhamnose. The main chain of another sphingan, diutan (S-657), differs from gellan in that it has an additional disaccharide side chain of L-rhamnose attached to glucose residue 2, which forms a hexapolysaccharide repeat unit. Still another sphingan, welan (S-130), has the same primary structure as gellan but with a side chain of a single L-mannose or a single L-rhamnose attached to glucose residue 2, which forms a pentapolysaccharide repeat unit.

Some members of the sphingan polysaccharide family are acetylated at various positions. For example, as described herein, gellan (also referred to as “gellan gum”) has the same carbohydrate backbone as welan (i.e., X=Rha), lacks a side chain sugar as welan has (i.e., m=0 and n=0), and, in contrast to welan, glucose residue 1 is fully glycerylated and partially acetylated. Gellan gum has, on average, about one glyceryl group per tetrasaccharide repeat unit and about one acetyl group per two repeat units. Another sphingan containing acyl groups is diutan (S-657), which contains acetyl groups at position 2 and/or position 6 of glucose residue 2. As is known in the art and described herein, sphingan polysaccharides may be subjected to conditions that promote deacylation in a conventional manner to remove the acyl groups. Thus, “deacylated,” as used herein, refers to a sphingan polysaccharide that lacks one or more acyl substituents, such as glyceryl and acetyl groups.
By way of background, Sphingomonas can produce a sphingan exopolysaccharide in the form of a capsule or in the form of slime. As used herein, “capsule” refers to a polysaccharide attached to the surface of a producing bacterial cell, which remains attached to the cells even after aqueous dilution, sedimentation, or centrifugation. Typically, some form of physical (e.g., heat) or chemical treatment is required to separate capsule exopolysaccharide from a bacterial cell. As used herein, “slime” refers to a polysaccharide that is not attached to the producing bacterial cell. That is, exopolysaccharide in slime form can be substantially separated from bacterial cells by, for example, centrifugation of the fermentation broth or aqueous dilution of the broth (even in the absence of heat treatment or other physical or chemical treatment). As is known in the art, slime form exopolysaccharide producing bacteria can be distinguished from those producing capsular polysaccharide by observation with a light microscope: encapsulated Sphingomonas form multicellular aggregates, while slime-forming bacteria are evenly dispersed. In addition, an encapsulated Sphingomonas can be converted into a slimy Sphingomonas by, for example, mutagenesis as described in U.S. Pat. No. 6,605,461.
The term “Sphingomonas,” as used herein, refers to a genus of gram-negative bacteria and derivative strains thereof that produce exopolysaccharides (e.g., sphingans), as described herein. The sphingan-producing family of gram-negative bacteria was first identified as belonging to the genus Sphingomonas in 1993 (see Pollock, J. Gen. Microb. 139: 1939, 1993). Sphingomonas useful in the present invention include parent Sphingomonas strains and derivatives thereof. As used herein, “parent strain” refers to bacteria or an individual bacterium before any treatment, such as chemical, biological or other types of mutagenesis, that will modify the genetic content (e.g., a substitution, insertion, or deletion within a genomic or extragenomic sequence) or phenotype of a parent strain. A person having ordinary skill in the art will understand that a mutant Sphingomonas can be a “parent strain,” such as a mutant Sphingomonas derivative that subsequent to undergoing mutation produces exopolysaccharide in slime form rather than capsule form. As used herein, the term “derivative,” when referring to a Sphingomonas species, strain, or bacterium, means any Sphingomonas species, strain, or bacterium that retains essentially the same or an enhanced capability of producing a sphingan exopolysaccharide, as described herein.
In addition, as used herein, “genetically mutated,” “genetically modified,” “mutagenized,” and “mutant” refer to the quality of having one or more spontaneous or induced mutations, and of exhibiting properties that distinguish the mutated bacterium or strain from the parent bacterium or strain. Thus, a mutant Sphingomonas species, strain, or bacterium that hyper-produces a sphingan exopolysaccharide is contemplated as a derivative of the parent Sphingomonas species, strain, or bacterium for purposes of the present invention. “Induced mutagenesis,” as used herein, means the treatment of bacterial cells with agents commonly known to induce a genetic alteration in DNA, including chemical compounds, electromagnetic radiation, ionizing radiation, and biological agents (such as viruses, plasmids, insertion elements or transposons). In one preferred embodiment, the invention provides a mutated Sphingomonas that produces exopolysaccharide in the presence of a negative regulator of exopolysaccharide biosynthesis.
The term “biosynthesis” as used herein describes the biological production or synthesis of any type of macromolecule, such as a nucleic acid, a polypeptide, or a polysaccharide (e.g., sphingans of Sphingomonas or xanthans of Xanthomonas), which may include several biosynthetic steps to arrive at an intermediate or final product. For example, sphingan exopolysaccharides are synthesized from individual carbohydrate units in a series of steps controlled by a number of enzymes (e.g., glycosyl transferases) of the bacteria. The term “biomass” refers to the exopolysaccharide plus bacterial cells in a bacterial culture.
In certain embodiments, Sphingomonas of the present invention produce exopolysaccharide in slime form. For example, Sphingomonas strains genetically mutated to synthesize and export sphingan exopolysaccharides in a slime form can be used as the “parent strain” in the context of the instant invention. Examples of Sphingomonas parent strains that are useful in the present invention include strain X287 (ATCC PTA-3487), which produces gellan gum (S-60) in a slime form; strain X530 (ATCC PTA-3486) and α252 (ATCC PTA-5128), which produce welan gum (S-130) in a slime form; strain Z473 (ATCC PTA-3485), which produces exopolysaccharide S-88 in a slime form; and strain X031 (ATCC PTA-3488), which produces exopolysaccharide S-7 in a slime form (see, e.g., U.S. Pat. Nos. 5,338,841 and 6,605,461). One advantage of a Sphingomonas strain that produces sphingan exopolysaccharide in slime form is that the fermentation broth viscosity can be significantly reduced, which should allow accumulation of increased amounts of a desired polysaccharide. However, exemplary slime form Sphingomonas strain X287 (ATCC PTA-3487) produced gellan gum at a level similar to parent strain Sphingomonas paucimobilis (ATCC 31461), while still advantageously decreasing broth viscosity. Accordingly, one aspect of the invention is the identification of a nucleic acid sequence capable of modulating the expression of polysaccharides, such as sphingans.
Sphingan Biosynthesis Modulator
Many species of bacteria synthesize and secrete acidic polysaccharides if supplied with a readily convertible carbon source, such as glucose, and an adequate amount of oxygen. Several members of the bacterial genus Sphingomonas produce a variety of acidic polysaccharides, collectively known as sphingans. Under certain environmental situations, bacteria will conserve energy by minimizing exopolysaccharide production via a negative regulatory system. The present invention is directed generally to nucleic acid sequences that encode one or more polypeptides capable of altering (e.g., increasing or decreasing in a statistically significant manner) exopolysaccharide production in Sphingomonas. This invention also pertains to methods of making bacteria capable of hyper-producing an exopolysaccharide in slime form by screening for bacteria that no longer respond to the modulator of exopolysaccharide biosynthesis. Thus, in certain preferred embodiments of the instant invention, an isolated nucleic acid molecule that encodes one or more polypeptides capable of modulating exopolysaccharide production in Sphingomonas species is used to make mutant bacteria capable of hyper-producing (i.e., producing, in a statistically significant manner, a greater quantity than the parent strain) an exopolysaccharide, for example, in slime form.
Suitable nucleic acid molecules and polypeptides capable of modulating exopolysaccharide production include, but are not limited to, naturally occurring nucleic acid molecules and polypeptides, and derivatives or analogues thereof. A “purified peptide, polypeptide, or protein” or “purified nucleic acid molecule” are sequences that are individually essentially free from contaminating cellular components, such as carbohydrate, lipid, nucleic acid (DNA or RNA), or other proteinaceous impurities associated with the nucleic acid molecule or polypeptide in nature. Preferably, the purified nucleic acids and polypeptides are sufficiently free of contaminants for use in the chemical coupling reactions of the instant invention or for other uses as needed. An “isolated peptide, polypeptide, or protein” or “isolated nucleic acid molecule” are sequences that have been removed from their original environment, such as being separated from some or all of the co-existing materials in a natural environment (e.g., a natural environment may be an unaltered cell).
Standard molecular genetic techniques can be used to identify and isolate a nucleic acid encoding a modulator of exopolysaccharide biosynthesis. As used herein, “modulator” refers to a compound (naturally or non-naturally occurring), such as a biological macromolecule (e.g., nucleic acid, protein, non-peptide or organic molecule), that typically has activity (directly or indirectly) as an inhibitor or an activator (or both) in a biological process or processes (e.g., repressor, activator, sigma factor, antimicrobial agent, antisense molecule, interference molecule, enzyme, and the like) in assays or screens described herein. “Modulation” refers to the capacity of a compound to enhance or inhibit (or both) a functional property of a biological activity or process in a statistically significant manner (e.g., gene expression, enzyme activity, or receptor binding). For example, using methods well known in the art (see, e.g., Sambrook et al., Molecular Cloning: A Laboratory Manual, 2nd edition, Cold Spring Harbor Press, Cold Spring Harbor, N.Y., 1989), a genomic expression library from Sphingomonas sp. S-88 (ATCC 31554) can be constructed, transformed into bacteria that express exopolysaccharide in capsule or slime form (e.g., Sphingomonas strain X031), preferably slime form, and screened for recombinant bacteria that no longer express exopolysaccharide.
