Method for separating nucleic acids by means of liquid chromatography

Abstract: Disclosed is a method for separating nucleic acids by hydrophobic interaction chromatography. The purpose is to provide a method for separating and purifying nucleic acids by hydrophobic interaction chromatography, which enables to separate nucleic acids such as plasmids and DNA fragments in a shorter time.

Description: The present invention relates to a method for separating and purifying nucleic acids to be used for genome analysis or gene manipulation. In more detail, it relates to a method for separating long chain nucleic acids represented by particular DNA contained in the cells of animals, human, etc. that are effective for gene therapy to be utilized for the therapy of genetic disease etc. due to DNA abnormality, by utilizing liquid chromatography, for example, plasmids, in bacteria, organelle DNA, phage DNA, etc. In recent years, gene therapy is attracting attention, and a method for separating and purifying a large quantity of long chain nucleic acids such as plasmids and DNA fragments to be used for gene therapy in a simpler way and in shorter time is desired. For using nucleic acids for the therapy of human, it is desirable that the nucleic acids can be separated and purified keeping the same structure (higher-order structure) as they exist in organisms. Here, since the enzyme reaction is utilized for the recombination of nucleic acids, the nucleic acids are required to have been separated and purified to the extent that they can become the substrate for reaction. Also, in order to avoid the adverse effect of impurities in human body, the nucleic acids are required to have been separated and purified up to high degrees of purity. For separating and purifying long chain nucleic acids such as DNAs and plasmids contained in the cells and bacteria, chemical treatment methods have been used most frequently, so far. Among various long chain nucleic acids used for gene therapy, in particular, a plasmid is currently utilized in many cases, because of limited cleavage sites by particular restriction enzymes and relatively easy recombination manipulation. In the following, a general example of purifying a plasmid from Escherichia coli will be shown. First, the cell wall is digested by treating with lysozyme for a short time, and RNase to degrade RNAs of Escherichia coli is added. Next, a mixed solution of NaOH and sodium dodecylsulfate (SDS) is added for the purpose of dissolving the cytoplasmic membrane. NaOH partially denatures DNAs and partially degrades RNAs and SDS acts to dissolve the membrane and to denature proteins. Successively, the SDS-protein complex and cell debris are precipitated by adding 5N potassium acetate (pH 4.8). At this time, the pH is important for both to neutralize NaOH used in said manipulation and to renature the plasmid. Thereafter, centrifugation is applied to remove the precipitates, thus obtaining the desired plasmids in the supernatant. In a series of these manipulations (hereinafter referred to as pretreatment process), it is important to mix the components slowly and firmly. If introducing violent vibration during this manipulation, then the bacterial chromosomal DNA is cut off to small fragments so that they cannot aggregate, causing them to contaminate the plasmid. Successively, isopropanol is added to the supernatant, and the mixture is centrifuged to precipitate and concentrate plasmids. Finally, protein is removed from the plasmid fraction by precipitating with phenol and chloroform, and the plasmid is precipitated with alcohol. Through a series of manipulations as described above, it is possible to obtain a plasmid with relatively high purity (hereinafter, said method of separating and purifying nucleic acid is referred to as chemical separating method). However, with the chemical separating method, the separating and purifying process is complicated and a large quantity of organic solvent must be used, hence it poses many problems such as disposal of waste solvents and others. Besides the chemical separating and purifying method, there is a method of separating plasmids by electrophoresis. This method is a technique having the highest resolution at the moment. The electrophoretic method includes paper electrophoresis and gel electrophoresis, and gel electrophoresis is common currently. The electrophoretic method has an advantage of obtaining plasmids with very high purity, while it has many problems such as long separation time, difficult collection, low sample loading, etc. Consequently, at present electrophoretic separation is used only when the purity of plasmid fraction purified by the above chemical separating and purifying method should be improved further. For solving the problems in the chemical separating and purifying method and the electrophoretic separation as explained above, a method of separating and purifying nucleic acids that utilizes liquid chromatography has been used recently. So far, there are examples, wherein long chain nucleic acids such as plasmids were separated and purified by using ion exchange chromatography and reversed phase chromatography. Separating and purifying nucleic acids utilizing liquid chromatography is favourable in that manipulation is simple compared with chemical separating methods, easy collection of nucleic acids and no necessity of using organic solvent etc. With said conventional method using the ion exchange chromatographic method or reversed phase chromatographic method alone, however, there is a problem that the nucleic acids with sufficiently high purity, in particular, long chain nucleic acids such as plasmids cannot be obtained in large quantity. Therefore, the invention aims at providing a separating method that utilizes liquid chromatography, with which it is possible to separate a large quantity of long chain nucleic acids such as plasmids and DNAs in a shorter time. The invention as defined in claim 1 of the present application having been made in view of the aforementioned purpose provides a method of separating a plasmid from a solution containing the plasmid together with contaminants selected from the group consisting of proteins, RNAs, DNAs and mixtures thereof, characterized by using hydrophobic interaction chromatography. The invention as defined in claim 3 of the present application provides a method for separating and purifying a plasmid from a solution containing the plasmid together