Planetary Countercurrent Chromatography Centrifuge and Mixer-Settler Rotor
20190015761 ยท 2019-01-17
Inventors
Cpc classification
B01D15/1892
PERFORMING OPERATIONS; TRANSPORTING
B01D15/1807
PERFORMING OPERATIONS; TRANSPORTING
B01D15/22
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01D15/22
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A mixer-settler countercurrent chromatography centrifuge and rotor of increased capacity is described.
Claims
1. A planetary countercurrent chromatography centrifuge comprising: 1) vertical solar and planetary shafts with a revolution radius of at least 13 cm; and 2) a rotor of at least 22 cm outer diameter comprising a plurality of disks, each disc comprising a channel comprising a device to impede flow, and gaskets, wherein said disks and said gaskets comprise a central void not in contact with said shafts, and each disc comprises a gasket thereon.
2. The centrifuge of claim 1 wherein said shafts comprise a sealed bearing.
3. The centrifuge of claim 1 wherein said shafts comprise a terminal flared portion.
4. The centrifuge of claim 1, comprising at least six disks.
5. The centrifuge of claim 1, comprising at least eight discs.
6. The centrifuge of claim 1 wherein said discs comprise a raised lip about an outer edge of said disk.
7. The centrifuge of claim 1 wherein said discs comprise a raised lip about an inner edge of said disk.
8. The centrifuge of claim 6 wherein said gaskets seat within said raised lip.
9. The centrifuge of claim 7 wherein said gaskets seat within said raised lip.
10. The centrifuge of claim 1 wherein said rotor comprises ribbed endplates.
11. The centrifuge of claim 1 wherein said rotor comprises a tubing protector.
12. The centrifuge of claim 11 wherein said tubing protector comprises a sleeve.
13. The centrifuge of claim 12 wherein said sleeve is corrugated.
14. The centrifuge of claim 11 wherein said tubing protector comprises a foam, a sponge or a hydrogel.
Description
BRIEF DESCRIPTION OF THE FIGURES
[0028] The following description of the figures and the respective drawings are non-limiting examples that depict various embodiments that exemplify a present invention.
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DETAILED DESCRIPTION OF THE INVENTION
[0043] As used herein, a superior or top face of a disc comprises the spirals, channels, grooves of interest for comprising the stationary and mobile phases for separation.
[0044] An inferior or bottom face of a disc does not comprise the spirals, channels, grooves of interest, but may contain a hole or a void, a rim, a border, a partition and so on. Separation of reagents or analytes does not occur on an inferior or bottom face of a disc.
[0045] A rotor of interest is generally cylindrical or circular in shape with an increased approximate diameter of at least about 22 cm, at least about 24 cm, at least about 26 cm, at least about 28 cm, or larger, such as, 22.5 cm, 23 cm, 25 cm and so on, and a height of at least about 10 cm, at least about 11 cm, at least about 12 cm, at least about 13 cm, or taller, as compared to existing rotors with an outer diameter (OD) of 17.5 cm and a height or 5 cm.
[0046] An accommodating centrifuge can have a revolution radius (distance between the solar axis and the planetary axis) increased from about 10 cm to about 13 cm. The revolution radius can be at least about 13 cm, at least about 14 cm, at least about 15 cm, at least about 16 cm, or greater.
[0047] A centrifuge of interest can be operated at higher speeds, for example, at least about 1000 rpm, at least about 1100 rpm, at least about 1200 rpm, at least about 1300 rpm or higher speeds.
[0048] With the revolution radius incrementally increased from about 10 cm to about 13 cm, with a concomitant increase in disc size of about 5 cm in diameter, from 17.5 cm to about 22.5 cm, and speed increased from 840 rpm to 1200 rpm, the relative centrifugal field (a function of revolution radius and speed) was increased from x79 g to x209 g, a greater than 2.5 increase. RCF can be increased 2, 2.25, 2.75, 3, 3.5, 4 or more.
[0049] Relative centrifugal field (RCF) can be calculated using the formula, RCF=11.17r(RPM/1000).sup.2, where r is the revolution radius in centimeters.
[0050]
[0051] In channels (also used interchangeably herein with, grooves, slots, slits, and spirals,) are impediments to flow, such as, protrusions, such as, pins or partial walls, glass beads, barrier and so on, generally, that do not touch either side of a groove or channel wall, generally do not contact a gasket above a disc to enable gasket expansion and/or deformation. Not wishing to be bound by speculation or theory, it is believed flow impediments impact flow of phases, such as, upper phase (UP) close to the center of a channel and lower phase (LP) on sides of an impediment outward from the center. SP gets, retained, in settling sections that do not have an impediment, as depicted in
[0052] A feature of planetary motion is no tangling or twisting of tubing that enters and exits the planetary rotor. Nonetheless, with solar and planetary motions, with speeds of 1000 rpm or more, tubing at the rotor ingress and egress sites undergo considerable movement. Hence, to minimize wear on tubing, a rotor can provide protection of incoming and outgoing tubing, in the form of, for example, a protective and/or insulated sleeve through which a tubing traverses into and out of a rotor. That sleeve can be a tubing of larger diameter, constructed of more durable material, contain insulating material to dampen movement within the sleeve and so on, to protect and to prevent wear on tubing entering and exiting a rotor of interest.
[0053] Hence, a tubing protector can comprise an insulating or dampening material surrounding a tubing of interest, such as, a foam, a sponge, a hydrogel and so on. The sleeve can be crenulated, crinkled, comprise an, accordion, surface, grooved, corrugated and so on, such as, a bending straw, to facilitate bending of the sleeve and of the tubing within.
[0054] In embodiments, a tubing protector can be contained within a more durable material, such as, a ceramic, a plastic, a metal and so on, to provide additional support for the tubing, to allow greater clearance for movement, to minimize areas of friction or contact of tubing with a surface and so on, such as, a sleeve, a nut, a hollowed screw and so on.
[0055] Due to high cost of machining a mixer-settler spiral form as HDPE disks (herein, disc, disk, and plate, are used interchangeably) and use of TEFLON sheets (which are non-compressible) as gaskets, current rotors are prone to leaks, particularly at higher centrifuge speeds.
