LIQUID CHROMATOGRAPHY USING MICROPOROUS HOLLOW FIBERS

Abstract: Liquid chromatography separations of solutes are achieved using porous hollow fibers. The pores of the hollow fibers immobilize a solute-absorbing phase (preferably organic) which has a greater absorbance affinity towards at least one solute in a mixture of solutes. By passing the solute mixture through the central lumen of the hollow fibers, chromatographic separations are realized due to the greater retention time of that solute with which the immobilized phase has greater absorbance affinity. The immobilized phase may be a liquid organic which may contain a surfactant so as to form reversed micelles or it may be in the form of a polymeric gel. Separations of biological species (e.g., proteins) may thus be accomplished by means of the present invention.

Description: FIELD OF THE INVENTION The present invention relates to liquid chromatography. In specific embodiments, the invention relates to novel methods which effect liquid chromatography using microporous hollow fibers. BACKGROUND OF THE INVENTION High performance liquid chromatography is a well known method of separating solute species in dependence upon the differential absorption/desorption between different solute species. Typically, a liquid carrier (in which the solute species to be separated are present) is passed through a column packed with separation media (e.g., solid or gel particles). This separation media, in effect, increases the residence time of one (or more) solute species in the liquid carrier (which is inert to the solute species) relative to one (or more) other solute species in the liquid carrier (i.e., due to the greater rate of absorption/desorption of the one solute species relative to the other solute species). Due to the increased residence time of the one solute species in the column, there will be a time when an essentially pure mixture of carrier liquid and the other solute species will be present at the discharge of the column -- that is, the one and other solute species will be separated. With the recent advent of commercial manufacture of biological species (e.g., proteins), however, the conventional liquid chromatography technique of using packed particle beds has proven to be an inefficient means of separating one species from another with high resolution. This inability of packed particle chromatography columns can be attributed generally to the high pressure drops which are experienced and which lead to lesser flow rates of the liquid carrier through the column (thereby leading to lesser rate of production of the desired biological species). In addition, the very stringent control over particle size, the uniformity of the particles and the manner in which such particles fill the column contribute to increased costs which, in general, cannot be tolerated on a commercial scale. Hence, the conventional packed particle technique for liquid chromatography, while being adequate for analytical purposes on a small scale, is inadequate for separating solute species (particularly biological species) on a commercial scale. Recently, it has been proposed to employ hollow fibers for liquid chromatography. The geometry of such hollow fibers provides an attractive alternative to particles in terms of lesser pressure drop through the column, and the lower cost of hollow fibers (relative to uniform particles) which provides attractive economies of scale and thus may allow commercially viable liquid chromatography systems to be achieved. One prior proposal in this regard employs a tube packed to between 60 and 100 percent of the tube's theoretical packing density with generally parallel aligned fibers so as to provide the means to perform liquid chromatography. See, U.S.-A-4,657,742. The fibers in U.S.-A-4,657,742 are preferably glass fibers which may be solid or they may be solid fibers that have been rendered porous. Alternatively, the fibers may be hollow fibers having solid walls or hollow fibers whose walls have been treated so as to render them porous. The process for packing the tube with a high density of fibers is also said to be applicable to fibers other than glass, for example, cellulosic and organic fibers (see column 10, lines 10-13 of US-A-4,657,742). In JP-A-55018244, there is disclosed a hollow fiber which is suitable for use in liquid chromatography. The hollow fiber disclosed therein includes an external liquid-impermeable skin layer and an internal (i.e., adjacent the lumen of the fiber) porous layer. The liquid-impermeable layer apparently allows liquid chromatography to proceed with increased pressure within the internal lumen of the fiber without carrier liquid "breakthrough" to the external side of the fiber. US-A-3,570,673 discloses a method of producing a separation column for use in liquid chromatography wherein a bundle of parallel fibers, in particular inorganic fibers such as glass fibers, is inserted into a tube of chemically resistant material, the tube is shrunk securely onto the bundle of fibers, and a solvent is then forced through the bundle of fibers to remove a soluble phase of the fibers and to obtain a porous fibrous body. The