with contaminants selected from the group consisting of proteins, RNAs, DNAs and mixtures thereof, characterized by using hydrophobic interaction chromatography and ion exchange chromatography in combination. Fig. 1 is a chromatogram showing the result of separating a cleared lysate of Escherichia coli by means of hydrophobic interaction chromatography according to Example 1. Fig. 2 is a chromatogram showing the result of separating an eluate of hydrophobic interaction chromatography by means of ion exchange chromatography according to Example 1. Fig. 3 is a schematic diagram of the images of gel electrophoresis showing the results of the purity assay of plasmid fractions obtained according to Example 1 and Comparative Example 1. Fig. 4 is a chromatogram showing the result of separating a cleared lysate of Escherichia coli separated by means of ion exchange chromatography according to Comparative Example 1. Fig. 5 is a chromatogram showing the result of separating a cleared lysate of Escherichia coli by means of hydrophobic interaction chromatography according to Example 2. Fig. 6 is a chromatogram showing the result of separating an eluate of hydrophobic interaction chromatography by means of ion exchange chromatography according to Example 2. Fig. 7 is a chromatogram showing the result of separating a cleared lysate of Escherichia coli by means of ion exchange chromatography according to Comparative Example 2. In the Figures, the numerals represent the following: numeral 1 peak of impurities numeral 2 peak of plasmid-fraction numeral 3 DNA size marker numeral 4 plasmid-fraction obtained by comparative Example 1 numeral 5 plasmid-fraction obtained by Example 1 numeral 6 commercial purified plasmid In the following, the invention will be illustrated in detail using the case of separating and purifying a plasmid being a long chain nucleic acid from Escherichia coli , cultured in large quantity as an example. In such case, the inventive methods are useful for separating and purifying nucleic acids such as plasmids and DNAs being the desired products. The compounds to be used for the synthesis of base materials that are used for the packing material for the hydrophobic interaction chromatography and ion exchange chromatography to be used in the invention may be any compounds, if various functional groups that exhibit hydrophobicity or various ion exchange groups can be introduced by a post-reaction after the base materials were synthesized in both cases. For example, as monofunctional monomers, styrene, o-halomethylstyrene, m-halomethylstyrene, p-halomethylstyrene, o-haloalkylstyrene, m-haloalkylstyrene, p-haloalkylstyrene, α-methylstyrene, α-methyl-o-halomethylstyrene, α-methyl-m-halomethylstyrene, α-methyl-p-halomethylstyrene, α-methyl-o-haloalkylstyrene, α-methyl-m-haloalkylstyrene, α-methyl-p-haloalkylstyrene, o-hydroxymethylstyrene, m-hydroxymethylstyrene, p-hydroxymethylstyrene, o-hydroxyalkylstyrene, m-hydroxyalkylstyrene, p-hydroxylalkylstyrene, α-methyl-o-hydroxymethylstyrene, α-methyl-m-hydroxymethylstyrene, α-methyl-p-hydroxymethylstyrene, α-methyl-o-hydroxyalkylstyrene, α-methyl-m-hydroxyalkylstyrene, α-methyl-p-hydroxyalkylstyrene, glycidyl methacrylate, glycidyl acrylate, hydroxyethyl acrylate, hydroxymethacrylate, vinyl acetate, etc. can be exemplified. Here, as examples of haloalkyl groups substituted on an aromatic ring, halogens such as Cl, Br, I and F and straight chain and/or branched saturated hydrocarbons with carbon atoms of 2 to 15 are mentioned. As polyfunctional monomers, divinylbenzene, trivinylbenzene, divinyltoluene, trivinyltoluene, divinylnaphthalene, trivinylnaphthalene, ethylene glycol dimethacrylate, ethylene glycol diacrylate, diethylene glycol dimethacrylate, diethylene glycol diacrylate, methylenebismethacrylamide, methylenebisacrylamide, etc. can be exemplified. As described above, for the compounds to be used in the invention, there is no special restriction, provided it is possible to introduce various functional groups that exhibit hydrophobicity or various ion exchange groups by the post-reaction, but, in order to minimize the influence on the products desired to separate due to the hydrophobicity exhibited by the base material itself, or the swelling or shirinking of the base material itself due to the change in salt concentration and the change in pH value, it is particularly preferable to prepare the base material using relatively hydrophilic monomers, for example, glycidyl methacrylate, glycidyl acrylate, hydroxyethyl acrylate, hydroxymethacrylate, vinyl acetate, etc. How to commonly make the base material using said monomers is as follows (how to make the base material is not confined to a method shown here): First, monofunctional monomers and polyfunctional monomers are weighed out at an appropriate ratio and precisely weighed-out diluent (solvent used for the purpose of adjusting the pores in the particles formed) and similarly precisely weighed-out; the polymerization initiator is added, followed by well stirring. The mixture is submitted to a so-called oil-in-water type suspension polymerization wherein the mixture is added into an aqueous solution comprising a dissolved suspension stabilizer weighed out precisely beforehand, and oil droplets with the desired size are formed by mixing with a stirrer, and polymerization is conducted by gradually warming the mixed solution. The ratio of monofunctional monomer to polyfunctional monomer is not particularly restricted, and, to 1 mol of monofunctional monomer, around 0.01 to 0.2 mol of polyfunctional monomer are used in the case of making relatively soft particles (base material) and around 0.2 to 0.5 mol of that in the case of making hard particles; in the case of making harder particles, polyfunctional monomer alone may be used. The polymerization initiator is also not particularly restricted, and the azobis type and/or the peroxide type being used commonly may be used. The suspension stabilizer is also not particularly restricted, and, if possible to prevent the aggregation among oil droplets themselves, any ionic surfactants, nonionic surfactants and polymers with amphipathic property or mixtures of these can be used. The diameter of formed particles is also not particularly restricted and particles with appropriate diameter of 2 to 500 µm may be selected in line with the use purpose. For example, when aiming at analysis, the particle diameter is favourably 2 to 30 µm, more preferably