[0056] Thus, a mixer-settler rotor described in the '847 patent was redesigned and built with less expensive, more durable functional materials, for example, a durable plastic, to prevent leakage. TEFLON sheets are a cold flow material and do not retain original thickness after being compressed. During and after use, a rotor needs to be retightened. However, it is difficult to retain a secure liquid seal. Hence, an improved gasket would be beneficial. For purposes herein, septum, gasket, sheet, washer, and so on are used interchangeably.
[0057] In embodiments, each disc can be associated with two or three, or more, gaskets above and/or below in a rotor stack, as compared to a single gasket in the prior art. Hence, a rotor of interest includes at least two, at least three, at least four or more gaskets above and/or below a disc.
[0058] A mixer-settler spiral disk can comprise, for example, polycarbonate, polyoxymethylene and so on, fabricated by, for example, injection molding, and packed between softer, compressible sheets made of, for example, an elastomer (for example, about 0.035 inch thickness and coated with TEFLON or a fluorinated ethylene propylene (FEP), such as, VITON (VITON is a trademark of Chemours of Wilmington, DE and is a copolymer of hexafluoropropylene and vinylidene fluoride, terpolymers of tetrafluoroethylene, vinylidene fluoride and hexafluoropropylene, or perfluoromethylvinylether, which can be formed into membranes and other forms), an artificial rubber, a synthetic rubber and the like, that compress and regain original shaping when pressure, weight or any other compressible force is removed or reduced. Gaskets are available commercially and are provided in a variety of materials, of chemical resistance, of thickness, of hardness and so on, selection of which for use in CCC is a design choice. Thus, consideration is provided as to, for example, solvents used, to ensure a gasket material is not degraded by, is immune to, is not chemically reactive with and so on solvents used; a suitable thickness to ensure no leaks occur without adding much weight to a rotor stack; and so on.
[0059] Of plural gaskets, one or more may be of reduced diameter (as compared to a disc) and placed or situated about center screws and void of a rotor to minimize or to avoid fluid leak toward a central void, such as, a shaft, centrally situated in a rotor and a disc. Such a gasket may serve as a washer about a central void. A washer facilitates maintaining even and secure pressure with gaskets and a disc. That gasket can be made of a more rigid or stiff material, such as, acetate or TEFLON with a thickness of about 0.01 in. A, ring (that term is used interchangeably with, washer, gasket, and so on) with fastener devices, such as, screw holes, as needed based on design, an example of which is shown as C in
[0060] Full sized gaskets are constructed or selected to have a diameter less than that of a disc, the outer perimeter of a gasket fits within the outer hard stop, rim, lip, barrier and the like of a disc. The central void of a gasket has a perimeter that fits within or contacts the outer surface (distal, away from the shaft) of the inner hard stop of a disc. Hence, a gasket applied to a disc does not extend beyond the area bounded by the rims of a disk or the boundaries of a disc (
[0061] Another gasket can comprise at least one radial slit, slot or channel, where a slit or channel marries with, is in register with, aligns with, complements, completes a void provided by a radial channel at an inferior surface of a disc and so on, so such a gasket does not constrict flow within a radial channel of a disc. A gasket can be made of any of the above materials and can have a thickness and the like as a design choice to ensure no leaks occur without adding too much weight to a rotor stack; and so on.
[0062] Thus, for example, a radial slit about 1 mm wide can be made on an inferior surface of a disc between a hole from end of a spiral on a surface above and start of a next spiral above to serve as a conduit for liquid flow between the spirals. Such a gasket is shown as B in
[0063] The slitted gasket, washer and compressible gasket, B, C and D in
[0064] In embodiments, each disc comprises a gasket thereon. Thus a gasket sits atop a disk with a gasket abutting, laying atop, contacting and so on the superior channeled surface of a disk. Hence, the gasket above the uppermost or first disc can contact an endplate. Alternatively, that gasket above the first or uppermost disc can contact another spacer, seal, separator, gasket and so on, in turn can contact another spacer, seal, separator, gasket and so on or the inferior surface of the top or superior endplate. The lowermost or last disc also can comprise therebelow a spacer, seal, separator, gasket and so on, which can contact a second spacer, seal, separator, gasket and so on or the superior surface of the bottom or inferior endplate.
[0065] In embodiments, an improved device for separation and purification of CNT's is a modification of a device described in the '847 patent. A rotor is made of stacked spiral grooved disks where solvent flows to separate molecules therein. A groove terminates in a hole that allows liquid to flow under a disc to a next interleaved spiral or to a next disk. In one type, there are four interleaved (interwoven) grooves, (channels are designed to course in alternating or non-adjacent grooves or layers) on and of a stackable disc, which at the end of each spiral, a channel underneath each disc courses fluid to beginning of a next spiral groove on an upper surface of a disc. Disks are sandwiched between gaskets or septa that keep fluid flow in a groove. Each disk is shaped as provided, for example, in
[0066] Disks of the '847 patent were made of HDPE and were 5 mm thick. However, in light of the leaking issue discussed above, new discs were needed and designed.
[0067] Thinner disks that are durable, reduce weight, are not chemically reactive with solvents and are made of materials conducive to more cost effective construction methods, such as, injection molding, stereolithography, 3D printing and so on are described herein, Hence, discs can be made of, for example, polycarbonate, acrylonitrile butadiene styrene, a polyoxymethylene, such as, DELRIN (a trademark of Chemours, Wilmington, Del., is a thermoplastic that can be formed in to a number of shapes), a polyphenolsulfone, an ultra high molecular weight polyethylene, any material used in a 3D printing process, such as, epoxy, ester and styrene compounds, and so on. Discs can be less than 5 mm in thickness, to minimize weight and overall weight of a stacked rotor. Diameter of discs is a design choice based on size of a planetary centrifuge, tubing used and so on.
[0068] A rotor of interest, being larger and having greater capacity, can comprise larger disc, more discs or both. Hence, as mentioned herein, a rotor and disc can be about 22.5 cm in diameter. Alternatively, a rotor can comprise 6 or more discs (along with a gasket thereon and any other gasket, seal or spacer), 7 or more, 8 or more, 9 or more, 10 or more, or more discs.