fibers may be surface-modified, e.g. by means of a trimethylchlorosilane or carbon coating. Summary of the Invention While the above-mentioned proposals for liquid chromatography may provide some improvement over the conventional packed particle columns used in liquid chromatography applications, there still exists a need in this art for greater solute separation resolution on a commercially viable scale -- that is a liquid chromatography system which is adapted to separate a greater amount of solute species per unit time as compared to conventional liquid chromatography techniques. It is towards achieving such needed improvements that the present invention is directed. According to the present invention, microporous hollow fibers (preferably polyolefinic fibers which are normally hydrophobic) are employed as the means to immobilize, within the micropores of the fiber, a stationary phase having a greater affinity to at least temporarily absorb at least one solute species relative to at least one other solute species. Thus, when a liquid carrier containing the solute species to be separated is passed through the central lumen of the hollow fiber, at least one of the solute species will have a greater residence time within the hollow fiber (i.e., due to its affinity to be at least temporarily absorbed by the immobilized phase within the fiber's micropores), thereby causing the solute species to be separated at the outlet end of the fiber -- that is, the solute species with which the immobilized phase has a lesser affinity for absorption will appear in essentially "pure" form (but carried by the carrier liquid) before the solute species with which the immobilized phase has a greater absorption affinity. In one aspect, the present invention provides a liquid chromatography method for separating at least solute species A and B comprising the steps of: (a) immobilizing, within pores of a number of open celled, microporous hollow fibers having an average pore size of less than 500 nm (5,000 Å), an inner diameter of from about 5 to about 1500 µm (microns), a coefficient of variation in inner diameter of less than about 8%, and an average ratio of maximum pore density around the circumference of the fiber of less than about 3:1, by uniformly wetting each of said microporous hollow fibers therewith, a solute-absorbing phase having a greater affinity for absorbing/desorbing solute species A as compared to solute species B; (b) passing a carrier liquid stream through the lumens of said microporous hollow fibers; and then (c) injecting a sample mixture comprised of solute species A and B into said carrier liquid stream so that a liquid mixture comprised of said carrier liquid and said solute species A and B passes through the lumens of said hollow fibres; (d) allowing said solute species A to be absorbed preferentially by said immobilised solute-absorbing phase so that a first mixture comprised essentially of the carrier liquid and solute species B is initially discharged from said hollow fiber lumens; and then (e) allowing the solute species A to desorb into said carrier stream so as to form a second mixture comprised essentially of the carrier liquid and the solute species A which is discharged from said hollow fiber lumens subsequent to the discharge of said first mixture comprised essentially of the carrier liquid and solute species B, whereby solute species A and B are separated from said sample mixture thereof. Preferably, the immobilised phase within the fiber's micropores is organic since it more easily "wets" the normally hydrophobic hollow fibers (i.e., so that the organic phase fills completely the micropores of the hollow fiber). The immobilised phase may thus be an organic liquid or a gel, with the particular chemical composition of the immobilised phase being selected in dependence upon a number of factors, including its compatibility with the material of the hollow fiber and/or its compatibility with the solutes to be separated, and/or its absorption/desorption affinity for particular solute species of interest to be separated. In a further aspect, the present invention provides a process for separating at least one biological species from another biological species, comprising the steps of: (a) immobilising, within the micropores of a number of open-celled microporous hollow fibers having an average pore size of less than 500 nm (5,000 Å), an inner diameter of from about 5 to about 1500 µm (microns), a coefficient of variation in inner diameter of less than about 8%, and an average ratio of maximum pore density to minimum pore density around the circumference of the fiber of less than about 3:1, by uniformly wetting each of said microporous hollow fibers therewith, an organic phase which includes a surfactant capable of forming reversed micelles within said organic phase; (b) buffering an aqueous phase comprised of a mixture of one and another biological species to an initial pH whereby one of said biological species exhibits a negative charge and said another biological species exhibits a positive charge; (c) passing said buffered aqueous phase through lumens of said hollow fibers and allowing