around 2 to 10 µm. When aiming at large scale purification of nucleic acids with high purity, the diameter is around 10 to 100 µm and, when separating the desired product from crude stock solution, it may be 100 to 500 µm, more preferably around 200 to 400 µm. For adjusting the particle diameter, the rotational speed of the stirrer may be adjusted during polymerization; when particles with small diameter are needed, the number of revolutions may be increased and, when large particles are desired, the number of revolutions may be decreased. Here, since the diluent to be used is used for adjusting pores in the formed particles, the selection of the diluent is particularly important. As a fundamental concept, for the solvent to be used for polymerization, adjustment is made by varying combinations of a solvent that is a poor solvent for the monomer with a solvent that is a good solvent for the monomer. The size of pore diameter may be selected appropriately depending on the molecular size of the nucleic acids which one aims to separate, but it is preferable within a range of 500 to 4000 Angstroms for the packing material for the hydrophobic interaction chromatography and within a range from 1500 to 4000 Angstroms for the packing material for the ion exchange chromatography. In the hydrophobic interaction chromatography, for separating nucleic acids with different hydrophobicity preferable by utilizing packing materials with different hydrophobicity, respectively, the surface modification of the base material is important. The applicable hydrophobic group is not particularly restricted as long as it does not deviate from the purpose to separate nucleic acids with different hydrophobicity with packing materials with different hydrophobicity, respectively, but hydrophobic groups having one or more kinds of compounds selected from a group consisting of following compounds (a) through (c) as major components are particularly preferable. Compounds (a): These may be long chained or branched, saturated hydrocarbon groups or unsaturated hydrocarbon groups with carbon atoms of 2 to 20 (however, aromatic ring may be contained in the hydrocarbon group). Compounds (b): Compounds represented by a following structural formula (1) (however, n = 0 ~ 20 and the alkylene group may be straight chained or branched, m = 0 ∼ 3 and the hydrocarbon group may be straight chained or branched, and A is a C = 0 group or an ether group, but the alkylene group may be bonded directly to the base material without A). Compounds (c): Ether group of alkylene glycol with carbon atoms of 2 to 20, which consists of repeating units of 0 to 10 (however, the opposite end of functional group reacted with the base material may be an OH group left as it is or may be capped with alkyl group with carbon atoms of 1 to 4). When modifying the surface using compounds dividable into three categories as above, they may be used solely or in mixture. In the following , one example of different ways to use them will be explained, taking alkyl groups that belong to Compounds (a) as an example. For example, for separating compounds with high hydrophobicity such as RNA originating from Escherichia coli and RNA in the cells of humans and animals, alkyl groups with carbon atoms of 2 to 15 are particularly suitable. Moreover, in the case of compounds with relatively low hydrophobicity such as DNAs originating from Escherichia coli and DNAs in the cells of humans and animals, alkyl groups with carbon atoms of 4 to 18 are particularly suitable. Furthermore, in the case of compounds with low hydrophobicity like plasmids, alkyl groups with carbon atoms of 6 to 20 are suitable. Upon separating these compounds, compounds may be selected appropriately to modify the surface without being confined to said exemplification. The reason for this is that the degree of hydrophobicity of the packing material varies depending on the concentration of salt in the medium or the concentration of salt in the eluent for adsorption. Moreover, this is because of the fact that, even with the same functional group, the degree of hydrophobicity of the packing material differs depending on the amount of the group introduced into the base material. The pore diameter of the base material for hydrophobic interaction chromatography is particularly preferable to be 500 to 4000 Angstroms, but it can be selected appropriately from said range depending on the molecular size of the nucleic acids which one aims to separate. In general, since the retention of nucleic acids on the packing material and the adsorption capacity (sample loading) differ depending on the pore diameter, it is preferable to use a base material with large pore diameter for nucleic acids with large molecular size and a base material with small pore diameter for nucleic acids with small molecular size. Next, one example of the methods for reacting these hydrophobic groups with base material will be described. In the case of the base material being a styrene base and reacting with compounds in the first and second category, using a halogen-containing compound B and/or a carbonyl halide C and a catalyst such as FeCl 3 , SnCl 2 or AlCl 3 , and utilizing Friedel-Craft reaction, it is possible to add directly to an aromatic ring in the base material a dehalogenated compound B and/or acylated compound C. In the case of the base material being a particle containing a halogen group and, for example, using compounds with OH contained in functional group to be added, like butanol, and utilizing Williamson reaction with alkali catalyst such as NaOH or KOH, it is possible to introduce the functional group through an ether bond. In the case of the functional group which one intends to add being an amino group-containing compound, like hexylamine, it is possible to introduce this compound by using an alkali catalyst such as NaOH or KOH followed by a dehydrohalogenation reaction. If an epoxy group is to be introduced into a base material containing OH groups, halogen groups or carbonyl halide groups may be introduced beforehand into the functional group to be added, so that it is possible to introduce the functional group through an ether or ester bond. In the case of the base material containing epoxy groups, and if reacting with a compound with OH groups or amino groups contained in the functional group one intends to add, it is possible to introduce the functional groups through an ether or amino bond. Moreover, if