Using such methods for the instant invention, a nucleic acid molecule (of approximately 2,600 nucleotides, SEQ ID NO:3) was identified and isolated from a Sphingomonas sp. S-88 genome, which encodes one or more polypeptides that inhibit, directly or indirectly, sphingan biosynthesis. Furthermore, a fragment of 573 nucleotides (SEQ ID NO:1) isolated from SEQ ID NO:3 was identified as sufficient to inhibit sphingan biosynthesis in Sphingomonas, including in S-7, S-88, S-130, S-194, S-198, and NW11. SEQ ID NO:1 is also capable of inhibiting xanthan biosynthesis in Xanthomonas (e.g., Xanthomonas campestris X59, ATCC 55298). In a preferred embodiment, the modulator of exopolysaccharide biosynthesis is a nucleic acid molecule that encodes a polypeptide modulator, preferably the modulator is a negative regulator of exopolysaccharide biosynthesis. That is, a host cell that expresses a nucleic acid that encodes a negative regulator of exopolysaccharide biosynthesis will result in inhibition of expression of exopolysaccharide in that host cell.
By way of background and not wishing to be bound by theory, nucleic acid sequence analysis of SEQ ID NO:3 revealed that potentially three polypeptides are encoded by this sequence, including a homologue of 3-deoxy-D-arabino-heptulosonic acid-7-phosphate synthase (DAHPS), a new polypeptide referred to as MPG, and a new polypeptide referred to as SpsN. DAHPS is involved in aromatic amino acid biosynthesis. In addition, SEQ ID NO:1 encodes SpsN, MPG and the carboxy-terminal terminal end of DAHPS. Thus, and as described in greater detail herein, one or more of MPG and SpsN can function as a modulator, directly or indirectly, of sphingan and xanthan biosynthesis. Example 3 describes how the presence of an spsN nucleic acid sequence is necessary, and potentially sufficient, to inhibit certain bacterial exopolysaccharide biosynthesis. In a preferred embodiment, the invention provides a nucleic acid molecule as set forth in SEQ ID NO:3 or SEQ ID NO:1, which encodes at least one polypeptide capable of altering exopolysaccharide production in a Sphingomonas or Xanthomonas species. Furthermore, the instant invention should be understood to also pertain to a nucleic acid molecule as set forth in SEQ ID NO:3 or SEQ ID NO:1 that itself functions as a modulator or encodes another nucleic acid that functions as a modulator. Thus, in another preferred embodiment, there is provided a nucleic acid molecule as set forth in SEQ ID NO:3 or SEQ ID NO:1 that is capable of altering exopolysaccharide production in a Sphingomonas or Xanthomonas species.
While particular embodiments of isolated nucleic acids encoding a modulator of exopolysaccharide biosynthesis are depicted in SEQ ID NOS:3 and 1, within the context of the present invention, reference to one or more isolated nucleic acids includes variants of these sequences that are substantially similar in that they encode native or non-native proteins, polypeptides or peptides with similar structure and function to a modulator of exopolysaccharide biosynthesis, such as SEQ ID NO:4 or SEQ ID NO:2. As used herein, the nucleotide sequence is deemed to be “substantially similar” if: (a) the nucleotide sequence is derived from the coding region of SEQ ID NO:3 or 1 isolated from a Sphingomonas or Xanthomonas (including, for example, portions of the sequence or allelic variations of the sequences discussed above) and is capable of altering exopolysaccharide biosynthesis; (b) the nucleotide sequence is capable of hybridization to the nucleotide sequences of the present invention under moderate or high stringency; (c) the nucleotide sequences are degenerate (i.e., sequences which code for the same amino acids using a different codon sequences) as a result of the “wobble” in the genetic code for the nucleotide sequences defined in (a) or (b); or (d) is a complement of any of the sequences described in (a), (b) or (c). Polynucleotide variants may contain one or more substitutions, additions, deletions, and/or insertions such that the activity of the encoded polypeptide, preferably, is not substantially diminished, as described herein.
In one embodiment, preferred is an isolated nucleic acid molecule comprising a sequence that remains hybridized under highly stringent conditions to a probe, wherein the probe consists of SEQ ID NO:1 or a complement of SEQ ID NO:1. In a preferred embodiment, the present invention provides an isolated nucleic acid molecule that consists of SEQ ID NO:1 or a complement of SEQ ID NO:1. Certain isolated nucleic acids of the inventions are, therefore, useful for detecting the presence of a nucleic acid that encodes a modulator of exopolysaccharide biosynthesis or an analogue, homologue, or derivative thereof, or are useful for expressing a polypeptide capable of altering exopolysaccharide biosynthesis. As used herein, “nucleic acid molecule” or “polynucleotide” refers to a polymeric form of nucleotides of a least ten bases in length, either ribonucleotides or deoxynucleotides or a modified from of either type of nucleotide. The term includes single and double stranded forms of DNA or RNA or any of a number of known natural and non-natural chemical variants of nucleic acids, for instance, nucleic acids having greater resistance to degradation, such as those containing phosphorothioates. In certain embodiments, the nucleic acid molecules that encode a modulator of exopolysaccharide biosynthesis are DNA or RNA.
“Moderately stringent hybridization conditions” and “highly stringent hybridization conditions” are conditions of hybridization of a probe nucleotide sequence to a target nucleotide sequence according to established principles of nucleotide base-pairing and hydrogen bond formation wherein hybridization will only be readily detectable when a portion of the target sequence is substantially similar to the complement of the probe sequence. Hybridization conditions vary with probe size as well as with temperature, time, and salt concentration in a manner known to those having ordinary skill in the art. For example, moderate hybridization conditions for a 50 nucleotide probe would include hybridization overnight in a buffer containing 5×SSPE (1×SSPE=180 mM sodium chloride, 10 mM sodium phosphate, 1 mM EDTA (pH 7.7), 5×Denhardt's solution (100×Denhardt's=2% (w/v) bovine serum albumin, 2% (w/v) Ficoll, 2% (w/v) polyvinylpyrrolidone) and 0.5% SDS incubated overnight at 55-60° C. Post-hybridization washes at moderate stringency are typically performed in 0.5×SSC (1×SSC=150 mM sodium chloride, 15 mM trisodium citrate) or in 0.5×SSPE at 55-60° C. Highly stringent hybridization conditions typically would include 2×SSPE overnight at 42° C., in the presence of 50% formamide, followed by one or more washes in about 0.1×SSC to about 0.2×SSC, and 0.1% SDS at 65° C. for 30 minutes or more.
The isolated nucleic acids encoding a modulator of exopolysaccharide biosynthesis according to this invention can be obtained using a variety of methods. For example, as described above, a nucleic acid molecule may be obtained from a cDNA or genomic expression library by screening with an antibody or antibodies reactive with an SpsN or MPG polypeptide (see, e.g., Sambrook et al., Molecular Cloning: A Laboratory Manual, Cold Spring Harbor, 1989; Ausubel et al., Current Protocols in Molecular Biology, Greene Publishing, 1987). Further, random-primed PCR can be employed (see, e.g., Methods in Enzymol. 254:275, 1995). In addition, variations of random-primed PCR can also be used, especially when a particular gene or gene family is desired. In one such method, one of the primers is a random primer and the other is a degenerate primer based on the amino acid sequence or nucleotide sequence encoding a modulator of exopolysaccharide biosynthesis.
Other methods may also be used to obtain isolated nucleic acid molecules that encode a modulator of exopolysaccharide biosynthesis. For example, a nucleic acid molecule can be isolated by using the sequence information provided herein to synthesize a probe that can be labeled, such as with a radioactive label, enzymatic label, protein label, fluorescent label, or the like, and hybridized to a genomic library or a cDNA library constructed in, for example, a phage, plasmid, phagemid, or viral vector designed for replication or expression in one or more selected host cells (see, e.g., Sambrook et al., supra; Ausubel et al., supra). DNA representing RNA or genomic nucleic acid sequence can also be obtained by amplification using sets of primers complementary to 5′ and 3′ sequences of the isolated nucleic acid sequences provided in SEQ ID NOS:1 and 3, or to variants thereof, as described above. For ease of cloning, restriction enzyme sites can also be incorporated into the primers. Thus, the present invention includes nucleic acid molecules that are useful as primers for use in PCR amplification procedures specific for the amplification of at least one mRNA or DNA encoding a modulator of exopolysaccharide biosynthesis, particularly in samples derived from Sphingomonas or Xanthomonas (for PCR procedures see, e.g., U.S. Pat. No. 4,683,195; U.S. Pat. No. 4,965,188; and Innis et al., PCR Strategies, Academic Press, San Diego, 1995). Such PCR amplification methods are known in the art and include primer extension PCR, real time PCR, reverse transcriptase PCR (Freeman et al., BioTechniques 26:112, 1999), inverse PCR (Triglia et al., Nucleic Acids Res. 16:8186, 1988), capture PCR (Lagerstrom et al., PCR Methods Applic. 1:111, 1991), differential primer extensions (WO 96/30545), and other PCR amplification methods known in the art or later developed (see, e.g., Innis et al., PCR Strategies, Academic Press, San Diego. 1995).
In operation, PCR methods generally include the use of primer molecules that are chemically synthesized, but they may be generated enzymatically or produced recombinantly. PCR primers generally comprise two nucleotide sequences, one with sense orientation (5′->3′) and one with antisense orientation (3′->5′), employed under preferred conditions for identification of a specific gene or condition. The same PCR primers, nested sets of oligomers or a degenerate pool of oligomers can be employed under less stringent conditions for detection and/or quantitation of closely related DNA or RNA sequences. These nucleic acid molecules can also be used individually or in combination as probes to identify contactin mRNA or DNA molecules in a sample. These nucleic acid molecules include:








5′-GACGGATCCTTGCCGAGGTGCG-3′,
(SEQ ID NO: 5)


 


5′-CGACGGCCACTACTAGCGTTCGAACG-3′,
(SEQ ID NO: 6)


 


5′-GTCCGTCGGTATCTACGGCTTCGAACG-3′,
(SEQ ID NO: 7)






SEQ ID NO: 5 is a forward primer, while SEQ ID NO:6 and SEQ ID NO:7 are reverse primers.

The nucleic acid molecules of the present invention can be made by a variety of methods known in the art. For example, nucleic acid molecules can be made using synthetic procedures or molecular biology techniques known in the art (see, e.g., Sambrook et al., supra). The length of the nucleic acid molecules of the present invention can be readily chosen by one skilled in the art depending on the particular purpose that the nucleic acid molecule is to be used for. For PCR primers, the length of the nucleic acid molecule is preferably between about 10 nucleotides and about 50 nucleotides in length, more preferably between about 12 nucleotides and about 30 nucleotides in length, and most preferably between about 15 nucleotides and about 25 nucleotides in length. For probes, the length of the nucleic acid molecule is preferably between about 20 nucleotides and about 1,000 nucleotides in length, more preferably between about 100 nucleotides in length and about 500 nucleotides in length, and most preferably between about 150 nucleotides and about 400 nucleotides in length.
Variants (including alleles) of the isolated SEQ ID NOS:1 and 3 nucleic acid sequences provided herein can be readily obtained from natural variants (e.g., polymorphisms, mutants and other serotypes) either synthesized or constructed. Many methods have been developed for generating mutants (see, generally, Sambrook et al., supra; Ausubel et al., supra). Briefly, preferred methods for generating nucleotide substitutions utilize an oligonucleotide that spans the base or bases to be mutated and contains the mutated base or bases. The oligonucleotide is hybridized to complementary single stranded nucleic acid and second strand synthesis is primed from the oligonucleotide. The double-stranded nucleic acid is prepared for transformation into host cells, such as E. coli or other prokaryotes, and yeast or other eukaryotes. Standard screening and vector amplification protocols are used to identify mutant sequences and obtain high yields.
Similarly, deletions or insertions of a nucleic acid molecule that encodes a modulator of exopolysaccharide biosynthesis may be constructed by any of a variety of known methods. For example, the sequence may be digested with restriction enzymes or nucleases and be religated such that sequences are deleted, added, or substituted. Similarly, a variety of transposons and other insertional elements may be used to make recombinants having deletions and insertions. Thus, in one example, an spsN mutant containing a Tn10Kan transposon in the spsN coding sequence, as described herein, can be made according to methodologies known in the art. Other means of generating variant sequences, also known in the art, may be employed without requiring undue experimentation (for examples see Sambrook et al., supra, and Ausubel et al., supra). Moreover, verification of variant sequences is typically accomplished by restriction enzyme mapping, sequence analysis, hybridization, and the like. Variants that encode a modulator of exopolysaccharide biosynthesis that are capable of altering exopolysaccharide biosynthesis are particularly useful in the context of this invention.
A person having ordinary skill in the art would appreciate that other spsN encoding sequences can be identified and isolated in a similar manner. For example, analogues or derivatives thereof of spsN, or spsN homologues from other species of Sphingomonas or other related bacteria (such as Xanthomonas or Pseudomonas) can be identified and isolated using assays described herein. Thus, in certain embodiments, preferred modulators of exopolysaccharide biosynthesis in Sphingomonas or Xanthomonas comprise a nucleic acid sequence as set forth in SEQ ID NO:3 or SEQ ID NO:1, and analogues or derivatives thereof of SEQ ID NO:3 or SEQ ID NO:1 that are capable of altering exopolysaccharide biosynthesis. As used herein, the terms “derivative” and “analogue” when referring to a modulator of exopolysaccharide biosynthesis, refer to any modulator of exopolysaccharide biosynthesis that retains essentially the same (at least 50%, and preferably greater than 70%, 80%, 90%, or 95%) or enhanced biological function or activity as such parent modulator, as noted above. The biological function or activity of such analogues and derivatives can be determined using standard methods (e.g., plate assay, gel analysis, transcription assay, translation assay), such as with the assays described herein and known in the art. For example, an analogue or derivative may be a proprotein that can be activated by cleavage, or may be a precursor that can be activated or stabilized by an amino acid modification, to produce an active modulator of exopolysaccharide biosynthesis. Alternatively, a modulator of exopolysaccharide biosynthesis and analogues or derivatives thereof can be identified by their ability to specifically bind to one or more anti-modulator antibodies.
Another example of an analogue or derivative includes a modulator of exopolysaccharide biosynthesis (e.g., SpsN) that has one or more conservative amino acid substitutions, as compared with the amino acid sequence of a naturally occurring modulator. Among the common amino acids, a “conservative amino acid substitution” is illustrated, for example, 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) serine and threonine, (4) aspartate and glutamate, (5) glutamine and asparagine, and (6) lysine, arginine and histidine, or a combination thereof. Furthermore, an analogue or derivative of a modulator may include, for example, non-protein amino acids, such as precursors of normal amino acids (e.g., homoserine and diaminopimelate), intermediates in catabolic pathways (e.g., pipecolic acid and D-enantiomers of normal amino acids), and amino acid analogues (e.g., azetidine-2-carboxylic acid, homoproline, and canavanine).
Yet other embodiments of analogues or derivatives include a modulator of exopolysaccharide biosynthesis that retains at least about 60% identity with the parent molecule (i.e., the “parent” molecule will depend on the starting point, whether the parent is, for example, wild-type SpsN or an analogue of SpsN), more preferably at least about 70%, 80%, 90%, and most preferably at least about 95%. As used herein, “percent identity” or “% identity” is the percentage value returned by comparing the whole of the subject polypeptide, peptide, or analogue or variant thereof sequence to a test sequence using a computer implemented algorithm, typically with default parameters. Sequence comparisons can be performed using any standard software program, such as those provided in the Lasergene® bioinformatics computing suite, which is produced by DNASTAR® (Madison, Wis.). References for algorithms, such as BLAST® or ALIGN, may be found in, for example, Altschul, J. Mol. Biol. 219:555-565, 1991; or Henikoff and Henikoff, Proc. Natl. Acad. Sci. USA 89:10915-10919, 1992; and preferably BLAST® is used (as used herein, BLAST® refers to one or more of the following search algorithms: BLASTn, MEGABLAST, BLASTp, PSI-BLAST, PHI-BLAST, BLASTx, tBLASTn, tBLASTx, RPS-BLAST, CDART, VecScreen, trace BLAST, and the like), which is available at the National Center for Biotechnology Information (NCBI, Bethesda, Md.) website (www.ncbi.nlm.nih.gov/BLAST) and results compared to databases, such as GenBank®. Other methods for comparing multiple nucleotide or amino acid sequences by determining optimal alignment are well known to those of skill in the art (see, e.g., Peruski and Peruski, The Internet and the New Biology: Tools for Genomic and Molecular Research (ASM Press, Inc. 1997); Wu et al. (eds.), “Information Superhighway and Computer Databases of Nucleic Acids and Proteins,” in Methods in Gene Biotechnology, pages 123-151 (CRC Press, Inc. 1997); and Bishop (ed.), Guide to Human Genome Computing, 2nd Edition, Academic Press, Inc., 1998).
As used herein, “similarity” between two or more peptides or polypeptides is generally determined by comparing the amino acid sequence of one peptide or polypeptide with one or more other peptides or polypeptides having conserved amino acid substitutions thereto. Further, as is known in the art, a consensus sequence may be determined for a group of homologues, analogues, or derivatives based on the amino acid sequence of a parent compound, such as MPG (SEQ ID NO:4) or SpsN (SEQ ID NO:2). In a preferred embodiment, the polypeptide modulator comprises the amino acid sequence of SEQ ID NO:2, and in an even more preferred embodiment the modulator consists of the amino acid sequence of SEQ ID NO:2.
An analogue or derivative may also be a fusion protein of a modulator of exopolysaccharide biosynthesis. Fusion proteins, or chimeras, include fusions of one or more modulators of exopolysaccharide biosynthesis with non-modulator peptides or polypeptides, such as a polypeptide tag (e.g., an epitope tag or 6× His tag), carrier, or enzyme. The peptides may also have a detectable label or “tag” (i.e., be labeled), such as with a radioactive label, a fluorescent label, a mass spectrometry tag, biotin, and the like.
Peptides may be produced by recombinant techniques and a variety of host systems are suitable for production of modulators of exopolysaccharide biosynthesis and analogues or derivatives thereof, including bacteria (e.g., E. coli), yeast (e.g., Saccharomyces cerevisiae), insect (e.g., Sf9), and mammalian cells (e.g., CHO, COS-7). Many expression vectors have been developed and are available for each of these hosts. In a preferred embodiment, vectors that are functional (i.e., capable of replicating) in bacteria are used in this invention, even more preferably the vectors are broad host range plasmids, such as pRK311 (Ditta et al., Plasmid 13:149, 1985) and pMMB(EH) (Fürste et al., Gene 48:119, 1986). However, at times, it may be preferable to have vectors that are functional in other hosts or more than one host. Vectors and procedures for cloning and expression in E. coli are discussed herein and, for example, in Sambrook et al. (1987) and in Ausubel et al. (1995).