essentially all of said one biological species to be absorbed within said reversed micelles of said immobilised phase while said another biological species passes on to an outlet end of said hollow fibers so that a stream comprised essentially of all said another biological species is discharged from said outlet end of said hollow fibers, whereby said one and another biological species are separated; and then subsequently (d) eluting said absorbed one biological species after said another biological species has been discharged from said outlet end of said hollow fibers, said step of eluting said absorbed one biological species including the steps of: (i) buffering a carrier liquid to a pH different from said initial pH of said aqueous phase and to a pH which is sufficient to effect a charge reversal of said one biological species from a negative charge to a positive charge; and then (ii) passing the buffered carrier liquid through said lumens of said hollow fibers to effect said charge reversal of said one biological species and to thereby cause said one biological species to be eluted from said micropores into said carrier liquid. Therefore, according to the present invention, a commercially viable alternative to prior liquid chromatography techniques is provided. This advantage, as well as others, will become more clear after careful consideration is given to the following detailed description of the preferred exemplary embodiments thereof. BRIEF DESCRIPTION OF THE ACCOMPANYING DRAWINGS Reference will hereinafter be made to the accompanying drawings wherein like reference numerals throughout the various FIGURES denote like structural elements, and wherein; FIGURE 1 is a schematic view of a liquid chromatography system utilized in the Examples below; FIGURE 2 is a representative plot of absorbance versus time showing the separation resolution achieved according to EXAMPLE I below; FIGURE 3 is a plot of absorbance versus time for the same solutes shown in FIGURE 2 but without using an organic phase immobilized in the micropores of the hollow fiber (i.e., according to EXAMPLE III, below); FIGURE 4 is a plot of absorbance versus time for separation attained according to EXAMPLE IV below; and FIGURE 5 is a plot of absorbance versus time for the separation attained according to EXAMPLE V below. DETAIL DESCRIPTION OF THE PREFERRED EXEMPLARY EMBODIMENTS The novel liquid chromatographic columns of the present invention include a number of microporous hollow fibers. Although any suitable microporous hollow fiber may be employed in the practice of this invention, it is presently preferred to use microporous, normally hydrophobic polyolefin (e.g., polypropylene or polyethylene) hollow fibers arranged generally parallel to one another in a closely packed relationship within an outer shell structure. The preferred hollow fibers employed in this invention are those of the type made using the "up-spinning" technique disclosed in U.S.-A-4,405,688 and US-A-4,451,981. Briefly, non-porous precursor hollow fibers are produced according to the techniques disclosed in these prior patents by melt spinning the precursor fibers in a substantially vertically upward direction (i.e., up-spinning). The thus melt spun hollow precursor fibers are then spin-oriented while subjecting them to a symmetrical quenching step using a hollow annular structure surrounding the precursor fiber which has one or more openings on its inner surface that distribute the quenching medium against the precursor fiber in a substantially uniform manner. The thus formed hollow precursor fiber may then be heat annealed by, for example, subjecting the non-porous precursor hollow fiber to a temperature of between about 5°C to 100°C for a time period of at least a few seconds (e.g., from a few seconds up to about 24 hours, preferably between about 30 minutes to about 2 hours). The finished microporous hollow fibers will possess an average inner diameter in the range of from about 5 to about 1500 µm (microns), and preferably in the range of from about 70 to about 1500 µm (microns). The fibers are moreover characterized by a substantially uniform internal diameter (I.D.), for example, a coefficient of variation in inner diameter through a cross-section taken perpendicular to the axis of the fiber of less than about 8%, preferably less than about 5%, and more preferably less than about 3%. The pores of the preferred microporous hollow fibers are essentially interconnected through tortuous paths which may extend from one exterior surface or surface region to another, i.e., open-celled. Further, the pores of the preferred microporous hollow fibers of the present invention are microscopic, i.e., the details of the pore configuration or arrangement are described only in terms of microscopic dimensions. Thus, the open cells or pores in the fibers are smaller than those which can be measured using an ordinary light microscope, because the wavelength of visible light, which is about 500 nm (5,000 Angstroms), is longer than the longest planar or surface dimension of the open cell or pore. The pore size of the microporous hollow fibers may be defined by using electron microscopy