the functional group one intends to add contains halogen groups, it is possible to add the functional group through an ether bond using an acid catalyst. Since the proportion of functional groups to be introduced into the base material is influenced by the hydrophobicity of subject product to be separated, preferably in general, packing material with around 0.05 to 4.0 mmol of functional groups added per 1 g of dried base material is suitable. With respect to the surface modification, a method of adding the functional groups through post-reaction after formation of the base material (particles) has been exemplified above, but no difference exists, even if a method may be adopted, wherein the base material is formed after polymerization using monomers with said functional groups added before polymerization, thus posing no particular problem. In addition, the base material to be used may also be porous silica gel. As an example of the method of manufacturing silica gel, silane coupling may also be conducted, using a compound such as alkyltrimethoxysilane, directly onto particles manufactured according to the method described in "Latest High-Speed Liquid Chromatography", page 289 ff. (written by Toshio Nambara and Nobuo Ikegawa, published by Tokyo Hirokawa Bookstore in 1988). Or, after conducting the silane coupling using an epoxy group-containing silane coupling agent, the functional group may be added according to the method aforementioned. As for the proportion of functional groups to be introduced, packing material with around 0.05 to 4.0 mmol of functional groups added per 1 g of dried base material is suitable. Next, one example of the methods of separating and purifying a nucleic acid using these packing materials will be described. First, as the eluents to be used for the hydrophobic interaction chromatography of the invention, at least two types of eluents consisting of eluent A containing high-concentration of salt and eluent B containing low-concentration of salt are used. The eluting method switching stepwise from eluent A to eluent B and the gradient eluting method continuously changing the composition from eluent A to eluent B can be used. For the buffers and salts to be used in these eluents, those used usually for hydrophobic interaction chromatography can be used. For the eluent A containing high-concentration of salt, an aqueous solution with a salt concentration of 1.0 to 4.5M and a pH value of 6 to 8 is particularly preferable. For the eluent B containing low-concentration of salt, an aqueous solution with a salt concentration of 0.01 to 0.5M and a pH value of 6 to 8 is particularly preferable. For the salts, ammonium sulfate and sodium sulfate can be exemplified. In the invention, it is particularly preferable to conduct the hydrophobic interaction chromatography by combining a packing material having a functional group with weak hydrophobicity with a packing material having a functional group with strong hydrophobicity in sequence. This method is suitable particularly for the separation of plasmids. For example, in the medium wherein Escherichia coli has been cultured in large quantity, various components with different hydrophobicity such as polysaccharides, Escherichia coli genome DNA, RNAs plasmids and proteins are contained, and, according to the inventors' knowledge, there are differences in the hydrophobicity even among nucleic acids themselves; protein impurities have higher hydrophobicity compared with plasmids which are the desired product. Hence, by connecting columns packed with various packing materials with different hydrophobicity in order from lower hydrophobicity, plasmids can be separated and purified efficiently. Concretely, after adsorbing sequentially onto the packing materials with increasing higher hydrophobicity in order from higher hydrophobicity of components in the medium, the column with the desired component adsorbed alone is detached and eluted. In the invention, it is preferable to separate and purify nucleic acids by hydrophobic interaction chromatography and ion exchange chromatography in combination for efficiently obtaining nucleic acids with high purity in large quantity. Here, for the hydrophobic interaction chromatography, packing material etc. as described above can be used. Moreover, here, as the hydrophobic interaction chromatography, it is particularly preferable to connect columns packed with various packing materials different in hydrophobicity in order from lower hydrophobicity. The packing material to be used for ion exchange chromatography for purifying the desired plasmid having been separated beforehand by means of hydrophobic interaction chromatography further to higher purity is preferable to have relatively large pore diameter, particularly within a range from 1500 to 4000 angstroms. How to commonly make the base material used for ion exchange chromatography is as described above, and the surface modification to introduce ion exchange groups to these base materials can be performed by publicly known methods. As the eluents to be used for the ion exchange chromatography, at least two types of eluents consisting of eluent C containing a low concentration of salt and eluent D containing a high concentration of salt are used. The eluting method switching stepwise from eluent C to eluent D and the gradient eluting method continuously changing the composition from eluent C to eluent D can be used. For the buffers and salts to be used in these eluents, those used usually for the ion exchange chromatography can be used. For the eluent C containing a low concentration of salt, an aqueous solution with a concentration of buffer of 10 to 50 mM and pH value of 6 to 9 is particularly preferable. For the eluent D containing a high concentration of salt, an aqueous solution with 0.1 to 2M sodium salt added to eluent C is particularly preferable. As sodium salts, sodium chloride and sodium sulfate can be mentioned. Moreover, a component other than buffer can be contained in both eluents, and, in particular, a chelating agent for a bivalent metal ion, for example, ethylenediamine-tetraacetic acid is particularly in the case of separating plasmids preferable, since it can inhibit the degradation of plasmids due to DNA-degrading enzymes in the lysate of Escherichia coli . The concentration of the chelating agent for the bivalent metal ion is preferably 0.1 to 100 mM. And, in the particularly preferable embodiment of the