“Vector” refers to a nucleic acid assembly that is capable of directing the expression of a desired polypeptide. The vector may include an expression control sequence (e.g., transcriptional promoter/enhancer elements) that is operably linked to the nucleic acid coding sequence or isolated nucleic acid molecule(s) of interest. The vector may be composed of DNA, RNA, or a combination of the two (e.g., a DNA-RNA chimera). Optionally, the vector may include a polyadenylation sequence, one or more restriction sites, as well as one or more selectable markers, such as neomycin phosphotransferase or hygromycin phosphotransferase, as needed. Additionally, depending on the host cell chosen and the vector employed, other genetic elements such as an origin of replication, additional nucleic acid restriction sites, enhancers, sequences conferring inducibility or repressibility of transcription, and selectable markers, may also be incorporated into the vectors described herein.
“Cloning vector” refers to nucleic acid molecules, such as a plasmid, cosmid, or bacteriophage, which are capable of replicating autonomously in a host cell. Cloning vectors typically contain one or a small number of restriction endonuclease recognition sites, at which foreign nucleotide sequences can be inserted in a determinable fashion without loss of an essential biological function of the vector. Cloning vectors also typically contain a marker gene (e.g., antibiotic resistance encoding gene) that is suitable for use in the identification and selection of cells transformed with the cloning vector. Marker genes typically encode proteins that provide resistance to antibiotics, such as tetracycline, kanamycin, ampicillin, and the like.
As used herein, “nucleic acid expression construct” refers to a nucleic acid molecule construct containing a nucleic acid sequence that is expressed in a host cell. Typically, expression of a nucleic acid sequence of interest is placed under the control of an expression control sequence (e.g., promoter), and optionally, under the control of at least one regulatory element. Such an expressed sequence is said to be “operably linked to” the promoter. Similarly, a regulatory element and a promoter are operably linked if the regulatory element alters (i.e., increases or decreases with statistical significance) the activity of the promoter. As used herein, “expression control sequence” refers to a nucleotide sequence that directs the transcription of a structural gene. Typically, an expression control sequence is located in the 5′ region of a gene, proximal to the transcriptional start site of a structural gene. If an expression control sequence is an inducible promoter, then the rate of transcription may, for example, be increased by the addition of an inducing agent or decreased by the addition of an inhibiting agent. In contrast, an inducing or an inhibiting agent does not affect the rate of transcription of a constitutive promoter.
A person having ordinary skill in the art is capable of selecting a suitable expression control sequence and suitable host for expressing, for example, an isolated nucleic acid sequence encoding a peptide having the amino acid sequence of SEQ ID NO:4 or variants thereof, wherein the variants comprise amino acid sequences having conservative amino acid substitutions or having at least 80% sequence identity to SEQ ID NO:4, and wherein the variants are capable of altering exopolysaccharide biosynthesis. In a preferred embodiment, there is provided a recombinant expression vector comprising at least one promoter operably linked to a nucleic acid molecule as set forth in SEQ ID NO:1 or 3, or a variant thereof, that encodes at least one polypeptide capable of altering exopolysaccharide biosynthesis in Sphingomonas. 
A DNA sequence encoding a modulator of exopolysaccharide biosynthesis may be introduced into an expression vector appropriate for a particular host. In certain embodiments, the nucleic acid sequence may be cloned into a vector or expression vector to generate a fusion protein. The fusion partner may be chosen to be a polypeptide tag, such that isolation of a fusion protein is facilitated. The fusion carrier may prevent modulator degradation by host proteases, or the fusion partner may further function to transport the fusion peptide to inclusion bodies, the periplasm, the outer membrane, or the extracellular environment. Thus, the instant invention contemplates a recombinant expression vector comprising at least one promoter operably linked to a nucleic acid molecule as set forth in SEQ ID NO:1 or 3 or a variant thereof that encodes at least one polypeptide, which is expressed as a fusion protein capable of altering exopolysaccharide biosynthesis in Sphingomonas. Typically, the protein portion fused to a modulator of exopolysaccharide biosynthesis will be encoded by a second nucleic acid sequence; preferably the second nucleic acid sequence encodes a polypeptide tag or an enzyme, as described herein and is known in the art. In certain embodiments, the expression vector promoter will preferably be regulated and, in certain circumstances, the vector will preferably be a plasmid that replicates in Sphingomonas, Pseudomonas, or Xanthomonas. In a preferred embodiment, the plasmid is pRK311 containing SEQ ID NO:1 (X029, ATCC PTA-5127) or SEQ ID NO:3.
As used herein, “host cell” refers to any prokaryotic or eukaryotic cell that contains either a cloning vector or a nucleic acid expression construct. This term also includes those prokaryotic or eukaryotic cells that have been recombinantly engineered to contain cloned nucleic acid sequence(s) in the chromosome or genome of the host cell. Preferably, a host cell is a prokaryotic cell, more preferably a bacterium, and even more preferably a Sphingomonas, Xanthomonas, or Pseudomonas. Sphingomonas being most preferred. In certain preferred embodiments, the host cell is a sphingan producing bacterium, such as Sphingomonas sp. that produce gellan, welan, rhamsan, diutan, alcalan, S-7, S-88, S-198, and NW11. In one embodiment, the present invention provides a host cell Sphingomonas, such as α027, containing plasmid X029 (ATCC PTA-5127). In another embodiment, the host cell is Xanthomonas. 
Enhanced Exopolysaccharide Biosynthesis
According to another aspect of the present invention there are provided methods for identifying and isolating bacteria that are capable of over-producing exopolysaccharide. In particular, a modulator of exopolysaccharide biosynthesis can be used to identify exopolysaccharide-producing bacteria that no longer respond to the modulator of exopolysaccharide biosynthesis. For example, colonies of bacteria that produce exopolysaccharide will have a mucoid appearance on agar plates, while non-producers will have a non-mucoid appearance. Introduction of a recombinant expression vector that encodes a modulator of exopolysaccharide biosynthesis into an exopolysaccharide producing bacterium will suppress exopolysaccharide expression, which means the bacteria will have a non-mucoid appearance on agar plates. These suppressed strains can be screened for spontaneous mutants or induced mutants that are capable of expressing exopolysaccharide even in the presence of a modulator of exopolysaccharide biosynthesis.
Within certain embodiments, there is provided a method for making bacteria capable of hyper-producing an exopolysaccharide in slime form, comprising contacting bacteria suppressed for production of an exopolysaccharide in slime form with a mutagen, wherein the bacteria (i) contain a recombinant expression vector comprising at least one promoter operably linked to a nucleic acid molecule that encodes at least one polypeptide capable of altering exopolysaccharide production, and (ii) express a polypeptide of part (i) such that exopolysaccharide production is suppressed; and then identifying therefrom bacteria capable of hyper-producing exopolysaccharide in slime form in the presence of a polypeptide capable of suppressing exopolysaccharide production.
The term “hyper-producing” refers to the capability of a first bacterial strain that produce statistically significantly more exopolysaccharide than a second strain from which the first bacterial strain was directly or indirectly derived. A first bacterial strain is “directly derived” from a second bacterial strain if the first strain was obtained from a single cycle of mutagenesis and/or selection of the second strain. A first bacterial strain is “indirectly derived” from a second bacterial strain if the first strain was obtained from multiple cycles of mutagenesis and/or selection of the second strain.
In one preferred embodiment, there is provided a method for making bacteria that are capable of hyper-producing an exopolysaccharide in slime form, comprising (A) contacting (a) a mutagen with (b) bacteria that are capable of producing an exopolysaccharide in slime form, wherein the bacteria (i) contain a recombinant expression vector comprising at least one promoter operably linked to a nucleic acid molecule that encodes at least one polypeptide, wherein the nucleic acid molecule encodes at least one polypeptide capable of altering exopolysaccharide production, and (ii) express said at least one polypeptide of (i) such that exopolysaccharide production is suppressed, under conditions and for a time sufficient to produce mutagenized bacteria; and (B) identifying among said mutagenized bacteria one or a plurality of bacteria that are capable of hyper-producing exopolysaccharide in slime form. In certain preferred embodiments, the bacteria are Sphingomonas, such as S-60, S-7, S130, S-7, S-194, S-198, and NW11, and the mutagen is, for example, ethylmethane sulfonate (EMS), N-methyl-N′-nitro-N-nitrosoguanidine (MNNG) or another suitable mutagen as known in the art. In another preferred embodiment, the modulator of exopolysaccharide biosynthesis is encoded by SEQ ID NO:1 or 3, and preferably by a nucleic acid molecule comprising a sequence that encodes the amino acid sequence of SEQ ID NO:2 or 4. In one particularly preferred embodiment, the parent bacterium is Sphingomonas α027, and the mutant of α027 that no longer responds to a modulator of exopolysaccharide biosynthesis is Sphingomonas α062 (ATCC PTA-4426) (for more details, see Examples). In another embodiment, the parent bacterium is Xanthomonas campestris X59, and the mutant of X59 that no longer responds to a modulator of exopolysaccharide biosynthesis is Xanthomonas campestris α449 (ATCC PTA-5064). Preferably, the mutant strain produces (in a statistically significant manner) more exopolysaccharide than the parent strain, such as at least about 10% to about 20% more, preferably at least about 20% to about 30% more, and more preferably at least about 30% to about 40% more.