techniques which are capable of resolving details of pore structure below 500 nm (5,000 Angstroms) or by mercury porosimetry techniques. The average effective pore size of the microporous hollow fibers useable in the practice of this invention is preferably between 5 to 200 nm (50 to 2000 Angstroms), and more typically between 10 to 100 nm (100 to 1000 Angstroms). By "average effective pore size" is meant the smallest dimension of a pore which would allow a generally spherical particle of that same dimension to pads therethrough. The pores generally have an elongated shape with a width of from 5 to 200 nm (50 to 2000 Angstroms), and a length of from 50 to 1000 nm (500 to 10,000 Angstroms). Hence, the "average effective pore size" of the preferred microporous hollow fibers will usually be determined by the width dimension of the pores. These pores will, moreover, be fairly uniform around the circumference of the fiber. For example, the preferred microporous hollow fibers will exhibit an average ratio of the maximum pore density to the minimum pore density around the circumference of the fiber of less than about 3:1, and usually less than about 2:1. Microporous hollow fibers of the type described above are commercially available from Hoechst Celanese Corporation, Separations Products Division, Charlotte, North Carolina under the registered trademark CELGARD®. The microporous hollow fibers are preferably a part of a module having an inlet end and an outlet end. The module includes a number (e.g., from a few hundred to many thousand) of hollow fibers of predetermined length arranged substantially parallel to one another within the central space of a generally tubular shell structure (e.g., glass or metal tubes). The individual fibers are positionally retained within the outer shell structure by means of suitable potting compounds (e.g., epoxy resins). Modules of this type are commercially available in a wide range of sizes and capacities. For example, one particular microporous hollow fiber module which may be satisfactorily employed in the practice of the present invention is commercially available from Hoechst Celanese Corporation, Separations Products Division, Catalog No. 50101060. This module has 27,000 CELGARD® microporous hollow fibers of 100µm internal diameter. Other suitable microporous hollow fiber modules may, however, be used for the chromatographic separations according to the present invention. The phase that is immobilized within the micropores of the hollow fibers is preferably organic and can be either a liquid or a solid (e.g., a polymeric gel). The selection of any particular immobilized phase depends upon a number of factors including the particular solute(s) to be separated, its pH dependency, and/or its compatibility and wettability with respect to the microporous hollow fibers in the chromatographic module. Important to the present invention is that the immobilized phase be selected so that it exhibits a greater absorption affinity towards at least one solute species as compared to its absorption affinity towards at least one other solute species. That is, the immobilized phase must have a differential partition coefficient "K" as between one and another of the solute species intended to be separated. In this regard, refer to Skoog et al, "Fundamentals of Analytical Chemistry", pages 639-671 (1976). The immobilized phase is most preferably an organic liquid. Virtually any suitable organic liquid may be employed in the practice of this invention, the selection of any particular organic liquid again depending upon at least some of the factors enumerated above. For example, when employing polypropylene microporous hollow fibers, the organic liquid is one which is capable of "wetting the fiber. Such organic liquids will preferably be water immiscible and/or will exhibit surface tension of less than about 50 dynes/cm, (50 mN/m), and more preferably less than about 35 dynes/cm (35 mN/m). By way of example only, organic liquids which may be employed in the practice of the present invention includes aldehydes, ketones (e.g., methyl ethyl ketone, methyl isobutyl ketone, methyl cyclohexanone, dimethyl cyclohexanone), esters (e.g., cyclohexyl acetate, furfuryl acetate, amyl acetate), ethers (e.g., 2-chloro-2-methoxy diethyl ether, diisopropyl ether), aliphatic and aromatic hydrocarbons (e.g., hexane, dodecane, and benzene, toluene, respectively), organic alcohols (e.g., iso-butanol, butanol-pentanol, octanol, dodecanol, methyl cyclohexanol, 2-ethyl bexanol), and carboxylic acids (e.g., octanoic acid, naphthenic acids). Other organic liquids may also be employed, such as, tributyl phosphate, trioctyl phosphate, trioctyl phosphine oxide, phosphonic acid esters, dimethyl phthalate, diethyl oxalate, aryl sulfonic acids, hydroxyoximes, oxine derivatives, β-diketones, alkarylsulfonamides, and primary, secondary, tertiary and quartenary amines, to name just a few. When used to separate biological species, for example proteins, the immobilized liquid organic phase most preferably includes nanometer scale droplets of an aqueous solution stabilized in an apolar environment by the presence of surfactant