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    • 专利摘要:
    A method of making a separation capillary column, or separation channel in a microfabricated device, comprising the steps of: providing an unfilled quartz glass capillary column, or channel in a microfabricated device, etching the inner surface of the column or channel with an etchant, silanizing the column means or the filling column with a polymerization solution comprising monomers, at least one porogen and a polymerization initiator, and polymerizing the mixture to form a rigid monolithic polymer plug in the column or channel. The process is characterized in that the monomers comprise a mixture of divinylbenzene as the main monomer and isodecyl acrylate, and that the porogen or porogens comprise isobutanol, and that the capillary column, or channel in a microfabricated device, preferably has an inner diameter of about 0.05 mm or less.
    公开号:SE1250948A1
    申请号:SE1250948
    申请日:2012-08-23
    公开日:2014-02-24
    发明作者:Cato Brede
    申请人:Helse Stavanger Hf；
    IPC主号:
    专利说明:

    In general, using columns with 0.075 mm ID phase the variable phase can be reduced to a few hundred nanoliters per minute.
    As other researchers have shown, it is even possible to scale down the liquid chromatography further to achieve sufficiently sensitive LC-MS analysis. However, due to the difficulty of filling a very narrow capillary tube with particles, commercially available packed columns are still technically limited to 0.075 mm ID. Theoretically, there are no such limitations and difficulties associated with the production of monolithic columns.
    In a monolithic column, the separation medium is in a form comparable to a single large "particle" which does not contain interparticle cavities, in other words a continuous medium. As a result, the entire moving phase must flow through the stationary phase. This convective de fate accelerates the mass transfer to a great extent. In contrast to diffusion, which is the typical driving force for mass transfer within the pores of particulate stationary phases during chromatography processes, convective genom through the pores allows a significant increase in separation rate.
    Due to the advantages they provide over packed columns, the development of continuous separation media has attracted considerable attention in recent years. In principle, two types of monolithic materials have been used, the first based on modified silica gel and the second on organic polymers. However, while the continuous silica gel media shrinks during the polymerization process, making it difficult to produce practically useful silica gel-based monolithic columns with small inner diameters, these difficulties in producing monolithic columns by in situ polymerization of suitable organic monomers in quartz diameter capillaries as small as 0 , 1 mm.
    The polymerization mixture can be prepared using a wide variety of monomers, giving an almost unlimited choice of both matrix and surface chemistries for variation in retention and separation selectivity. Monolithic columns of acrylamide, polystyrene and methacrylate can be mentioned as frequently used examples. A porogen or a porogenic solvent is usually added to control the porosity of the resulting monolith. A large number of polymer monolith columns, including small ID capillary columns, and methods for their preparation have been previously described in the art.
    WO 2007/149498 A2 describes a separation capillary column, or separation channel in a microfabricated device, produced by in situ copolymerization of a functional monomer and a crosslinking monomer, which increases the strength of the polymer matrix. Styrene-based monomers, such as styrene and divinylbenzene, or meth / acrylic acid-based monomers, such as butyl or stearyl methacrylate and ethylene glycol dimethacrylate, are preferred. A polar porogenic solvent (or a polar porogen), such as ethanol, methanol, propanol or acetonitrile, is used in the reaction. Columns can be produced in a robust way with very little ID, e.g. 5 to 15 μm, making them suitable for use in LC / MS proteomic analysis.
    WO 2004/064974 A2 describes a method for preparing a monolithic separation medium for liquid chromatography (LC) in ultrananoscale for use in capillary columns, or channels in microchipped devices, and capillaries prepared by the method. Applying a moderate overpressure to both ends of the capillary during the monolith polymerization process allows the production of monolithic capillary columns with very small ID, e.g. 25 μm and less, with increased mass transfer properties and low back pressures, as well as excellent reproducibility for column to column retention times. In a preferred embodiment, styrene was selected as monomer, tetrahydrofuran (THF) and n-octanol were selected as inert porogens, and divinylbenzene (DVB) was the crosslinker.
    Azobisisobutyronitrile (AIBN) served as a radical initiator. Other suitable crosslinkable monomers include methacrylates.