invention, the eluent A with high salt concentration prepared according to the aforementioned method is passed through columns of hydrophobic interaction chromatography, which are connected in order from lower hydrophobicity. After having reached the stationary state, the medium of Escherichia coli etc. is injected into a column omitting the degrading manipulation of RNA with degrading enzyme etc. Successively, the eluent A is passed through to flow out the compounds that were not adsorbed in any column outside the system. Thereafter, the column with the desired compound adsorbed alone is detached and the desired product is eluted by the stepwise method or gradient method. Following this, the eluent C is passed through said ion exchange column, and, after the stationary state has been reached, the elute containing the desired product is injected as it is. Thereafter using the eluent D, the desired product is eluted by a stepwise method or gradient method to obtain the purified product. The invention provides a method for separating and purifying nucleic acids by simple manipulation. Concretely, in the preferable embodiment of the invention using columns wherein columns packed respectively with packing materials different in hydrophobicity are connected in order from lower hydrophobicity, the desired nucleic acids, in particular, long chain nucleic acids such as plasmids can be separated and purified simply in large quantity only by passing the solution from the pretreatment process in the conventional manipulation. Besides, in the invention, it is also possible to separate and purify nucleic acids by passing the solution obtained from the pretreatment process involving degrading manipulation of Escherichia coli -originated RNA with degrading enzyme in the conventional pretreatment process which was omitted above, directly through the columns of hydrophobic chromatography. In the invention, if using the hydrophobic interaction chromatography and the ion exchange chromatography in combination, which is preferable in particular, it is possible to separate and purify the desired nucleic acids with high purity, in particular, long chain nucleic acids such as plasmids in large quantity by simple manipulation. As described, according to the inventive method for separating nucleic acids, the desired products with high purity can be obtained in large quantity by simpler manipulation over the conventional method. In the following, the invention will be illustrated in more detail based on the examples, but the invention is not confined to these examples. Example 1 (1) Preparation of packing material for hydrophobic interaction chromatography Employing a packing material for gel filtration chromatography (G6000PW (from Tosoh Corp.)) with average particle diameter of 20 µm and average pore diameter of 2000 angstroms as the base material, the packing material for the hydrophobic interaction chromatography was prepared. A mixture of 20 g of G6000PW washed and substituted with 1,4-dioxane, 20 g of 1,4-dioxane and 1 g of 1,2-epoxybutane was stirred and mixed for 6 hours at 45 °C to obtain a packing material (hereinafter referred to as Butyl-6PW) having butyl group as a functional group of weak hydrophobicity. Similarly, a mixture of 20 g of G6000PW, 20 g of 1,4-dioxane and 1 g of 1,2-epoxyoctane was stirred and mixed for 6 hours at 45 °C to obtain a packing material (hereinafter referred to as Octyl-6PW) having octyl group as a functional group of strong hydrophobicity. Each packing material was packed into a stainless steel column with inner diameter of 7.5 mm and length of 7.5 cm. (2) Separation of a plasmid by hydrophobic interaction chromatography After Escherichia coli having pBR322 as a plasmid was cultured for 16 hours at 37 °C, the medium was subjected to centrifugal separation for 20 minutes at 4 °C and 8000 rpm. The precipitated Escherichia coli was suspended into 10 ml of 25 mM Tris hydrochloric acid buffer (pH 7.5) containing 100 mg of lysozyme, 50 mM glucose and 10 mM ethylenediamine-tetraacetic acid (hereinafter referred to as EDTA), which was stirred and then allowed to stand for 5 minutes at room temperature to dissolve cell wall. Then, 20 ml of 0.2N sodium hydroxide solution containing 1 % sodium dodecylsulfate were added thereto, and, after mixed gently, the mixture was allowed to stand for 10 minutes under cooling with ice to dissolve cytoplasmic membrane. Next, 15 ml of 3M sodium acetate buffer (pH 5.4) were added thereto, and the mixture was stirred slowly and allowed to stand for 30 minutes under cooling with ice. Then, after having been subjected to centrifugal separation for 20 minutes at 4 °C and 10000 rpm, the supernatant was collected to obtain a cleared lysate of Escherichia coli . After equal volume of 0.1M sodium phosphate buffer (pH 7.0) containing 4M ammonium sulfate was added to the crushed liquor of Escherichia coli , this mixture was subjected to a hydrophobic interaction chromatography. Into tandem columns of Butyl-6PW column and Octyl-6PW column linked in series, which were equilibrated with 0.1M sodium phosphate buffer (pH 7.0) containing 2M ammonium sulfate and 1 mM EDTA, 3 ml of the crushed liquor of Escherichia coli containing ammonium sulfate were injected, and then 0.1M sodium phosphate buffer (pH 7.0) containing 2M ammonium sulfate and 1 mM EDTA was fed into the tandem columns for 20 minutes at flow rate of 1 ml/min to elute the impure substances outside the columns. Following this, after having detached Butyl-6PW column outside the flow path system, 0.1M sodium phosphate buffer (pH 7.0) containing 1 mM EDTA was fed for 15 minutes at flow rate of 1 ml/min into only Octyl-6PW column. As a result, a chromatogram as shown in Fig. 1 was obtained. In Fig. 1, numeral 1 shows a peak of impurities and numeral 2 shows a peak of plasmid-containing fraction. The column eluate corresponding to the peak 2 was collected and purified further by means of ion exchange interaction chromatography as shown below. (3) Separation of a plasmid by a combined use of hydrophobic interaction chromatography and ion exchange chromatography As a packed column for the ion exchange chromatography, DEAE-5PW (trade name, from Tosoh Corp., inner diameter of 7.5 mm, length of 7.5 cm) was used. Into DEAE-5PW column equilibrated with 20 mM Tris hydrochloric acid buffer (pH 7.5) containing 0.6M sodium chloride and 1 mM EDTA, 3 ml of plasmid fraction was injected, and then 20 mM Tris hydrochloric