at the interface -- that is, so-called "reverse micelles". In this regard, see Goklen et al, "Protein Extraction Using Reverse Micelles", Biotechnology Progress, Vol. 1, No. 1, pp. 69-74 (March, 1985) and Goklen et al, "Liquid-Liquid Extraction of Low Molecular-Weight Proteins by Selective Solubilization in Reversed Micelles", Separation Science and Technology, 22(2&3), pp. 831-841 (1987). These reverse micelles exhibit a certain electrostatic charge which is pH dependent (i.e., changes with a change in pH) and which can therefore be utilized to solubilize a protein of an opposite charge. In the context of the present invention therefore, when the solutes to be separated are proteins and the immobilized organic phase within the micropores of the hollow fiber include such reverse micelles, the pH of the mobile phase is selected so that the reverse micelle will solubilize a particular protein of different electrostatic charge. After the other protein of substantially like electrostatic charge has been separated (i.e., since it is not solubilized by means of the reverse micelles), the solubilized protein can be eluted by changing the pH of the mobile phase (which will affect the electrostatic charge of the reverse micelle). Any surfactant capable of forming reversed micelles in a apolar environment may be used in the practice of this invention. Preferably, the surfactant will be di-dodecylsulfosuccinate (Aerosol-OT), or a cationic amine, for example, hexadecyltributyl ammonium chloride. When organic liquids are employed as the immobilized phase according to the present invention, the micropores of the hollow fibers are most conveniently filled by placing a small volume of the organic liquid at the top of a column containing a number of hollow fibers and allowing this liquid to wick into the fibers thereby wetting the same (i.e., filling the micropores). It is important that all of the microporous fibers in the module be wet evenly with the organic liquid. When using normally hydrophobic microporous hollow fibers of polyolefin (e.g., polypropylene) as above described, the appearance of the fibers will change from a characteristic normal opaque to translucent when wet with the organic liquid. The presence of unfilled micropores in the hollow fiber is therefore readily determined visually by inspecting the fibers for opaque regions surrounded by translucent regions. In order to be usable in the practice of the present invention, all of the fibers in the module must be translucent indicating that all micropores have been uniformly filled. Another class of organic phases which may be immobilized in the micropores of the hollow fiber are so-called polymeric gels modified with affinity ligands. The polymeric gels may, for example, be polyacrylamide, cross-linked polystyrene, starch (e.g., aqueous Dextrin commercially available from Sephadex Corporation and Pharmacia Corporation), or cross-linked silanes, with polyacrylamide being presently preferred. When employing polyacrylamide as the immobilized gel phase within the micropores of the hollow fibers, it is preferred to wet the fiber (i.e., fill the micropores) with a liquid acrylamide monomer, modified to take affinity ligands, in a manner similar to that described above with respect to other liquid organics. Liquid acrylamide monomers so modified are very well known in and of themselves and are available from a number of commercial sources, for example, from Pharmacia and Biorad Corporations. The selection of any particular acrylamide monomer (i.e., one having particular affinity ligands) that is employed in the practice of the present invention will, of course, depend to a large extent upon the particular solute species intended to be separated. Suffice it to say here, that those skilled in this art are entirely capable of selecting any particular acarylamide monomer with an affinity ligand suitable to achieve separation of solute species of particular interest. When the acrylamide monomer has been immobilized within the hollow fiber micropores, polymerization of the acrylamide monomer may then be accomplished in situ. Once the organic liquid or gel has been immobilized within the micropores of the hollow fiber, chromatographic separations can then be accomplished, for example, using the system 10 shown in accompanying FIGURE 1. As is seen, the system 10 includes a solvent reservoir 12 which contains pure liquid solvent. For most solutes, an aqueous solution is employed for the solvent. The solvent is pumped from the reservoir 12 via a suitable pump 14, through an injector valve 16 into the inlet of a hollow fiber module 18 as above described. The solute species may thus be injected at time t₀ into a stream of pure solvent via the injector valve 16 and travel on to the inlet of the hollow fiber module 18. The stream exiting the module 18 at time t₁ later than time t₀ may be analyzed via any suitable analytical instrument, for example, an ultraviolet visible detector 20 which outputs signals to a suitable microprocessor 22 so as to generate graphs and/or otherwise put the collected data in human-readable form. Thereafter the stream may be passed to a collection