Production of Exopolysaccharides
Another aspect of the present invention relates to the enhanced production of exopolysaccharide. For example, to produce sphingan exopolysaccharide, genetically mutated Sphingomonas bacteria are cultured under suitable fermentation conditions, which are well known in the art and which are generally described in U.S. Pat. No. 5,854,034. Briefly, a suitable medium for culturing the genetically mutated Sphingomonas is an aqueous medium that generally contains a source of carbon such as, for example, carbohydrates including glucose, lactose, sucrose, maltose or maltodextrins; a nitrogen source such as, for example, inorganic ammonium, inorganic nitrate, organic amino acids or proteinaceous materials such as hydrolyzed yeast, soy flour or casein; distiller's solubles or corn steep liquor; inorganic salts and vitamins. A wide variety of fermentation media will support the bacterial production of sphingans according to the present invention. The carbohydrates are included in the fermentation broth in varying amounts, but usually between about 1% and about 5% by weight of the fermentation medium. The carbohydrates may be added all at once prior to fermentation or alternatively, during fermentation. The amount of nitrogen may range from about 0.01% to about 0.2% by weight of the aqueous medium. A single carbon source or nitrogen source may be used, as well as mixtures of these sources. Among the inorganic salts which find use in fermenting Sphingomonas are salts that contain sodium, potassium, ammonium, nitrate, calcium, phosphate, sulfate, chloride, carbonate and similar ions. Trace metals, such as magnesium, manganese, cobalt, iron, zinc, copper, molybdenum, iodide and borate, may also be advantageously included. Vitamins, such as biotin, folate, lipoate, niacinamide, pantothenate, pyridoxine, riboflavin, thiamin and vitamin B.sub.12 and mixtures thereof, may also be advantageously employed.
Generally, the fermentation can be carried out at temperatures between (and including) about 25° C. and 35° C., with optimum productivity obtained within a temperature range of about (and including) 28° C. to 32° C. The inoculum is prepared by standard methods of volume scale-up, including shaken flask cultures and small-scale submerged stirred fermentation. The medium for preparing the inoculum can be the same as the production medium or can be any one of several standard media well-known in the art, such as Luria broth or YM medium. The concentration of carbohydrate can be reduced in the seed cultures to less than about 1% by weight. More than one seed stage may be used to obtain the desired volume for inoculation. Typical inoculation volumes range from about 0.5% to about 10% of the total final fermentation volume. The fermentation vessel typically contains an agitator to stir the contents. The vessel may also have automatic pH and foaming controls. The production medium is added to the vessel and sterilized in place by heating. Alternatively, the carbohydrate or carbon source may be sterilized separately before addition. A previously grown seed culture is added to the cooled medium (generally, at the fermentation temperature of about 28° C. to about 32° C.) and the stirred culture is fermented for about 48 hours to about 96 hours, producing a broth having a viscosity of from about 15,000 centipoise (cp) to about 20,000 cp, and from about 10 to about 15 g/L sphingan exopolysaccharide in slime form. The fermentation of a corresponding parent Sphingomonas strain will typically provide a broth having a viscosity of from about 25,000 cp to about 50,000 cp.
In this aspect, the invention provides an exopolysaccharide in slime form obtained from Sphingomonas or Xanthomonas grown in submerged, stirred and aerated liquid culture. The concentration of dissolved oxygen in the liquid culture preferably exceeds about 5% of saturation of water after 24 hours of culturing. Similar fermentations with encapsulated strains resulted in 0% dissolved oxygen after 24 hours. The lower viscosity provided by the exopolysaccharide in slime form results in improved aeration which allows Sphingomonas to be productive in culture for a longer period of time. In another aspect of the present invention, fermentation may be carried out in a semi-batch process where bacteria from one fermentation are used as an inoculum for a subsequent fermentation. In this aspect, for example, Sphingomonas that have been separated from the exopolysaccharide which they produced may be added to a fresh fermentation broth, or a fresh fermentation broth may be added to the remaining Sphingomonas. Hence, this aspect of the invention precludes the need to provide a separate seed culture.
Recovery of exopolysaccharides, regardless of the conditions used to produce them, preferably involves a precipitation step. The precipitated exopolysaccharide may then recovered by centrifugation. A typical method for recovering gellan and welan gums is a follows. Immediately after fermentation, the culture broths are heated to at least 90° C. to kill the living bacteria. The exopolysaccharides are then separated from the culture broth by precipitation with approximately 2 volumes (i.e., culture volume equivalents) of isopropyl alcohol, and the precipitated polysaccharide fibers are collected, pressed, dried, and milled. The alcohol is removed by distillation. In this most simple process, the polysaccharide remains attached to the cells, such that when the dried and milled polysaccharide is resuspended in water, the solution is not transparent. In the case of gellan gum, additional steps can be introduced to purify the polysaccharide away from the bacterial cells so that the resuspended product is more transparent. Before the alcohol precipitation, the culture broth is centrifuged and/or filtered or both while the temperature is maintained above the critical transition temperature between a highly viscous state and a liquefied state that is amenable to centrifugation or filtration. These processes for different sphingans are disclosed in, for example, U.S. Pat. No. 4,326,052 (gellan); U.S. Pat. No. 4,326,053 (gellan); U.S. Pat. No. 4,342,866 (welan); U.S. Pat. No. 3,960,832 (S-7); and U.S. Pat. No. 4,535,153 (S-88).
In certain embodiments, the present invention provides a method for hyper-producing exopolysaccharide, comprising culturing bacteria under conditions and for a time sufficient to permit exopolysaccharide production, wherein the bacteria hyper-produce exopolysaccharide in slime form when expressing at least one polypeptide encoded by a nucleic acid molecule that is capable of altering exopolysaccharide production; and separating the exopolysaccharide in slime form from the culture. Preferably, the bacteria are Sphingomonas, such as those that produce gellan, welan, rhamsan, diutan, alcalan, S7, S88, S198, or NW11, more preferably Sphingomonas strains α062 (ATCC PTA-4426), α063, α065 and α069. In a preferred embodiment, the culturing is by fermentation and the bacteria produce from about 5 grams to about 80 grams of exopolysaccharide per liter of culture, more preferably from about 10 grams to about 70 grams, and even more preferably from about 20 grams to about 60 grams. Optimal conditions for the fermentation is from about 48 hours to about 96 hours at a temperature ranging from about 25° C. to about 35° C. Preferably, the exopolysaccharide is separated by alcohol precipitation, wherein about 1 to about 1.5 volumes of alcohol is preferably added to the culture. Preferably, the fermentation culture has a final viscosity ranging from about 5,000 cp to about 40,000 cp, more preferably from about 10,000 cp to about 35,000 cp, and most preferably from about 15,000 cp to about 30,000 cp.
All of the above U.S. patents, U.S. patent application publications, U.S. patent applications, foreign patents, foreign patent applications and non-patent publications referred to in this specification and/or listed in the Application Data Sheet, are incorporated herein by reference, as if set forth herein, in their entirety.
EXAMPLES
Example 1
Preparation of White, High Glucose Resistant Sphingomonas 
Sphingomonas X287 (ATCC PTA-3487) was used to inoculate 50 ml 1⁄4YM−, having either 1% or 5% glucose in 125 ml baffled flask at 30° C. for two weeks without shaking. No exopolysaccharide-negative mutants appeared when the culture was spread onto a 1⁄4YM+ plate after such an extended incubation. The same culture was spread onto a plate of 1⁄4YM having 10% Glucose. Isolated colonies (83) were selected and used to inoculate 2 ml 1⁄4YM having 3% Glucose, and then incubated for 40 hrs at 30° C. with shaking at 300 rpm. These cultures were spread on high glucose plates, and 12 colonies chosen and saved as X729-X741. Six out of those twelve mutants were visually white mutants.
Colonies were used to inoculate 2 ml YM− in small tubes and shaken at 300 rpm for 24 hrs at 30° C. (referred to as seed-1). Then 100 μl of these cultures were used to inoculate 5 ml B10G3, which culture was placed at an angle and incubated at 300 rpm for 24 hrs (referred to as seed-2). Then 5 ml of seed-2 was added to 20 ml B10G3 into 125 ml baffled flask and incubated with shaking at 200 rpm during the first 17 hrs, and then 400 rpm up to 46 hrs. 10 g of the final broth was precipitated by 20 volumes isopropyl alcohol (IPA) at room temperature. The sample was dried at 60° C. under vacuum for 2 hrs.
High Glucose Resistant, White Mutants

