acid buffer (pH 7.5) containing 0.6M sodium chloride and 1 mM EDTA was fed into the column for 35 minutes at flow rate of 1 ml/min to elute the impure substances outside the column. Then, the elution was conducted by a gradient method wherein the concentration of sodium chloride in 20 mM Tris hydrochloric acid buffer (pH 7.5) containing 1 mM EDTA was changed continuously from 0.6M to 0.8M over 30 minutes at flow rate of 1 ml/min. As a result, a chromatogram as shown in Fig. 2 was obtained. In Fig. 2, numeral 1 shows peaks of impurities and numeral 2 shows a peak of plasmid-containing fraction. The column eluate corresponding to the peak 2 was collected and the purity was examined by agarose gel electrophoresis. When dyeing the gel after the electrophoresis with ethidium bromide, electrophoretic images as shown in Fig. 3 were obtained. In Fig. 3, numeral 3 shows a DNA size marker, numeral 5 shows a plasmid fraction obtained by the present purifying method, and numeral 6 shows an electrophoretic image of commercial purified pBR322. As evident from the diagram, high-purity supercoil type plasmid could be obtained by simple manipulation according to the present purifying method. Comparative Example 1 For comparison, purification of a plasmid pBR322 was conducted from the cleared lysate of Escherichia coli by means of ion exchange interaction chromatography alone. After having prepared the cleared lysate of Escherichia coli similarly to the Example, equal volume of 20 mM Tris hydrochloric acid buffer (pH 7.5) was added thereto to make a sample for the ion exchange chromatography. Into the previous DEAE-5PW column equilibrated with 20 mM Tris hydrochloric acid buffer (pH 7.5) containing 0.6M sodium chloride and 1 mM EDTA, 3 ml of sample were injected, and then 20 mM Tris hydrochloric acid buffer (pH 7.5) containing 0.6M sodium chloride and 1 mM EDTA was fed into the column for 60 minutes at flow rate of 1 ml/min to elute the impure substances outside the column. Next, elution was conducted by the gradient method similarly to the Example. As a result, a chromatogram as shown in Fig. 4 was obtained. In Fig. 4, numeral 1 shows peaks of impurities and numeral 2 shows a peak of plasmid-containing fraction. The column effluent corresponding to the peak 2 was collected and the purity was examined by agarose gel electrophoresis. As a result, electrophoretic images as shown in Fig. 3 were obtained. In Fig. 3, numeral 3 shows a DNA size marker, numeral 4 shows a plasmid fraction obtained in the Comparative Example, numeral 5 shows a plasmid fraction obtained in the Example 1, and numeral 6 shows an electrophoretic image of commercial purified pBR322. Many impurities were contained in the plasmid fraction obtained by means of ion exchange chromatography alone. Example 2 (1) Preparation of packing materials for hydrophobic interaction chromatography Employing a packing material for gel filtration chromatography (G6000 PW (from Tosoh Corp.)) with average particle diameter of 20 µm and average pore diameter of 2000 angstroms as the base material, the packing material for the hydrophobic interaction chromatography was prepared. A mixture of 20 g of G6000 PW washed and substituted with 1,4-dioxane, 20 g of 1,4-dioxane, 1 g of 1,2-epoxyoctane and 0.5 ml of boron trifluoride as catalyst was stirred and mixed for 6 hours at 45 °C to obtain a packing material (hereinafter referred to as Octyl-6 PW) having octyl group for adsorbing plasmid and for hydrophobic interaction chromatography. Next, employing a packing material for gel filtration chromatography (G5000 PW (from Tosoh Corp.)) with average particle diameter of 20 µm and average pore diameter of 950 angstroms as the base material, a packing material with weak hydrohobicity was prepared. A mixture of 20 g of G5000 PW, 20 g of 1,4-dioxane, 1 g of 1,2-epoxybutane and 0.5 ml of boron trifluoride as catalyst was stirred and mixed for 6 hours and at 45 °C to obtain a packing material (hereinafter referred to as Butyl-5 PW) having butyl group for adsorbing RNAs and proteins and for hydrophobic interaction chromatography. Each packing material was packed into a stainless steel column with inner diameter of 7.5 mm and length of 7.5 cm. (2) Separation of a plasmid by a combined use of hydrophobic interaction chromatography and ion exchange chromatography - separation by hydrophobic interaction chromatography After Escherichia coli having pBR 322 as a plasmid was cultured for 16 hours at 37 °C, the medium was subjected to centrifugal separation for 20 minutes at 4 °C and 8000 rpm. The precipitated Escherichia coli was suspended into 10 ml of 25 mM Tris hydrochloric acid buffer (pH 7.5) containing 100 mg of lysozyme, 50 mM glucose and 10 mM ethylenediamine tetraacetate (hereinafter referred to as EDTA), which was stirred and then allowed to stand for 5 minutes at room temperature to dissolve cell wall. Then, 20 ml of 0.2N sodium hydroxide solution containing 1 % sodium dodecylsulfate were added thereto, after gentle mixing, the mixture was allowed to stand for 10 minutes under cooling with ice to dissolve cytoplasmic membrane. Next, 15 ml of 3M sodium acetate buffer (pH 5.4) were added thereto, and the mixture was stirred slowly and allowed to stand for 30 minutes under cooling with ice. Then, after being subjected to centrifugal separation for 20 minutes at 4 °C and 10000 rpm, the supernatant was collected to obtain a cleared lysate of Escherichia coli . After equal volume of 0.1M sodium phosphate buffer (pH 7.0) containing 4M ammonium sulfate was added to the cleared lysate of Escherichia coli , this mixture was subjected to a hydrophobic interaction chromatography. Into tandem columns of Butyl-5 PW column and Octyl-6 PW column linked in series, which were equilibrated with 0.1M sodium phosphate buffer (pH 7.0) containing 2M ammonium sulfate and 1 mM EDTA, 3 ml of the cleared lysate of Escherichia coli containing ammonium sulfate were injected, and then 0.1M sodium phosphate buffer (pH 7.0) containing 2M ammonium sulfate and 1 mM EDTA was applied into the tandem columns for 20 minutes at flow rate of 1 ml/min to elute the impure substances outside the columns. Following this, after having detached Butyl-5t PW column outside the flow path system, 0.1M sodium phosphate buffer (pH 7.0) containing 1 mM EDTA was fed into only Octyl-6 PW column for 15 minutes at flow rate 1 ml/min. As the result, chromatogram as shown in Fig. 5 was obtained. In Fig. 5, numeral 