[0069] Discs can comprise a rim, a lip, a raised portion that describes a circumference of a disc, which may be discontinuous, a hard stop, a border, a levee, a ridge and so on about an outer perimeter and about a central void to provide better seating, a more snug fit, better sealing of a gasket to a disc, to minimize leakage, to prevent or to minimize expansion or bulging of a gasket beyond the perimeters and confines of a disc and so on (
[0070] Discs are constructed so that walls of channels are of a height that provides conduits for tubing but also engages a gasket. Partition and radial channels that traverse spiral channels have a wall height less than that of the spiral channel walls and thus, without compression, do not engage a gasket that is laid on a disc, prior to sealing of a rotor,
[0071] The interior void of a disc, and, of a gasket, also is of a size that avoids contact with the planetary shaft of the planetary centrifuge (
[0072] The centrifuge shaft also is constructed to comprise at a lower portion that engages the lower face of a rotor stack, a shelf, a ridge, a flared portion, an extension, an extrusion, pins and so on, of diameter greater than that of the centrifuge shaft. That shelf can have an extending size from one to several millimeters or inches depending on the size of the centrifuge to a size approximating the radius of a disc. The shelf can be continuous about the circumference of a shaft, or can be interrupted, with regular or irregular interruptions. The shelf can be of unitary construction of a shaft, that is, the shaft is formed to comprise a shelf. Alternatively, s shelf can be constructed to include a pin, a bar, a shelf, a stud and the like, appended or affixed to a shaft.
[0073] In embodiments, the rotor can be formed using a three-dimensional prototyping machine (3-D) printer). Examples of a machine that can be used to form the material for the design of the rotor frame include, but are not limited to a Sinterstation 2300 plus, Objet Geometries, Inc. Eden500V, or an EOS Precision.
[0074] The rotor frame securing a rotor in a centrifuge can be machined from a strong, yet light, material, such as, a metal, such as, aluminum; can be molded, such as, a ceramic; can be printed using a 3-D printer using suitable particulate starting materials and so on, as known in the art, and as a design choice.
[0075] The rotor frame is seated on a rotor shaft or spindle, for example, the planetary shaft, using suitable seating materials, lubricating material, shock absorbing material and so on, such as, a washer, spacer, wear pad and so on, of suitable composition to distribute load, dampen vibration, to serve as a bearing, to minimize wear, to minimize friction and so on. For example, a sealed bearing, which can be lubricated, is self-lubricated, is lubricated and sealed and so on can be used. The bearings can be circular, that is, balls, cylindrical and so on. The bearings can be affixed in a containing device to retain the bearings in place, that is, the bearings are sealed in place.
[0076] At movable joints of the shafts, sealed, pre-lubricated or self-lubricating roller bearings are employed, such as, at or in the juncture of the shaft and a shaft housing; at or in the juncture of a shaft and a shaft collar and so on. Such sealed bearings are suitable for high radial load and minimize angular misalignment at high speed. Increased rotor size and weight are better accommodated with such bearings.
[0077] Such devices provide a secure seating and connection of a rotor frame on a shaft, and enable free movement on the rotor frame about the shaft.
[0078] A rotor can be constructed so that the lower face of the rotor that engages, abuts, sits on and the like, a shelf of a shaft of interest, can comprise parts which engage complementary sites of the shelf, an accommodating void, such as, a rectangular void on an inferior rotor face in register with and which engages a protruding bar structure of a shaft. Such an engaging affixes a rotor to a shaft.
[0079] The planetary shaft also can be designed to comprise a flare in size that increases in diameter in the direction away from the rotor (
[0080] Also, end plates (end plates, end flanges, supporting plates, and, flanges, are equivalent terms herein) of a new rotor were redesigned. Generally, flanges or end plates are made of a metal material. To balance strength of material to ensure firm and equal pressure is applied to components of a rotor stack, and rotor weight, end plates are designed to be of a thickness that ensures those goals are achieved. A top end plate comprises fastening devices, as well as fittings for seating in a centrifuge and for entrance of sample and solvent, and can be at least about 7 mm, at least about 7.2 mm, at least about 7.4 mm, at least about 7.6 mm, or more in height. A bottom end plate comprises fastening devices, as well as fittings for seating in a centrifuge and is at least about 4 mm, at least about 4.2 mm, at least about 4.4 mm, at least about 4.6 mm, or more in height. The outer face of the end plates, the face that is not in contact with a disc or gasket, can be hollowed and is ribbed, with any number of ribs, which may or may not have the same length, which may extend from the inner void to the outer perimeter, can be of uniform shape, can be tapered, can have any shape which provides strength and support of the end plate, while minimizing weight.
[0081] Hence, a new rotor of interest comprises newly sized end plates and new, thinner, plastic discs, with a rim or rims, radial channels of an inferior surface comprising a depth of 1 mm or greater, gaskets with a diameter less than that of a disc, protective structures at tubing egress and ingress at the rotor, discs and gaskets do not contact the centrifuge shaft and various other improves taught herein to obtain the goals mentioned hereinabove.
[0082] Thus, flow tubing was attached in a top and an out-flow tubing out a bottom of a rotor, disc or stack of discs. The input and output sites of tubing into a rotor are fortified, protected and so on to minimize tubing wear and damage as discussed hereinabove.
[0083] End plates, discs and gaskets were configured to accept and to accommodate screws and nuts to secure a stack of disks and gaskets. Screws are tightened evenly and incrementally around a center and an outer perimeter, optionally, in an alternating or opposing order for even tightening and to obtain an even seal across a face of a rotor. Screws are tightened partially, alternatively and evenly around a central region and an outer perimeter to provide a uniform seal with gaskets without distorting or deforming gasket shape, to form an even seating of disc, gasket and rotor. Using such an assembly, liquid flow was obtained at up to about 1 ml/min at high centrifuge speeds with no leaks.
[0084] As a result of those improvements, a mixer-settler CCC rotor can be adapted for use at higher speeds, for use with thicker solvents and for use with samples of higher molecular weight by using new gasketing; using new washers, using new discs, using new end plates and so on in a rotor of interest that is lighter than prior art rotors; and using a shelfed shaft to support a rotor, to separate large molecules. Thus, there are no leaks when all discs, gaskets and washer are ordered and an assembly is tightened, for an even seal around and about a rotor; or new discs in a new rotor are used to form a rotor stack, again with an even seal about discs that enable use at higher centrifuge speed for separating larger molecules.