    US 7,473,367 B2 describes a method of making a monolithic chromatographic column by adding in a chamber a polymerization mixture containing a porogen and polymerizing the polymerization mixture in the chamber to form a monolithic polymer plug in the form of a chromatography column, wherein at least a part of the polymerization is carried out of a sufficient pressure on the polymerization mixture to prevent wall channel openings in the polymerized monolithic polymer plug and while the polymerization mixture is heated at a controlled elevated temperature. Examples of media for reverse phase chromatography are based on poly (styrene-co-divinylbenzene), poly (stearyl methacrylate-co-divinylbenzene) or poly (butyl methacrylate-co-ethylglycol dimethacrylate).
    Similar monolithic columns and methods for preparing them are described in WO 2006/017620 A2 and US 2010/0038298 A1. Yet very few monolithic products are commercially available, and their IDs are usually 0.1 mm or larger. It is difficult to produce monolithic columns with small ID, because the polymerization process and the precoating of the capillary tube seem to depend on the ID of the capillary. What appears to be a perfectly functioning solution in vials and even in capillary tubes with 0.1 mm ID therefore may not work at all with capillaries with an ID of 0.05 mm and less.
    An object of the present invention is to provide a process for producing an improved monolithic column which can have an ID of less than 0.05 mm and which can be used without inconvenience for sensitive separations of peptides and other small molecules.
    Summary of the Invention The above object is achieved by the method of the present invention which provides a capillary column or channel in a microfabricated device, which preferably has a small inner diameter with a homogeneous monolithic structure inside and which can be used for sensitive separation of peptides and other small molecules.
    According to the present invention, this has been achieved by carefully optimizing the overall polymerization process.
    More particularly, the present invention is designed for the production of monolithic columns (or channels) having an ID that is preferably less than 0.05 mm and is based on the selective use of (i) a specific combination of monomers, namely divinylbenzene (DVB) and iso decyl acrylate (IDA), (ii) a specific macroporogenic or macroporogenic mixture, namely isobutanol or isobutanol / octanol mixture, and, preferably, a "mild" procedure for silanizing the walls of the capillary column (or channel).
    One aspect of the present invention therefore relates to a method of making a separation capillary column, or separation channel in a microfabricated device, comprising the steps of: providing an unfilled quartz glass capillary column, or channel in a microfabricated device, etching the inner surface of the column or channel with an etchant, silanizing the inner wall of the column or channel with a silanizing agent, filling the column with a polymerization solution comprising monomers, at least one porogen and a polymerization initiator, polymerizing the mixture to form a rigid monolithic polymer plug in the column or channel, and usually washing the rigid monolithic polymer plug formed inside the column the channel to remove any remaining unreacted components, the process being characterized in that the monomers comprise a mixture of divinylbenzene as the main monomer and isodecyl acrylate, and that the porogen or porogens comprise isobutanol.
    In a preferred embodiment of the invention, the volume ratio of isodecyl acrylate to divinylbenzene is in the range of from about 1: 6 to about 1:40, preferably from about 1:10 to about 1:20.
    In another preferred embodiment of the invention, the porogen or porogens are selected from isobutanol and a mixture of isobutanol and octanol.
    In a further preferred embodiment of the invention, the capillary column, or channel in a microfabricated device, has an inner diameter (ID) of about 0.05 mm or less.
    Other preferred embodiments are set out in the subclaims.
    Another aspect of the present invention relates to a capillary column, or channel, in a microfabricated device obtainable by the method. A further aspect of the present invention relates to the use of a polymer monolith column, or channel in a microfabricated device, which can be obtained or produced by the process. Yet another aspect of the present invention relates to a polymerization composition comprising divinylbenzene, isodecyl acrylate and porogens in predetermined ratios.
    In the following, the invention will be described in more detail, reference being made to the accompanying drawings.
    Brief Description of the Drawings Figure 1 is a schematic diagram of an internally fabricated experimental arrangement for filling capillary columns with liquid in the preparation of polymer monoliths according to the invention.