site for collecting the separated solutes for further processing and/or purification (i.e., solvent removal). The invention will be further described by way of the following Examples which are intended to be illustrative only and non-limiting. EXAMPLE I An aqueous solution of solutes 2-butanone, 2-pentanone, 2-hexanone, and 2-heptanone in equal amounts was injected into a microporous hollow fiber module wherein the fibers were wet with a solution of 50% trioctylphosphate/50% dodecane. The module contained 420 microporous polypropylene hollow fibers (CELGARD®), each 60 cm long having an internal diameter of 100µm and a wall thickness of 30µm. Accompanying FIGURE 2 shows the results of the chromatographic separation of the solutes. EXAMPLE IIA Example 1 was repeated using a module having 420 microporous polypropylene hollow fibers, each 60cm in length and an internal diameter of 100µm. The solutes employed in this EXAMPLE II were 2-butanone, methyl-i-butanone 2-pentanone, cyclohexanone, 2-heptanone, and 4-heptanone with the immobilized phase being 50% trioctylphosphate/50% dodecane. The results appear below in Table A. Column Solute length/velocity (l /v,sec ) residence time (t R ,sec) band width (V²,sec²) 60 cm/420/TOP 2-Butanone 29.8 74.6 1,170 Methyl-i-Butanone 29.8 166.0 3,390 2-Pentanone 29.8 176.0 3,700 Cyclohexanone 29.8 139.0 3,300 2-Heptanone 29.8 2200.0 354,000 4-Heptanone 29.8 2410.0 460,000 The above data in Table A demonstrate that mixed solutes can be successfully separated by liquid chromatography in microporous hollow fibers having a liquid organic phase immobilized within the micropores thereof. EXAMPLE IIB Example IIA was repeated using the columns and solutes identified in Table B, below. As can be seen from the data of Table B, effective solute separations are possible. Column Solute length/velocity (l /v,sec ) residence time (t R ,sec) band width (V²,sec²) 61 cm/480/12 OH m-Nitrophenol 37.0 952.0 121,000 " 88.8 2330.0 44,300 p-Nitrophenol 65.8 1430.0 322,000 " 140.0 3290.0 899,000 Uracil 32.1 43.4 37 " 210.0 288.0 2,160 21 cm/480/12 OH m-Nitrophenol 10.3 250 14,900 " 43.8 1070 104,000 4-Heptanone 10.9 426 27,700 " 273.0 10,400 4.23 x 10⁶ 2-Pentanone 30.0 106 4,600 " 97.6 343 23,400 " 167.0 614 68,230 Phenol 17.6 100 7,020 " 25.5 139 8,290 " 75.5 437 48,900 o-Nitrophenol 29.7 20.4 14 " 118.0 79.4 157 EXAMPLE III (COMPARATIVE) Example I was repeated except that a liquid organic phase was not present in the micropores of the hollow fibers. Thus, the microporous hollow fibers employed in this EXAMPLE III did not have an immobilized phase within the fibers' micropores. The results appear in the graph of FIGURE 3. It will immediately be apparent from FIGURE 3 that no separation of the solute species occurred (i.e., since only a single peak is present). Note also the different time scale as between FIGURES 2 and 3, the latter being significantly shorter than that employed in the former. Hence, on the same time scale as that employed in FIGURE 2, the solutes would appear in FIGURE 3 as a sharp peak near the y-axis. This data indicates that the "empty" micropores were incapable of separating the solutes one from another. EXAMPLE IV The efficacy of liquid chromatography using an immobilized organic solution of reversed micelles was examined. This EXAMPLE IV employed a module 60 cm in length, containing 480 microporous polypropylene hollow fibers (CELGARD®) of 100µm internal diameter. The mobile phase consisted of an aqueous solution of the proteins myoglobin and cytochrome-c in equal masses buffered at a pH of 6. The immobilized phase consisted of dodecane as the solvent and sodium di-dodecylsulfosuccinate as the reverse micelle-forming surfactant. The mobile aqueous phase containing the proteins and buffered at a pH of 6 was injected into an aqueous stream which passed through the central lumens of the hollow microporous fibers in the module. At a pH of 6, the cytochrome-c exhibits a positive charge and was therefore retained in the micelles in the immobilized organic phase. The myoglobin, of negative charge at pH of 6, passed through the module at the mean residence time of the mobile phase. After the myglobin had passed through the module, the pH of the mobile phase was changed to 10. At this higher pH, the cytochrome-c has a negative charge, causing it to be eluted from the module. Thus, a high resolution separation occurred as between the cytochrome-c and the myoglobin as is shown in FIGURE 4. EXAMPLE V EXAMPLE IV was repeated, except that a larger commercial scale module (Catalog No. 50101060, Hoechst Celanese Corporation, Separations Products Division, Charlotte, North Carolina) was employed. The module used in this EXAMPLE V was 22 cm long, and contained 27,000 microporous hollow fibers (CELGARD®) of 100µm internal diameter. The results of the chromatographic separation achieved by this EXAMPLE V are shown in FIGURE 5. The above Examples demonstrate that the present invention achieves solute separation using microporous hollow fibers. Moreover, as Example V shows, the present invention can be "scaled-up" to provide a viable technique for separating commercially important solute species.