[0085] With a CCC rotor of interest, protein analytical and preparative separations are possible with ATPS systems. As an ATPS system, the general diluent is water. Hence, water is a primary vehicle for stationary and mobile phases.
[0086] Complete recovery of samples is possible and/or baseline separations can be developed for any protein mix or mix of larger molecules, including CNT's. Suitable solutes for forming the two phases include polyethylene glycol (PEG), for example, having a size from about 6,000 to about 10,000 MW, and dextran, for example, having a size from about 60,000 to 90,000 MW.
[0087] Polymer solutes can be present in phases or in originating solutions in an amount from about 0.1 wt % to 95 wt %, based on weight. A weight or volume ratio of the first polymer solution to the second polymer solution prepared separately and then combined can be from about 1:100 to about 100:1.
[0088] For example, a 10% by weight solution of 8,000 MW PEG in water and a 16% by weight solution of 75,000 MW dextran in water can be used. When combined in a 3:2 volume:volume ratio of the PEG solution to the dextran solution, two phases result on standing. That total 3:2 mixture comprises 6% PEG and 6.4% dextran. Those two phases can be used in a CCC rotor of interest forming mobile and stationary phases.
[0089] A solute, such as, PEG or dextran, can be derivatized or substituted with one or more chemical groups, which derivatives can be purchased commercially or produced practicing known methods. Substitutions can include a compound or a radical substituted with at least one substituent independently selected from, for example, a halide, a hydroxyl, an alkoxy, a nitro, an amino, a carbonyl, a thiol, an ester, a carboxyl, a salt, an alkyl, an aryl, an arylalkyl, a heteroalkyl, a heteroaryl, a cycloalkyl and so on, or a combination thereof.
[0090] Surfactants are included in a diluent or solvent, such as, sodium dodecyl sulfate (SDS) or other sulfates, sodium cholate (SC), sodium deoxycholate (SDC) and the like. Surfactants also may be present in CNT preparations to assist in dispersing particles in solution. Amount of a surfactant is a design choice to facilitate suspension and separation. A surfactant also can be used to form a gradient in a separation.
[0091] Thus, CNT's may have a surfactant, detergent or dispersant (equivalent terms) disposed therewith, generally on an external surface of a CNT. A dispersant may stabilize a CNT preparation and may aid fractionating of CNT populations during separation. A dispersant can be present on CNT's in an amount effective to form a colloid or to be dispersed in a solvent, diluent or phase.
[0092] In embodiments, a dispersant includes a polyether, a sulfate or a sulfonate (e.g., SDS and sodium dodecyl benzene sulfonate), a bile salt, a polyvinyl pyrrolidone or combination thereof.
[0093] Examples of bile salts include a salt (such as, a sodium or potassium salt) of a conjugated or unconjugated cholate or cholate derivative including, deoxycholates and the like.
[0094] A surfactant can be ionic or nonionic, where ionic surfactants include anionic, cationic or amphoteric surfactants. Surfactants often are amphiphilic. Examples of cationic surfactants include alkylamine salts, quaternary ammonium salts, and the like. Examples of amphoteric surfactants include amine oxides. Examples of anionic surfactants include alkylbenzene sulfonates, such as, dodecylbenzene sulfonate and dodecylphenyl ether sulfonates.
[0095] As a rotor of interest separates larger molecules, molecules, such as, single-wall carbon nanotubes (SWCNT's) can be separated [22]. Semi-conducting CNT's bind to polysaccharides and can be separated from metallic CNT's in agarose columns by elution with certain anionic detergents [17] as known in the art. In embodiments using a PEG and dextran ATPS system, semi-conducting CNT's bind to or are located preferentially with dextran in an SP and are separated from metallic CNT's which have high partitioning in a PEG-rich MP and are eluted generally earlier.
[0096] CNT's are a carbon allotrope, a derivatized carbon allotrope or combination thereof.
[0097] CNT's generally have an average particle size of less than about 1 m. CNT's are measured as known in the art, for example, by static or dynamic light scattering; ultraviolet, visible or fluorescence spectroscopy; atomic force microscopy; and so on. CNT's can have an average particle size of about 250 nm or less, although for purposes herein, actual size is a design choice as a focus is separation of populations of common property or properties.
[0098] Carbon nanomaterials include fullerenes, graphenes and CNT's, which comprise SWCNT's, double-walled CNT's (DWCNT), multi-walled CNT's (MWCNT) and so on, and for purposes herein, CNT is meant to include any carbon allotrope.
[0099] Fullerenes include cage-like, hollow forms of carbon possessing a polyhedral structure with, for example, from about 20 to about 100 carbon atoms. For example, C.sub.60 (buckminsterfullerene) has 60 carbon atoms with high symmetry.
[0100] Nanotubes include carbon nanotubes, metallated nanotubes and so on. Nanotubes have open or closed ends. In embodiments, nanotubes include additional components, such as, metals or metalloids, which can be incorporated into the structure of the nanotube, can comprise a surface coating or both.
[0101] CNT's can have one of several geometrical arrangements as to a lattice of carbon atoms. For example, SWCNT's can be distinguished by double vector indices (n,m), where n and m are integers that describe geometry and configuration of carbon atoms and component molecular structure of a nanotube. Arm-chair, SWNCT's are (n,n), when a nanotube is cut perpendicularly to tube axis, only sides of hexagons are exposed, and the pattern around a periphery of a tube edge resembles an arm and seat of an arm chair repeated n times. When (n,m=0), an SWCNT is, zigzag, and for (n,0), when a tube is cut perpendicular to a tube axis, atoms located at an edge of a tube have a zigzag arrangement. When n is not equal to in and not equal to 0, an SWCNT is chiral.
[0102] Electronic properties of SWCNT's can be dependent on configuration. Thus, SWCNT's can have different electronic signatures for different conformations. Consequently, SWCNT's are metallic (electrically conductive) or are semiconducting (comprising a bandgap from about a few meV to about 1 eV.) Generally, for n=m or n-m is a multiple of three, an SWCNT is metallic and for other n,m combinations, an SWCNT is semiconducting. Accordingly, armchair nanotubes are metallic and have higher electrical conductivity.