    Figure 2 is a schematic diagram of a chromatographic instrument array with a short piece of polymer monolith having a 0.05 mm ID used as a trap column to enable injection at high fl velocity rates to shorten the sample injection time.
    Figure 3 shows two base peak intensity (BPI) chromatograms A and B, obtained by separating tryptic peptides from cerebrospinal fluid (CSF) samples on A: a commercial column, Acquity nanoUPLC (Waters, USA); and B: a polymer monolith column prepared by the process of the invention.
    Figure 4 is a corresponding BPI chromatogram as chromatogram B in Figure 3 of tryptic peptides from CSF on a 600 mm long polymer monolith column with 0.05 mm ID, prepared by the method of the invention, using a short piece of polymer monolith with 0.05 mm ID as a trap column (shown in Figure 2) to shorten the injection time. Figure 5 shows ion chromatograms for separation of two single charged species with m / z 416.2 separated on A: a commercial column, Acquity nanoUPLC (Waters, USA); and B: a polymer monolith column prepared by the process of the invention.
    Figure 6 shows chromatograms for separation of a single charged species with m / z 613.8 separated on A: a commercial column, Acquity nanoUPLC (Waters, USA); and B: a polymer monolith column prepared by the process of the invention.
    Figure 7 shows chromatograms for separating a large number of procyanidins from fruit extracts on a 600 mm long polymer monolith column with 0.05 mm ID, prepared by the method of the invention, using a stair column arrangement.
    Figure 8 shows base peak intensity chromatogram (BPI chromatogram) for tryptic peptides from CSF on a 600 mm long polymer monolith column with 0.03 mm ID, prepared by the method of the invention, at a fl velocity of the mobile phase of A) 100 nl / min, and B ) 200 nl / min.
    Detailed Description of the Invention As mentioned above, the present invention relates to a process for producing a monolithic capillary column, or channel in a microfabricated device, which is capable of extremely sensitive nanoscale separation of peptides and other small molecules, and which preferably has a small inner diameter (ID). about 0.05 mm or less.
    Before describing the invention in more detail, a general description of monolithic columns and their preparation is given below.
    Monolithic polymer column A monolithic chromatographic stationary phase consists of a single piece of highly porous material that does not contain interparticle cavities typical of packed chromatographic beds. Most of the pores inside the monolith are open and form a network of interconnected channels. In order to produce a monolithic capillary column, or channel in a microbial chip, of organic polymer, a quartz glass capillary is usually filled with a polymerization mixture containing appropriate amounts of a monomer, a crosslinking monomer, a polymerization initiator and a mixture of porogenic solvents. The capillary is closed at both ends, and the polymerization is initiated by heating or by ultraviolet (UV) radiation.
    Usually a dinitrile or azo initiator, such as AIBN, is used, which decomposes on heating to form free radicals. While the monomer in the polymerization mixture controls the polarity of the final monolithic material, the crosslinking agent and the porogenic solvent determine the pore size distribution.
    In contrast to conventional suspension polymerization, the synthesis of monolithic columns proceeds in an intact state. In the presence of porogenic solvents, the polymer cores begin to precipitate out of the mixture as a result of both the crosslinking process and the insolubility of the polymer in the solvent mixture. Eventually a monolithic system is formed with a pore volume fraction which approximately corresponds to the volume fraction of the porogens.
    The size and morphology of the pores depends on your factors, including the polymerization temperature, the polymerization kinetics and the solubility of the porogens for the resulting polymer. Solvents with good solubility for the polymer favor the formation of micro- and mesopores, while macropores are generated with solvents that interact only to a small extent with the polymer.
    To anchor the monolithic polymer body to the quartz glass wall, it is necessary to etch and silanize the capillary tube or channel before introducing the polymerization mixture. Otherwise, the column risks being displaced at high application pressures for the moving phase. Silanization is typically performed with γ-trimethoxysilylpropyl methacrylate (VMAPS) after treatment of the inner wall with aqueous sodium hydroxide solution.