Claims: A liquid chromatography method for separating at least solute species A and B comprising the steps of: (a) immobilizing, within pores of a number of open celled, microporous hollow fibers having an average pore size of less than 500 nm (5,000 Å), an inner diameter of from about 5 to about 1500 µm (microns), a coefficient of variation in inner diameter of less than about 8%, and an average ratio of maximum pore density to minimum pore density around the circumference of the fiber of less than about 3:1, by uniformly wetting each of said microporous hollow fibers therewith, a solute-absorbing phase having a greater affinity for absorbing/desorbing solute species A as compared to solute species B; (b) passing a carrier liquid stream through the lumens of said microporous hollow fibers; and then (c) injecting a sample mixture comprised of solute species A and B into said carrier liquid stream so that a liquid mixture comprised of said carrier liquid and said solute species A and B passes through the lumens of said hollow fibres; (d) allowing said solute species A to be absorbed preferentially by said immobilised solute-absorbing phase so that a first mixture comprised essentially of the carrier liquid and solute species B is initially discharged from said hollow fiber lumens; and then (e) allowing the solute species A to desorb into said carrier stream so as to form a second mixture comprised essentially of the carrier liquid and the solute species A which is discharged from said hollow fiber lumens subsequent to the discharge of said first mixture comprised essentially of the carrier liquid and solute species B, whereby solute species A and B are separated from said sample mixture thereof. A method according to claim 1, wherein said solute-absorbing phase is organic and said carrier liquid is aqueous. A method according to claim 2, wherein said immobilized organic phase is liquid. A method according to claim 2, wherein said immobilised organic phase is a polymeric gel. A method according to claim 4, wherein said polymeric gel is selected from the group consisting of polyacrylamide, polystyrene, starch, and cross-linked silanes. A method according to any of claims 1 to 5, wherein said average pore size of said microporous hollow fiber is between 5 to 200 nm (50 to 2,000 Angstroms). A method according to any of claims 1 to 6, wherein said microporous hollow fiber has a coefficient of variation in inner diameter of less than about 5%. A method according to any of claims 1 to 7 comprising the further step of providing a liquid chromatography module having an inlet and an outlet, and a number of microporous hollow fibers arranged within said module generally parallel to one another between said module inlet and outlet, and wherein the central lumens of said hollow fibers establish fluid communication between said module inlet and outlet. A process for separating at least one biological species from another biological species, comprising the steps of: (a) immobilising, within the micropores of a number of open-celled microporous hollow fibers having an average pore size of less than 500 nm (5,000 Å), an inner diameter of from about 5 to about 1500 µm (microns), a coefficient of variation in inner diameter of less than about 8%, and an average ratio of maximum pore density to minimum pore density around the circumference of the fiber of less than about 3:1, by uniformly wetting each of said microporous hollow fibers therewith, an organic phase which includes a surfactant capable of forming reversed micelles within said organic phase; (b) buffering an aqueous phase comprised of a mixture of one and another biological species to an initial pH whereby one of said biological species exhibits a negative charge and said another biological species exhibits a positive charge; (c) passing said buffered aqueous phase through lumens of said hollow fibers and allowing essentially all of said one biological species to be absorbed within said reversed micelles of said immobilised phase while said another biological species passes on to an outlet end of said hollow fibers so that a stream comprised essentially of all said another biological species is discharged from said outlet end of said hollow fibers, whereby said one and another biological species are separated; and then subsequently (d) eluting said absorbed one biological species after said another biological species has been discharged from said outlet end of said hollow fibers, said step of eluting said absorbed one biological species including the steps of: (i) buffering a carrier liquid to a pH different from said initial pH of said aqueous phase and to a pH which is sufficient to effect a charge reversal of said one biological species from a negative charge to a positive charge; and then (ii) passing the buffered carrier liquid through said lumens of said hollow fibers to effect said charge reversal of said one biological species and to thereby cause said one biological species to be eluted from said micropores into said carrier liquid. A process according to claim 9, wherein each of said one and other biological species is a protein. A process according to claim 9 comprising the further step of immobilising a polymeric gel modified to take affinity ligands in the pores of a number of porous hollow fibers by (i) filling said hollow fiber pores with a liquid monomer of said polymeric gel, and then (ii) polymerising said monomer in situ within said pores of said hollow fibers. A process according to claim 11, wherein said monomer is a liquid acrylamide modified to take affinity ligands.

Inventors: CUSSLER, EDWARD L.
Applicants: HOECHST CELANESE CORPORATION
Application year: 1989
Main classification: B01D15
IPC codes: B01D15, G01N30, B01J20, B01D69