DW (g/L)



Final pH
OD600
(Ave = 14.9 g/L)





















X733white
5.82
17.7
15.1



X734white
5.77
17.9
15.5



X735white
5.78
17.5
15.3



X736white
5.84
16.1
14.7



X737white
5.55
12.5
13.6



X738white
4.31
6.0
3.6



X743white
5.78
17.0
15.3



X753
5.82
14.1
13.0










Parent Gellan Slime


















DW (g/L)



Final pH
OD600
(Ave = 12.7 g/L)





















X287-1
5.82
14.5
12.6



X287-2
5.78
14.2
12.8



X287-3
5.77
13.6
12.5



X287-4
5.78
14.2
12.8










The strain X733 inoculated in 125 ml baffled flask and incubated for 48 hrs. The culture broth spread on 1⁄4YM+ plate generated slimy-capsule form colonies and a few yellow color colonies. Color indicator shows a hint to predict the mutation stability in some extent. One of the white slimy colonies was selected and saved as X996.
The X996 was cultivated in 100 ml B10 containing 3% and 6% Glucose using 500 ml baffled flask at 160 rpm for 24 hrs with 0.1% inoculation.













24 hrs pH/OD600/Living cell number



















B10 3% Glucose
6.30/9.95/2.4 × 1010



B10 6% Glucose
6.32/7.88/1.7 × 1010










It was hard to cultivate this X996 mutant reproducibly when the inoculation rate was low. This mutant did not grow well when it incubated under high rate of agitation.
This X996 was incubated for 30 hrs in 30 ml B10 medium supplemented by 7% Glucose using 125 ml baffled flask.
Low rate of inoculation suppressed the X996 cell growth. This culture medium saved at room temperature for a week without shaking. Then the culture was spread onto 1⁄4YM 10% glucose plate. The Sphingomonas α016-α018 were isolated on high glucose containing 1⁄4YM plates.
Example 2
Identification of Sphingomonas No Longer Responsive to SpsN
This example describes identification of a DNA sequence that suppresses biosynthesis of sphingan and xanthan by the following steps: (1) making an expression library of Sphingomonas S-88 genomic DNA; (2) transforming the expression library into Sphingomonas S-7; and (3) screening for suppression of exopolysaccharide S-7 production in Sphingomonas S-7 (i.e., spread bacterial cultures on plates and observe colonies for non-mucoid appearance). Primers SEQ ID NO:5 (22mer), and SEQ ID NOS:6 and 7 (26 and 27mer, respectively) were made and used with template Z964 (pBluescriptKS-BH, 716 bp, which is a fragment from Z939 (pRK311-s88nc2, 2.7 Kb)) to produce a 573 base pair fragment (SEQ ID NO:1) encoding, inter alia, functional spsN. The 573 base pair PCR fragment (SEQ ID NO:1) was cloned into plasmid pRK311, and two independent clones (X026 and X029) were further tested as follows:












Strain















Plasmid
S-7
S-88
NW11
S-130
S-194
S-198
NW11
X59





X025
+
+
+
+
+
+
+
+


X026
−
−
−
−
−
−
−
−


X028
+
+
+
+
+
+
+
+


X029
−
−
−
−
−
−
−
−


Z959-1
+
+
+
+
+
+
+
+


Z959-2
+
+
+
+
+
+
+
+


Z959-3
+
+
+
+
+
+
+
+


Z967
−
−

−
−
−
−
−


Z939
−
−
−
−
−
−
−
−





X025 = pRK311-MPG (385 bp, 22 mer-26 mer);


X026 = pRK311-MPG + SpsN (573 bp, 22 mer-27 mer);


X028 = pRK311-MPG (385 bp, 22 mer-26 mer);


X029 = pRK311-MPG + SpsN (573 bp, 22 mer-27 mer);


Z959-1 to -3 = independent clones having pRK311-s88nc2 EH2700 bp spsN::Tn10Kn;


Z967 = pRK311-BH716 bp;


+ means the transconjugants produce exopolysaccharide, and


− means transconjugants do not produce exopolysaccharide on a selection plate.