[0103] Carbon atoms in a CNT can be displaced or substituted by another element practicing known materials and methods. Hence, a CNT can include an oxide, such as, silica, alumina, titanium, tungsten oxide, iron oxide and the like, a carbide, such as, tungsten carbide, silicon carbide and the like; a nitride, such as, titanium nitride, boron nitride, silicon nitride and the like; or combination thereof. CNT's can include an alkali metal, an alkaline earth metal, an inner transition metal (a lanthanide or actinide), a transition metal and so on. Such metals can coat a CNT. A CNT can be attached covalently to a pharmaceutically active compound and used for drug delivery.
[0104] CNT's can be made by a known method including chemical vapor deposition, such as, high-pressure carbon monoxide conversion (HiPco), laser ablation, arc discharge, a specific catalytic processes, such as, CoMoCAT (Chasm Advanced Materials, OK) and so on. CNT's also are available commercially. It is known many such synthetic methods produce a variety of species, such as, size, chirality, n,m dimension and so on.
[0105] In CCC, CNT's can be present in an MP or in a retrieved fraction in an amount from 0.1 wt % to 95 wt % based on weight. A concentration of MP polymer, SP polymer and sample load are selected to maximize resolution of a populations of particles or molecules.
[0106] In embodiments, a ratio of a volume of MP to SP can be from about 0.01:100 to about 100:0.01.
[0107] CNT's can be separated into chiral species by applying an ATPS system in a mixer-settler CCC of interest.
[0108] Because CNT's are available commercially, CNT's can be provided, for example, as a suspension or a powder. Each preparation contains reagents desired and used by a manufacturer. Hence, a CNT may be dispersed in a micelle, with a detergent, such as, an anionic detergent, or can be bound to a solid support, such as, an agarose bead. CNT's can be removed from agarose beads by exposure to SC or SDC. But, some solutes can impact CNT structure, property and behavior in a solvent and in a chromatographic separation. Thus, it is desirable to have CNT's suspended in a solution for use in CCC.
[0109] An extraction method was developed for CNT's using an ATPS system of PEG and dextran [19], with combinations of detergents that enable CCC separation of semiconducting from metallic CNT's from mixtures of CNT's of similar diameter. Partition coefficients (K) of individual CNT's could be measured by spectroscopy, UV, fluorescence and Raman spectroscopy [18].
[0110] Hence, for example, an aliquot of powder, such as, about 10 mg in an experimental chromatographic run, can be mixed with a 1:1 v/v mixture of SC and SDC as a dispersant solution and to standardize solutes used for CCC. For example, that 10 mg sample can be mixed with about 0.5 ml of SC and about 0.5 ml of SDC. SC and SDC solutions can be prepared as 5% w/w stock solutions. The CNT dispersion then is sonicated, for example, with a probe, three times at 20 sec each to suspend CNT's in that detergent solution. The mixture is centrifuged and an aliquot, such as, about 250 l, is added to about 3 ml of UP and 3 ml of LP (SS #1 in Table 1), which represent solvents useful in CCC. Particular UP and LP can comprise PEG and dextran, and SDS as a surfactant that forms a gradient in a chromatography. The preparation is mixed and allowed to settle into two phases. UP is removed and an additional 1 ml of UP is added and mixed, and that preparation then is used as a sample for a CCC run. By that method, CNT's are exposed to known surfactants, are washed and are suspended in a solvent that will be used directly in a CCC run. Centrifuge is turned on and mobile UP phase is introduced after sample, at a rate, for example, of about 0.5 ml/min, to produce an SDS gradient in the PEG-rich UP.
[0111] New gaskets, washers, discs and rotors can be operated at a speed and at an MP fluid flow rate as design choices, for example, which provide maximal separation of molecules. Hence, a flow rate can be about 0.25 ml/min or more, about 0.5 ml/min or more, about 0.75 ml/min or more, about 1 ml/min or more, or greater. A centrifuge can be operated at a speed of about 700 rpm or more, about 800 rpm or more, about 1000 rpm or more, about 1200 rpm, or faster.
[0112] Improved mixer-settler spiral disk rotor designs of interest enable a means to chromatograph CNT's in an automated system. A laboratory instrument system can consist of a planet centrifuge with one or more mixer-settler rotors, each comprising two or more discs, with gaskets as needed or as a design choice, a gradient pump, sample loading valve, fraction col lector and a system controller via computer or mobile phone app. Time of a run, with settings of rpm, pump solvent delivery gradient and flow rates, automatic sample injection and fraction collection time can be programmed as a design choice. Rotor and components of interest provide a new useful separation means for materials of the nanotechnology market.
[0113] After fractionating a composition (e.g., after a single run of a process above), separated particles may be included in more than one phase, even if in an amount that is not readily detectable. Using a, for example, PEG/dextran, ATPS system, semi-conducting CNT's are in LP. (To alleviate presence of CNT's in both phases, a fraction could be used in a second run of a separation process of interest, and so on, until a pure population of a particular CNT is obtained but that would require removal of SDS which was used to form the discriminating gradient.) That could result in a population with a purity of about 100%, greater than or equal to about 50%, greater than or equal to about 75%, greater than or equal to about 85%, or greater or more pure. By, about, herein is meant a metric that can vary up to 05% from a stated value, but no greater than an absolute, for example, about 100% cannot exceed 100%.
[0114] A fraction or a separated mixture is removed from a rotor and can be subjected to further processing, such as, removal of solute, surfactant, replacement of diluent and so on, practicing known methods, such as, dilution, washing, centrifugation, evaporation and so on to obtain a purified preparation of a CNT population.
[0115] A goal of the materials and methods of interest is to obtain a pure population of a CNT, based on a difference of a property between or among populations of particles in a starting sample, such as, metal chirality, shape, size, diameter, length, handedness and so on.
[0116] Materials for making a rotor or disc of interest are provided, for example, in the '847 patent; components can be machined; or components, such as, discs or rotors, can be purchased, for example, from CC Biotech (Rockville, Md.), Planetary centrifuges can be made as known in the art or can be purchased.
[0117] The invention now will be exemplified in the following non-limiting examples.
EXAMPLES
Example 1
[0118] A prior art mixer-settler spiral disk rotor, was disassembled for parts. Fluid flow had become blocked after use.