1 shows a peak of impurities and numeral 2 shows a peak of plasmid-containing fraction. The column effluent corresponding to the peak 2 was collected and purified further by means of ion exchange chromatography as shown below. (3) Preparation of a packing material for ion chromatography This was prepared by the way described below, employing a packing material (G6000 PW (from Tosoh Corp.)) for gel filtration chromatography with average particle diameter of 20 µm and average pore diameter of 2000 angstroms as base material. A mixture of 20 g of G6000 PW washed thoroughly with pure water, 40 g of pure water, 10 g of epichlorohydrin, 10 g of diethylaminoethanol and 5 g of NaOH was stirred and mixed for twenty-four hours at 40 °C to obtain anion exchanger (hereinafter referred to as DEAE-6 PW) having total ion-exchange capacity of 0.05 meq/ml-gel for purifying plasmid. This packing material was packed into a stainless steel column with inner diameter of 7.5 mm and length of 7.5 cm for ion-exchange chromatography. (4) Separation of a plasmid by a combined use of hydrophobic interaction chromatography and ion exchange chromatography After 3 ml of a plasmid fraction was injected into a DEAE-6 PW column equilibrated with 20 mM Tris hydrochloric acid buffer (pH 7.5) containing 0.6M sodium chloride and 1 mM EDTA, 20 mM Tris hydrochloric acid buffer (pH 7.5) containing 0.6M sodium chloride and 1 mM EDTA was fed into the column for 35 minutes at flow rate of 1 ml/min to elute impure substances outside the column. Then, the elution was conducted by a gradient method wherein the concentration of sodium chloride in 20 mM Tris hydrochloric buffer (pH 7.5) containing 1 mM EDTA was changed continuously from 0.6M to 0.8M over 30 minutes at flow rate of 1 ml/min. As a result, a chromatogram as shown in Fig. 6 was obtained. In Fig. 6, numeral 1 shows peaks of impurities and numeral 2 shows a peak of plasmid-containing fraction. The column effluent corresponding to the peak 2 was collected and the purity was examined by agarose gel electrophoresis. When dying the gel after the electrophoresis with ethidium bromide, a supercoil type plasmid of high purity could be obtained in the present Example. Comparative Example 2 For comparison, purification of a plasmid pBR 322 from the cleared lysate of Escherichia coli was conducted by ion-exchange chromatography alone. After the cleared lysate of Escherichia coli was prepared like as in Example 2, equal volume of 20 mM Tris hydrochloric acid buffer (pH 7.5) was added thereto to make a sample. Into the above-mentioned DEAE-6 PW column eguilibrated with 20 mM Tris hydrochloric acid buffer (pH 7.5) containing 0.6M sodium chloride and 1 mM EDTA, 3 ml of the sample were injected, and thereafter 20 mM Tris hydrochloric acid buffer (pH 7.5) containing 0.6M sodium chloride and 1 mM EDTA was fed into the column for 60 minutes at flow rate of 1 ml/min to elute impure substances outside the column. Then, the elution was carried out by the gradient method likewise as in Example. As the result, a chromatogram shown in Fig. 7 was obtained. In Fig. 7, numeral 1 shows peaks of impurities and numeral 2 shows a peak of fraction containing plasmid. The column effluent corresponding to the peak of numeral 2 was collected and the purity was examined by agarose-gel electrophoresis. As the result, the plasmid fraction obtained by ion-exchange chromatography alone was recognized to contain a lot of impurities. Example 3 Adsorption capacity of a plasmid Adsorption capacity of the packing material for hydrophobic interaction chromatography employed in Example 2, Octyl-6 PW was examined. Into a stainless steel column with inner diameter of 6.0 mm and length of 10 mm, the gel was packed and 0.1M sodium phosphate buffer (pH 7.0) containing 2.0M ammonium sulfate and 0.1 mM EDTA was fed thereinto for 20 minutes at flow rate of 0.64 ml/min to make the column equibrated. Then. about 0.4 mg/ml plasmid pUC 19 (2686 base pairs) of 4 ml was injected into the column and non-adsorption fraction which was not adsorbed onto the column was collected. Next, by changing the eluent to 0.1M sodium phosphate buffer (pH 7.0) containing 0.1 mM EDTA, plasmid adsorbed onto the column was eluted to collect the adsorption fraction. Following this, basing on the calibration curve of plasmid pUC 19 (an equation which shows the relationship between the injected quantity of plasmid pUC 19 and area of chromatograph) which was previously obtained by a gel filtration chromatography on TSK gel DNA-PW column (from Tosoh Corp.), the quantity of plasmid pUC 19 contained in every fraction was determined to calculate adsorption capacity per 1 ml of gel and recovery. With respect to the packing material for ion exchange chromatography, DEAE-6 PW, the adsorption capacity was likewise examined, too. Except adsorption and disorption eluents all of the others were conducted under the same condition. As the result, adsorption quantity of Octyl-6 PW was 1.1 mg/ml and adsorption quantity of DEAE-6 PW was 2.4 mg/ml. Further, recoveries thereof were 90.3 % and 77.3 %, respectively. Comparative Example 3 For comparison, a packing material of which pore diameter is smaller than that of Octyl-6 PW was prepared and the comparison of adsorption quantity was tested. The preparation was made by employing a packing material for gel filtration chromatography (G5000 PW (from Tosoh Corp.)) with average particle diameter of 20 µm and average pore diameter of 950 angstroms as a base material. A mixture of 20 g of G5000 PW, 20 g of 1,4-dioxane, 1 g of 1,2-epoxyoctane and 0.5 ml of boron trifluoride as catalyst were stirred and mixed for 6 hours at 45 °C to obtain Octyl-5 PW having octyl group. With respect to packing material for ion-exchange chromatography, commercially available DEAE-5 PW (average particle diameter of 20 µm, average pore diameter of 880 angstroms, from Tosoh Corp.) of which pore diameter is smaller than that of DEAE-6 PW was employed, too. The determination of adsorption capacity of plasmid was conducted likewise as in the above-mentioned Example. As a result, adsorption capacity of Octyl-5 PW was 0.6 mg/ml and adsorption capacity of DEAE-5 PW was 1.2 mg/ml. Recoveries thereof were 89.9 % and 60.6 %, respectively. As evident from the above results of Example 3 and Comparative Example, those having larger pore diameter can submit good results for long chain nucleic acids such as plasmid in both adsorption capacity and recovery.