These results demonstrate that the nucleic acid molecules encoding SpsN (e.g., X029) were capable of inhibiting polymer synthesis in Sphingomonas S-7, S-130, S-194, S-198, S-88, NW11, and Xanthomonas X59.
From analysis of the sequenced amplicon, spsN (modulator of exopolysaccharide biosynthesis) was located downstream of DAHPS (3-deoxy-D-arabino-heptulosonic acid 7-phosphate synthase). DAHPS regulates aromatic amino acid biosynthesis. The active PCR product was cloned into pRK311 and called X029 (pRK311-spsN, Tetr). This expression vector, which contains SEQ ID NO:1, was trans-conjugated into Sphingomonas α016, and named α027, which had a suppressed polymer production phenotype. Then this α027 was treated with EMS to find mutants that showed an exopolysaccharide-positive phenotype under drug pressure Tet (i.e., in the presence of X029, which encodes the modulator of exopolysaccharide biosynthesis, SpsN). Under these conditions, some of the exopolysaccharide-positive phenotype could be due to mutations in either SpsN or elsewhere. After selection under no drug condition to get rid of plasmid X029 (i.e., encoding SpsN), strains α061-α076 were selected and saved for further testing (e.g., biomass production). These strains were cultivated in grass tube that contain 4 ml B10 medium with 5% glucose for 24 hrs. Then 3 ml of those cultures were inoculated into 25 ml B10 seed medium with 3% glucose in 125 ml baffled flask at 300 rpm for 48 hrs. From the each flask, 10 g of culture broth was precipitated by 2 vol of IPA. Precipitated materials were dried at 60° C. for 6 hrs.













Dry Weight




















α061
13.18 g/L




α062
13.94
somewhat capsule-slime



α063
14.16
slimy on plate



α064
11.85



α065
15.77
slimy on plate



α066
12.13



α067
13.47



α068
13.66



α069
14.13
slimy on plate



α070
13.94



α071
13.60



α072
12.81



α073
13.10



α074
12.06



α075
 9.29



α076
10.86










2 ml culture was inoculated into 30 ml B10 seed medium with 5% glucose in 125 ml baffled flask. It was incubated at 200 rpm for 40 hrs and at 300 rpm until 72 hrs.
The following table indicates that the mutants (i.e., α062, α063, and α065) produced more than 20% biomass than that of original X287 slime mutant.















OD600
pH
DW(g/L)





















1
α062
11.5
5.72
14.0
+24% (white slime)


2
α063
12.6
5.71
13.9
+23% (white slime)


3
α065
11.1
5.57
14.3
+27% (white slime)


4
α016
12.5
5.71
13.1
+16% (white slime)


5
X287
10.1
5.73
11.3
Base (Original slime)









The components of the culture medium were as follows:















B10Medium
Seed
Production






















Glucose
30
g/L
45
g/L



NH4NO3
1
g/L
1.25
g/L



MSP*
1
g/L
1.00
g/L



K2HPO4
3.2
g/L
0.50
g/L



KH2PO4
1.6
g/L



MgSO4*
0.2
g/L
0.05
g/L



Trace minerals*
1
ml/L
1
ml/L



4% Deformer*


1.5
ml/L



DI Water
1
L
1
L






















×1000 Trace Minerals

×1000 conc


















2703 mg
FeCl3—6H2O
270.3 g/mol
10 mM


1363 mg
ZnCl2
136.3 g/mol
10 mM


1979 mg
MnCl2—4H2O
197.9 g/mol
10 mM


 238 mg
CoCl2—6H2O
237.93 g/mol 
 1 mM


 242 mg
Na2MoO4—2H2O
241.95 g/mol 
 1 mM


 250 mg
CuSo4—5H2O
249.7 g/mol
 1 mM







to 1000 ml divide to 4 in 250 ml









Example 3
Comparison of Exopolysaccharide Productions Between a Sphingomonas Strain No Longer Responsive to SpsN and its Parent Strains
The original slime strain X287 and α016 were compared with mutant α062 under several 42 L fermentation tests. 400 ml 24 hrs flask culture was prepared as 1% starting culture broth for those experiments. The strain ATCC31464, parent of X287, was used a capsule forming gellan wild type strain.










42L/70L-fermentation test (40 g/L Glucose)











24 hrs
48 hrs
60 hrs














X287(G116)
11.0 g/L-7980 cp
21.8 g/L-16,000 cp



α016(G118)
 9.6 g/L-5040 cp
19.2 g/L-10,400 cp
20.7 g/L-





11,900 cp


α062(G120)

23.2 g/L-13,500 cp


α062(G131)
10.3 g/L-6650 cp
22.8 g/L-13,100 cp



















42L/70L-fermentation test (45*-50 g/L Glucose)












24 hrs
48 hrs
60 hrs
72 hrs















α062(G121)
6.6 g/L-4160 cp
21.6 g/L-12,300 cp

26.1 g/L-18,000 cp


α062(G123)
8.8 g/L-5210 cp
21.7 g/L-15,800 cp

25.5 g/L-24,700 cp


α062(G131)
6.9 g/L-3910 cp
23.2 g/L-12,800 cp
25.7 g/L-16,200 cp









The broth was precipitated by 2 volumes IPA and subsequently dried at 60° C. for 6 hours. The final viscosity was 4-12 rpm.
The fermentation scores (biomass yield) are as follows.















X287
Duration
Glucose
Biomass
residual Glc
broth viscosity







G115
70 hrs
40 g/L
18.4 g/L
  0 g/L
16,400 cp


G116
48 hrs
40 g/L
21.8 g/L
0.2 g/L
16,000 cp


G100
70 hrs
50 g/L
22.9 g/L
4.8 g/L
27,700 cp
























α016
Time
Glucose
Biomass
residual Glc
broth viscosity







G118
60 hrs
40 g/L
20.7 g/L
0.6 g/L
11,900 cp
























α062
Time
Glucose
Biomass
residual Glc
broth viscosity







G120
48 hrs
40 g/L
23.1 g/L
  0 g/L
13,500 cp


G131
48 hrs
40 g/L
22.8 g/L
  0 g/L
13,100 cp


G132
48 hrs
40 g/L
22.7 g/L
0.5 g/L
14,400 cp


G127
53 hrs
40 g/L
23.7 g/L
1.3 g/L
13,700 cp


G121
72 hrs
50 g/L
26.1 g/L
2.5 g/L
18,000 cp


G122
71 hrs
50 g/L
25.9 g/L
4.5 g/L
19,900 cp


G128
60 hrs
45 g/L
25.7 g/L
1.9 g/L
17,500 cp


G139
72 hrs
45 g/L
26.3 g/L
1.9 g/L
18,200 cp


G141
59 hrs
45 g/L
26.4 g/L
  0 g/L
15,300 cp


G158
57 hrs
45 g/L
26.4 g/L
0.8 g/L
15,800 cp


G161
72 hrs
45 g/L
26.2 g/L
0.5 g/L
21,700 cp























ATCC31461
Glucose
Biomass
residual Glc
broth viscosity




















G157
72 hrs
45 g/L
22.1 g/L
4.3 g/L
48,100 cp









Culture Broth of α062(G158) was compared with that of ATCC31461(G157). The results are shown in the following table.