[0119] On inspection, the plastic plate or disc was found to have too shallow a return channel underneath, the depth was observed to be less than 1 mm. The soft gasket below the disc had filled the space in the channel and blocked fluid flow.
Example 2
[0120] After the rotor of Example 1 was used for about 3 months, leaking was observed through the center towards the shaft.
[0121] It was discerned that screws around the center had been overtightened resulted in breakage of some screws. Gaskets revealed solvent leaked around the screws in the center area, plates and gaskets were not sealed well.
[0122] Screw holes of the bottom end plate were reamed so screws could be tightened without pressure on the screws and on the substance of the bottom end plate, the threads and screw holes. The screws were associated instead with nuts for tightening and a more decentralized pressure on the bottom plate.
Example 3
[0123] An assembled rotor with a new gasket below a disc where radial slits in the gasket marry with channels in a disc, also included compressible VITON gaskets. A smaller gasket or washer of interest about the central portions of a rotor minimized or prevented leaking.
[0124] A mixer-settler spiral disk with gasketing can be used to separate large molecules, such as, proteins as well as separation of species of CNT's using an ATPS system.
Example 4
SWCNT's in an ATPS System
[0125] Single and multi-step extractions with an ATPS system in CCC containing anionic detergents produced separation of semi-conducting CNT's from metallic CNT's in mixes of larger diameter or of small diameter CNT's. Various species of CNT's displayed different K depending on diameter.
[0126] A solvent system consisted of PEG (MW=6,000-8,000) and dextran (MW=around 75,000 from Leuconostoc mesenteroides). Concentration of SC and of SDC is adjusted to modify K of particular species of CNT's as measured by fluorescence. For example, 0.27% SC and 0.21% SDS up to 0.81% SC and 0.63% SDS in a solvent system have semi-conducting CNT's in an UP with increasing K and metallic CNT's in an LP also with increasing K Thus, two classes of CNT's are fractionated with gradients of surfactants [18].
[0127] Metallic CNT's elute early with the PEG upper mobile phase and semiconducting CNT's are retained in the dextran lower stationary phase and elute later. Fractions can be collected and different CNT's eluted depending on hydrophobicity of micelles of nanotubes with different shape.
Example 5
Gradients
[0128] Gradients can be evaluated initially by measuring partitioning at onset of separation and after separation is completed. Increasing or decreasing pH gradients can be made, for example, with glacial acetic acid, triethylamine or cyclohexylamine, from pH 4 to 8, for example. Bases that do not cause UV interference can be useful. Another approach is to vary surfactants or to have a surfactant gradient for selectivity.
Example 6
Modification of a Polymer
[0129] Modification of an LP polymer, dextran, can be done by reaction with diphenyl carbamyl chloride which couples to hydroxyls [20]. After reaction, a polymer can be dialyzed to remove reagents and either used directly or freeze-dried and a, for example, 15% aqueous solution prepared. Aromatic groups added interact with SWCNT walls and micellar surfaces to change elution pattern.
[0130] Other modifications of dextran include coupling to other molecules that influence elution of micellar CNT's.
Example 7
Solvent Systems
[0131] Solvent system components are mixed to form two phases and a volume of each phase is taken and combined with CNT's. The solution is agitated and phases allowed to separate. Concentration of nanotubes in each phase is measured by, for example, fluorescence spectroscopy. Solvent systems giving different values of K are selected for separation experiments. Also, solvents that reveal differences between metallic and semi-conducting CNT's are considered. K can be used to provide a ratio of upper to lower phase (C.sub.u/C.sub.l), C is concentration. In CCC, K from a run is an SP to an MP ratio (C.sub.s/C.sub.m) which can be calculated from elution volumes. At K=1, a compound elutes at a column volume which is total volume of flow path excluding amounts in flow tubings. A phase chosen as an MP is that giving a K closer to 1. Elution volumes from about 0.3 to about 2 comprise a zone of maximal resolution. K.sub.s/m (SP/MP) calculated from elution of a compound is ratio of elution volume of the chromatographic peak (p) minus excluded volume of the column/rotor (m) to the total volume of the column/rotor (c) minus excluded volume of the column/rotor.
K=(V.sub.pV.sub.m)/(V.sub.cV.sub.m)
[0132] For analysis of sample mixtures, efficiency of separation can be determined by use of the conventional gas chromatographic equation [21]:
N=(4R/W).sup.2
[0133] Theoretical plates, TP or N, are calculated from shape of peaks. R is retention volume of a peak maximum and W is peak width expressed in the same units as that of R. For preparative separations, N may be up to 1000, but a more important relationship is resolution. Resolution between adjacent peaks is given by, where R values are retention volumes of the two species or populations:
R.sub.S=2(V.sub.R2V.sub.R1)/(W.sub.1+W.sub.2)
[0134] Using that equation and substituting each solute retention volume by the following:
V.sub.R=V.sub.m+KV.sub.S
[0135] where V.sub.m cancels giving:
R.sub.S=2(K.sub.2K.sub.1)V.sub.s/(W.sub.1+W.sub.2).
[0136] Thus, resolution is proportional to V.sub.s and difference between K's. From high V.sub.s typical of CCC, high resolution is possible even with low N values, which can be <1000.
[0137] Stationary phase (S.sub.F) retention measurement is done by filling a rotor with SP, beginning centrifugation and then pumping MP through at a flow rate appropriate for a rotor and solvent system, usually at about 0.5 ml/min. When solvent front comes through, excluded SP represents excluded volume, V.sub.m. Subtracting V.sub.m from total column volume, V.sub.c, yields SP volume, V.sub.s. Phase retention is ratio of SP volume to total volume, V.sub.s/V.sub.c. High S.sub.F values above 50% for polar and ATPS solvent systems have been achieved with the rotors of interest.
Example 8
[0138] Methods, such as, chemical vapor deposition, HiPco and CoMoCAT, produce different compositions or forms of SWCNT's. Dispersions produced may have more amounts of large diameter CNT s than small diameter CNT's, for example.
Example 9
[0139] Dextran (MW 75,000), SC, SDC, SDS and PEG (MW 8,000) were obtained from Fisher Scientific (Boston, MA) or Spectrum Chemical (Gardena, Calif.); and CNT dispersion of 6.5i in 0.2% SDC was obtained from SouthWest NanoTechnologies Inc. (Norman, Okla.). A sample of 6.5i powder from the same manufacturer also was used. Water was purified in a Neu-Ion system (Baltimore, Md.) or HPLC water was obtained from Fisher Scientific.