Claims: A method for separating a plasmid from a solution containing the plasmid together with contaminants selected from the group consisting of proteins, RNAs, DNAs and mixtures thereof, using hydrophobic interaction chromatography comprising the steps of: (a) selecting a first column material for a first hydrophobic interaction chromatography having a functional group with a weaker hydrophobicity than a second column material to adsorb protein and RNA onto the first column material; (b) selecting a second column material for a second hydrophobic interaction chromatography having a functional group with a stronger hydrophobicity than the first column material to adsorb plasmid and DNA onto the second column material; (c) injecting the solution containing the plasmid and contaminants into a first column containing the first column material and collecting an eluate containing plasmide and DNA; (d) injecting the eluate containing plasmid and DNA from the first column into a second column containing the second column material; and (e) eluting the adsorbed plasmid from the second column material with an eluent containing salt of a concentration at which the plasmid is eluted from the second column material; whereby the functional groups to adsorb the nucleic acids are derived from one or more kinds of compounds selected from the group consisting of the following compounds (a) through (c) as major components in the column materials: Compound (a): compounds with long chained or branched, saturated hydrocarbon groups or unsaturated hydrocarbon groups with 2 to 20 carbon atoms whereby an aromatic ring may be contained in the hydrocarbon group; Compound (b): compounds represented by the following structural formula (1) wherein n = 0 to 20 and the alkylene group may be straight chained or branched, m = 0 to 3 and the hydrocarbon may be straight chained or branched, and A is a C=0 group or an ether group or is absent; Compound (c): an ether group of alkylene glycol with 2 to 20 carbon atoms which consists of 0 to 10 repeating units whereby at the opposite end the functional group reacted with the base material may be an OH group which may be capped with an alkyl group with 1 to 4 carbon atoms. A method for separating a plasmid from a solution containing the plasmid together with contaminants selected from the group consisting of proteins, RNAs, DNAs and mixtures thereof, using hydrophobic interaction chromatography comprising the steps of: (a) selecting a first column material for a first hydrophobic interaction chromatography having a functional group with a weaker hydrophobicity than a second column material to adsorb protein and RNA onto the first column material; (b) selecting a second column material for a second hydrophobic interaction chromatography having a functional group with a stronger hydrophobicity than the first column material to adsorb plasmid and DNA onto the second column material; (c) preparing a tandem column by connecting in series a first column containing the first column material to a second column containing the second column material; (d) injecting the solution containing the plasmid and contaminants into the tandem column; (e) breaking the connection between the first column and the second column; and (f) eluting the adsorbed plasmid from the second column material with an eluent containing salt of a concentration at which plasmid is eluted from the second column material; whereby the functional groups to adsorb the nucleic acids are derived from one or more kinds of compounds selected from the group consisting of the following compounds (a) through (c) as major components in the column materials: Compound (a): compounds with long chained or branched, saturated hydrocarbon groups or unsaturated hydrocarbon groups with 2 to 20 carbon atoms whereby an aromatic ring may be contained in the hydrocarbon group; Compound (b): compounds represented by the following structural formula (1) wherein n = 0 to 20 and the alkylene group may be straight chained or branched, m = 0 to 3 and the hydrocarbon may be straight chained or branched, and A is a C=0 group or an ether group or is absent; Compound (c): an ether group of alkylene glycol with 2 to 20 carbon atoms which consists of 0 to 10 repeating units whereby at the opposite end the functional group reacted with the base material may be an OH group which may be capped with an alkyl group with 1 to 4 carbon atoms. The method of claim 1 or 2 further comprising the use of ion exchange chromatography comprising the steps of: (i) injecting the eluate containing the plasmid from the second column into a column for ion exchange chromatography at a salt concentration at which the material for ion exchange chromatography adsorbs the plasmid; and (ii) eluting the adsorbed plasmid from the material for ion exchange chromatography with an eluent containing salt of a concentration at which the plasmid is eluted from the material for ion exchange chromatography. The method of any one of claims 1 to 3, wherein the average particle diameter of the material for hydrophobic interaction chromatography is 2 to 500 µm. The method of any one of claims 1 to 4, wherein the average pore diameter of the material for hydrophobic interaction chromatography is 500 to 4000 angstroms. The method of any one of claims 3 to 5, wherein the average particle diameter of the material for the ion exchange chromatography is 2 to 500 µm. The method of any one of claims 3 to 6, wherein the average pore diameter of the material for ion exchange chromatography is 1500 to 4000 angstroms.

Inventors: KITAMURA TAKISHI, NAKATANI SHIGERU, KITAMURA, TAKISHI, NAKATANI, SHIGERU
Applicants: TOSOH CORP, TOSOH CORPORATION
Application year: 1999
Main classification: C12N15
IPC codes: C12N15