(45 g/L glucose) using 70L-fermentor









Final Broth
α062 (G158)
ATCC31461 (G157)





Frozen
G149F
061501C


Total Biomass (g/L)
 26.4 (59.7%)
  22.3 (54.8%)


Residual Glucose (g/L)
  0.8
  4.3


Breach debris (g/L) (PHB)
  9.1 (20.6%)
  6.8 (16.7%)


Duration (hrs)
 57
  72


pH(—)
  6.7
  5.17


OD600(—)
 23.4
  27.3


Viscosity (# 4 12-60 rpm)
15,800-3620
48,100-ND


Living cells (cells/ml)
1.6 × 1010
9.0 × 108




(not accurate)


5% KOH consumption (ml)
1270
>1690


Broth appearance
Homogeneous slime
Not homogeneous


Broth DO (%) hit 0%
None
36~39 hrs









Example 4
Identification of Xanyhomonas No Longer Responsive to SpsN
The DNA sequence contains biopolymer suppression factor in X029 (ATCC PTA-5127) was transconjugated into Xanthomonas campestris X55 (ATCC13951) and X59 (ATCC 55298) by mating. Polymer production suppressed colonies were isolated as α287, α300 and α301 on tetracycline containing selection plate.
This Xanthan Gum production suppressed α300 (X59:X029) transconjugant was treated with chemical mutagen EMS. Mutant colonies that do not respond to suppression factor X029 even under drug pressure were isolated first then drug sensitive mutants α449 (ATCC PTA-5064), α474, α485, α499, α501, α525, α526, α544 were selected under no drug pressure to get rid of the X029 suppression factor. Those mutants were incubated in 26 ml YM plus 3& glucose medium using 125 ml baffled flask for 48 hrs. Those mutants performance were shown in the following table.
Comparison Between X59 and its Mutants

















24/32/48




0/24/32/48
0/24/32/48
hours




OD600
pH
DW (g/L)




















1
α449
0.31/7.86/7.62/
6.27/7.28/6.87/
9.8/12.0/16.4
Ave = 16.0




9.24
5.43




2
α474
0.27/6.70/6.19/
6.31/7.48/7.04/
9.9/11.2/15.6





5.79
6.37




3
α485
0.29/6.82/6.60/
6.26/7.23/7.03/
7.1/11.3/16.0





7.10
5.94




4
α499
0.28/6.99/6.43/
6.25/7.40/7.07/
8.1/10.8/15.7





6.34
6.10




5
α501
0.26/7.13/6.73/
6.32/7.22/7.04/
7.7/12.2/16.2





5.13
6.23




6
α525
0.28/6.99/6.84/
6.29/7.32/7.09/
7.5/11.0/16.3





8.34
6.01




7
α526
0.30/7.59/7.22/
6.24/7.33/6.99/
7.7/11.6/16.5





7.54
5.71




8
α544
0.24/7.52/5.99/
6.28/7.27/7.11/
7.3/9.3/15.5





4.99
6.57




9
X59
0.27/7.28/6.74/
6.24/7.24/7.03/
7.4/10.0/15.3
Ave = 15.4




6.17
5.93




10
X59
0.27/7.21/6.94/
6.23/7.29/7.00/
8.1/9.7/15.5





7.02
5.67























OD600(0/24/32/48)
Living cell#(0/24/32/48)



















1
α449
0.31/7.86/7.62/9.24
3.9 × 108/8.9 × 109/8.4 × 109/





1.0 × 1010


2
α474
0.27/6.70/6.19/5.79
3.9 × 108/1.3 × 1010/4.6 × 109/





8.0 × 109


3
α485
0.29/6.82/6.60/7.10
3.7 × 108/9.3 × 109/1.2 × 1010/





8.4 × 109


4
α499
0.28/6.99/6.43/6.34
4.5 × 108/6.9 × 109/5.7 × 109/7.4 × 109


5
α501
0.26/7.13/6.73/5.13
4.0 × 108/1.0 × 1010/1.0 × 1010/





7.4 × 109


6
α525
0.28/6.99/6.84/8.34
3.7 × 108/9.9 × 109/6.0 × 109/9.5 × 109


7
α526
0.30/7.59/7.22/7.54
4.6 × 108/1.0 × 1010/1.4 × 1010/ND


8
α544
0.24/7.52/5.99/4.99
3.7 × 108/7.8 × 109/6.6 × 109/





1.3 × 1010


9
X59
0.27/7.28/6.74/6.17
3.6 × 108/8.1 × 109/9.0 × 109/6.9 × 109


10
X59
0.27/7.21/6.94/7.02
4.6 × 108/8.7 × 109/6.6 × 109/6.8 × 109









α449 and α501 generated 10-20% more biomass than that of parent X59 in 32 hrs even with the same level of living cell number. This indicates that polymer accumulation speed of those mutants is faster than that of parent X59.
FIG. 1 shows relation between living cell number and OD600 of α449 culture. To achieve optimum seed culture, cell numbers were maximized based upon OD600 value for next stage of production fermentation.
FIG. 2 shows α449 42 L production fermentation using SEB-022-SF+MSP medium. The open circle represents xanthan gum production from fermentation of X59 or α449 in SEB-022-MSP in a 6 L fermentor; the solid circle represents biomass (including cells and xanthan gum) of fermentation of α449 using SEB-022-SF+MSP (also referred to as “SFM”) in a 70 L fermentor; and the triangle represents xanthan gum production from fermentation of ATCC13951. The data of the ATCC13951 fermentation in FIG. 2 is from Letisse et al., Applied Microbiology and Biotechnology 55(4): 417-22, 2001. MSP refers to digested soy protein.
The final production yield was 57.3 g/L out of 80 g/L sucrose. This mutant did not respond to suppression factor X029 and accumulated higher level of Xanthan gum under the conditions of 28° C., dissolved oxygen (DO) at 30%, and pH6.5.
The α449 400 ml seed culture was inoculated into SEB-022-SF+FMSP (Suc=80 g/L) medium and incubated for 70 hrs using 70 L fermentor. This medium contains 0.69 g/L total nitrogen (0.6 g/L from Soy and 0.09 g/L from MSP). The final broth OD was 11.3, pH was 6.55, and the living cell number was 2.0×1010/ml. The final broth viscosity was 34,900 cp/16,300 cp/9,420 cp-12 rpm/30 rpm/60 rpm using No. 4 spindle by Brookfield viscometer.
The components of SEC-022-SF+MSP medium used in this example are as follows:

















Sucrose
80.0
g/L



MSP
1.0
g/L (N = 0.09)



MgSO4
0.5
g/L



K2HPO4
2.0
g/L



Soy Protein
7.6
g/L (N = 0.6)



4% DF289
1
ml/L



Trace
1
ml/L










The components of SEC-022-MSP medium used in this example are as follows:

















Sucrose
60.0
g/L



MSP
1.0
g/L (N = 0.09)



MgSO4
0.5
g/L



K2HPO4
2.0
g/L



Soy Protein
7.6
g/L (N = 0.6)



4% DF289
1
ml/L



Trace
1
ml/L

## Claims

1. A method for hyper-producing exopolysaccharide, comprising:
culturing a first strain of bacteria under conditions and for a time sufficient to permit exopolysaccharide production in a bacterial culture which comprises said first strain of bacteria,
wherein the first strain of bacteria is capable of exopolysaccharide hyper-production in slime form even when expressing a polypeptide encoded by a nucleic acid molecule that comprises a nucleotide sequence that is capable of hybridization to a probe under conditions that comprise exposure to 2×SSPE and 50% formamide at 42° C., wherein the probe consists of the nucleotide sequence set forth in SEQ ID NO:1 or a complement of SEQ ID NO:1, and wherein said polypeptide comprises the amino acid sequence of SEQ ID NO:2 or a derivative thereof having at least about 95% sequence identity to SEQ ID NO:2, wherein the polypeptide inhibits sphingan production when present in a Sphingomonas species compared to sphingan production in an unmodified Sphingomona, 
and wherein said first strain of bacteria produces statistically significantly more exopolysaccharide than does a second strain of bacteria that is not capable of exopolysaccharide hyper-production in slime form when expressing the polypeptide; and
separating the exopolysaccharide in slime form from the bacterial culture.

2. The method according to claim 1 wherein the bacteria are Sphingomonas bacteria.

3. The method according to claim 2 wherein said Sphingomonas bacteria are capable of hyper-producing an exopolysaccharide selected from the group consisting of gellan, welan, rhamsan, diutan, alcalan, S7, S88, S198, and NW11.

4. The method according to claim 1 wherein the bacteria are Sphingomonas strains α062 (ATCC PTA-4426).

5. The method according to claim 1 wherein the bacteria are Xanthomonas strain α449 (ATCC PTA-5064).

6. The method according to any one of claims 1 to 4 wherein the culturing comprises fermenting.

7. The method according to claim 6 wherein said bacteria produce from about 20 grams to about 60 grams of exopolysaccharide per liter of culture.

8. The method according to claim 6 wherein the fermentation is conducted from about 48 hours to about 96 hours at a temperature ranging from about 25° C. to about 35° C.

9. The method according to claim 6 wherein the separating of exopolysaccharide comprises alcohol precipitation.

10. The method according to claim 9 wherein alcohol precipitation comprises adding about 1 to about 1.5 culture volumes of alcohol to the culture.

11. The method according to claim 10 wherein the fermentation culture has a viscosity ranging from about 15,000 cp to about 40,000 cp.