[0140] A planetary centrifuge (CentriChrom, Inc. Buffalo, N.Y.) was mounted with one mixer-settler rotor (17.5 cm OD, cat. no. 205-10001, CC Biotech, Rockville, Md.), Some experiments were performed with a rotor made of stacked polycarbonate disks. Each disk had four interleaved spirals and flow goes through serially, then to a next disk. A flow channel groove in a disk has mixing and settling sections with a glass bead in every fourth section. Total volume in a rotor with six layers or discs is 84 ml. Some separations were conducted with a rotor comprising different number of discs, such as, five or seven layers or discs.
[0141] As noted in Examples 1 and 2, there were difficulties with leaking using prior art rotors. Hence, another gasket was designed containing radial slits in register with radial channels at a lower surface of a disc, to maintain or to space a sealing gasket and to allow unimpeded liquid flow. Also, a washer or gasket can be used about central portions of a disc.
[0142] CNT's were separated successfully using that rotor and gasket set up.
Example 10
[0143] Another rotor was machined with metal top and bottom base plates that contained ribs that ran the radius of the base plate and were tapered and of a lower height toward the outer periphery on the surface not in contact with disc or gasket (the outer face of a stack) to apply more secure and more even pressure on plastic disks around an entire surface of a rotor sandwich without contributing too much weight to the final rotor, see, for example, Example 2. A mixer-settler disk had deepened radial channels on a lower or interior face of a disc to minimize interruption of flow. Segment divisions or pins in flow channels were placed straight and at a height lower than channel walls. A disc was fabricated by stereolithography with an epoxy resin (SOMOS NeXt, DMS, Elgin, Ill.) with wet-dry blast surface treatment. A top or superior surface (
[0144] Polytetrafluoroethylene (PTFE, TEFLON) flow tubing, 1/32 in inside diameter (ID) (Zeus Industrial Products, Orangeburg, S.C.) was connected to a top flange (metal plate or end plate) with a metal nut (compression screw with a stainless steel flange and plastic ring (Idea Health and Science, Chicago, Ill.)) and passed into a rotor shaft and out a bottom into a central axis. Another flow tubing connected to a bottom end plate outlet also went into a rotor shaft and out an open end with other flow tubing into a central axis. Both tubes are inside a larger ID TYGON protective tubing containing some lubricating grease. Flow tubing passes out a top of a centrifuge and is clamped to prevent twisting. A rotor arm is counterbalanced with metal rings equal in weight to a mixer-settler rotor (which was balanced with, for example, weights, screws, nuts and so on), placed at same height and same distance from the center axis of the centrifuge.
[0145] Solvent is pumped from a gradient dual pump system (D-Star Instruments, Manassas, Va., controlled with Clarity software). Flow passes in a pump through a manifold with a 10 ml sample loop valve and another valve with helium for clearing rotor contents. Solvent flow then is connected to an in-flow tubing of a CCC instrument. Outflow from an instrument central axis goes to a fraction collector (Pharmacia or Bio-Rad).
[0146] Performance improved, with lower back pressure, no difficulty with air bubbles forming and no leaks.
[0147] An ATPS system of PEG MW 8,000 and dextran MW 75,000 (DEX) containing SDC was used. A gradient of SDS from 0 to 0.7% in the upper PEG-rich phase as MP served to elute CNT's in the chromatography. Prior to use in CCC, volumes of stock solutions (see Table 1) were mixed in a separatory funnel and phases separated after about 45 min with about 351 ml in the upper phase (UP) and about 129 ml in the lower phase (LP) for SS #1.
TABLE-US-00001 TABLE 1 Preparation of the solvent systems for sample and gradient spiral countercurrent chromatography Sample pre-load Stock solutions Solvent system #1 extraction by weight g/g (SS #1) SS #2 SS #3 SS #4 PEG 10% 300 ml 300 ml 4 ml DEX 16% 200 ml 200 ml 2.5 ml 2.5 ml SDC 10% 1 ml 1 ml SDS 3.5 g PEG 14% 4 ml
[0148] For sample preparation, a stock 1% by weight of CNT powder in solution was sonicated with a probe three times for 20 sec each. Thus, a suspension of about 10 mg of CNT's in about 0.5 ml of about 5% SC and about 0.5 ml of about 5% SDC was sonicated and 0.25 ml was removed and added to 3 ml of UP SS #1 and to 3 ml LP SS #1. The mixture was vortexed and allowed to settle into two phases. UP is removed and 1 ml of UP SS #1 was added to the CNT UP solution and the total was loaded into a CCC rotor as a 2.5 mg sample load.
[0149] CNT dispersions or suspensions provided by others were extracted according to a previously published method using SS #3 and SS #4 described in Table 1. A 0.5 ml or 1 ml amount of a CNT dispersion (approximately 0.1% of 6.5i CNT's in 0.2% SDC) is extracted and loaded through a sample loop valve. Sample prep was done by combining about 0.5 ml CNT's with about 0.5 ml of about 10% SC to 4 ml UP SS #3 and about 0.5 ml LP SS #3, the mixtures were vortexed and then centrifuged at 1000 rpm for 1 min. UP is removed and to that was added 1 ml UP #3 and all is loaded into a centrifuge.
[0150] A rotor is filled with LP at a rate of 0.5 ml/min. Sample is loaded in a 10 ml loop; centrifuge is set to about 990 to about 1000 rpm, sample is injected and UP #1 pumped with allow of about 0.5 ml/min. A gradient is started when all of sample is in the spinning rotor. A gradient of UP #1 A to UP #2 B is made over an 8 hr period for a 5 layer rotor (Table 2). Fractions are collected every eight min. Elution mode=U o H (U=upper phase; o=outer entry, bottom in CCW rotation; H=head to tail end of column/rotor, which means sample and mobile upper phase flow entered through the bottom of the rotor in head to tail direction)
TABLE-US-00002 TABLE 2 Gradient conditions for CNT separation Stationary phase = LP SS #1; Mobile phase A = UP SS #1 B = UP SS #2 Rotor Conditions Type of gradient 5 layer mixer-settler 0 to 100% B 480 min linear gradient disks 7 layer mixer-settler 0 to 100% B 660 min linear gradient disks 6 layer mixer-settler 0 to 100% B 540 min linear gradient disks See paragraph 90 7 layer mixer-settler 0 min 0% B convex gradient disks 220 min 50% B 440 min 80% B 660 min 100% B
[0151] Generally a 0.5 ml aliquot is taken from a vortexed fraction to include both phases and 0.5 ml 2% aq. SDS was added to dissolve all phases and to make a clear solution. Absorbance at two wavelengths is read with water as blank in a Cary 3E VC-Vis Spectrophotometer (Varian, Santa Clara, Calif.). Absorbance of fractions is plotted. Fractions containing black solids (soot) or dark solutions and colors are noted. When enough concentrated fractions were achieved in CCC runs, spectra were measured from 240 to 900 nm to analyze peaks of chiral species.
[0152] Fractions containing color were assessed for semiconductor activity in a polybrene impedance assay.
[0153] For characterization of a spiral CCC process, CNT's from SouthWest Nanotechnologies composed of mostly 6.5 chiral species with a range of lengths was used as a sample. The 0.1% CNT's in 0.2% SDC dispersion was dark, mostly black, with some passage of light. One ml of an extracted solution was loaded, where the original preparation was extracted as described above, but with extraction SS #4 made with 14% PEG (Table 1).
[0154] That set up results in CNT's in LP in a solution, not packed particles. Of each extract, 0.5 ml of LP were combined and loaded. Solvent front where excluded SP elutes was at fraction 9, or about 34.9 ml, meaning SP retention was about 59%, a high amount for ATPS. After solvent front, fractions were gray in the UP and clear fractions followed until fractions 39-41; light green, then darker green-purple at fractions 42 and 43; 44 is purple; and then samples were purple-grey until fraction 50. Colored fractions emerged at 35 to 40% B in the gradient. After chromatography, cloudy fractions separated into two phases with color in the LP, which contain separated CNT's.
[0155] The following run was with 2 ml CNT solution and 1 ml 10% SC and 2 ml LP #1 which was sonicated and the entire sample was loaded. A convex gradient (Table 2) was run. After solvent front, fractions were grey and strong UV absorbance (used to track compounds comprising aromatic moieties) was measured. (In the sample prep, UP was not separated. Therefore, a large peak after solvent front was present. In most other runs, UP was removed and fresh UP SS #1 was added. That removed a large UV peak after solvent front.) Green fractions are noted at fraction 47 and purple starting at 50 until 56. That run had two times more material than a previous run and subsequent runs with different extractions and more volume resembled the run with green fractions followed by purple fractions. Colored fractions had semiconductor activity in field effect transistors.
[0156] Impurities were removed as revealed by soot and dark colors in a UP at solvent front and more dark particles were in an SP left in a rotor, which was eluted after pump out. After chromatography runs, a rotor is flushed with many column volumes of water to remove SDS. Green fractions followed by purple fractions were 6.5 chiral species, the major type (based on composition of the starting sample and measured spectra of fractions), which were removed from a chiral type of green color.
Example 11
[0157] Materials and methods of Example 10 were practiced, except a different starting CNT preparation was used.
[0158] Powder from SouthWest NanoTechnologies, SWeNT SG 6.5i-L43 was suspended at 10 mg/ml and sonicated as described in Example 10. About 250 l were added to SS #1, 3 ml of each phase as described were used, mixtures shakened and allowed to form phases, UP was removed and 1 ml UP added and the total loaded. A linear gradient from 0 to 100% B was run at 0.5 ml/min over 540 min in a new mixer-settler rotor with 6 layers, third entry of Table 2. Fractions after solvent front had gray UP and black fluffy precipitate at the interface and comprised a high UV peak. That was followed by clear fractions, two pink fractions, followed by clear fractions then light blue fractions, a fraction that was dark yellow or green then purple fractions. Colors were bright and concentrated enough to provide spectra. The experiment was repeated with identical results.
[0159] From spectral analyses, purple fractions are the major chiral species of 6.5 and light blue fractions can be 7.6 or 7.3, which have close spectral peak maxima. CNT's with surfactants bind dextran in SP that elute as reverse micelles. On standing, those fractions separate into two phases with CNT's in LP.
Example 12
[0160] The materials and methods of Example 10 were practiced, except a different starting CNT preparation was used.
[0161] Separations of CNT powders provided by other suppliers were conducted in a rotor with slitted gaskets and washers; and with a new rotor with thicker upper and lower plates as described in Example 10. Samples of dispersions and of powders suspended in solvent, washed and extracted as described in Example 10 were prepared and separated.
[0162] Separation of CNT's was obtained with either rotor.
[0163] CCC using gaskets and washer of interest with prior art discs and rotors; using an ATPS system comprising PEG and dextran; or using a newly machined rotor with thicker flanges and improved fasteners, and manufactured discs with deeper radial channels separates chiral species of CNT's.
Example 13
[0164] A scaled centrifuge with a revolution radius of 13 cm was constructed. The planetary shaft was lipped, and flared at both ends. The increased size enabled a larger rotor, with larger discs and gaskets to increase fluid volume in the rotor. Rotor endplates were ribbed and contained protective sleeves for tubing entry and exit. Discs had channel walls and partition walls of heights as described herein, that is, channel wall were taller than partition walls. Discs contained an outer an inner lip or rim near the outside perimeter of a disc and at the central void of a disk.
[0165] The rotor stack was assembled with discs and gaskets fitted thereon and therein. The rotor stack was secured by fasteners and then seated and secured to the planetary shaft.
[0166] The centrifuge was operated at speeds up to 1000 rpm, with pressures up to 100 psi, without leakage.
[0167] All references cited herein, each herein is incorporated by reference in entirety.
[0168] Various modifications and changes can be made to the teachings herein without departing from the spirit and scope of the subject matter disclosed herein.
[0169] The instant application claims benefit from U.S. Ser. No. 62/533,428 which comprises as a supplement or exhibit the Invention Disclosure form of the instant invention, and the total disclosure of that provisional application is incorporated herein by reference in entirety.
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