    The Invention According to the present invention, accurate optimization of the overall polymerization process described broadly above makes it possible to produce polymer monolith columns having an ID of 0.05 or less, such as 0.03 or 0.02 mm, with increased sensitivity so that separation of even small peptides and other molecules is allowed. However, the process of the invention is not limited to such nanoscale type monolith columns but also involves the production of larger diameter monolith columns, including preparative scale columns which usually have inner diameters as large as 10-100 mm ID (the casting of porous monolith structures in these columns is likely to be cheaper than filling with particles).
    The process of the invention is based on filling the column with a polymerization mixture containing divinylbenzene (DVB) as main monomer in combination with a minor amount of isodecyl acrylate as comonomer, and isobutanol, or a mixture of isobutanol and octanol, as macroporogenic, preferably after silanizing the capillary column wall. with a relatively "mild" procedure, all under predetermined conditions. Thereby a homogeneous monolithic structure with sensitive separation properties can be produced.
    An example of how the inventive process can be performed will now be described: Preparation of a monolithic polymer column Arrangement for liquid filling To fill liquids in quartz glass capillaries, an arrangement of the type illustrated in Figure 1 and which will be described in more detail in the Experimental parts. Briefly, the set-up comprises an internally manufactured coupling of high pressure connections from SWagelokTM, whereby a Te fl on ferrule is used to attach a 10 mm glass tube containing the liquid and a PEEK sleeve (0.38 mm ID) is used to seal the capillary. Pressure (0.2-6 bar; 20-600 kPa) is applied with nitrogen flow from the side using a T-coupling. This arrangement is more robust and reproducible than the use of glass vials with a capillary sealing septum commonly used.
    Quartz glass capillary tubes with inner diameter 0.05 mm and outer diameter 0.36 mm are cut to the preferred length, e.g. l000 mm. The treatment and silanization of the wall of the quartz glass capillary is described in the literature, but is considerably modified according to the present invention as described below.
    Silanization Process 1. Fill the capillary with 2M NaOH and immerse the capillary in hot water, usually at about 65 ° C for about 5 minutes. 2. Rinse with water to neutral pH, then rinse with acetone. Filling the capillary with 10% γ- (trimethoxysilylpropyl methacrylate (VMAPS) in Xylene and immersing the capillary in hot water, usually at about 65 ° C for about 7 minutes 4. Rinse with acetone.
    Attachment of vinyl groups to the inner wall allows the monolith to be firmly attached to the capillary and thus prevents expulsion of the monolith from the high pressure mobile phase required for liquid chromatographic analysis.
    Polymerization process After silanization, the capillary is filled with a polymerization solution containing: 1. Monomers (divinylbenzene (DVB) and isodecyl acrylate (IDA)) 2. Porogens (octanol, isobutanol and chloroform or tetrahydrofuran) 3. Initiator (2,2'-azobisisobutyronitrile (AlI) , lauroyl peroxide or benzoyl peroxide).
    After filling, the outlet is closed with a piece of rubber, whereby the preferred pressure on the inside is maintained. Then the capillary is immersed in hot water (65-70 ° C) for 30- 120 minutes to start the heat-induced polymerization. All parameters are optimized and regulated very carefully. After the polymerization, the monolithic column can be rinsed using a high pressure acetonitrile stream. Thereafter, the column can be used for nanoscale peptide separations by liquid chromatography, preferably by mass spectrometry (M 5) detection.
    The silanization and polymerization steps will now be described more fully. Silanization As mentioned above, it is necessary to anchor the monolithic structure to the quartz inner wall to prevent expulsion upon application of the mobile phase at high pressure. This is achieved by etching / silanizing the inner wall of the capillary tube.
    In the present invention, the etching and silanization process is significantly improved to keep the quartz glass wall activated yet smooth, to prevent polymerization of the silanizing agent, γ-trimethoxysilylpropyl methacrylate, (VMAPS), and finally to prevent polymerization with a thick layer near the wall.
    Instead of high temperature (120 ° C) and long time (2 hours), which is usually used, the inventive process uses about 40-70 ° C, e.g. 65 ° C, and about 2-15 minutes, e.g. about 5 minutes or less, to etch with aqueous 2M NaOH instead of conventionally used 1M NaOH. This prevents unacceptable roughening of the wall. Flushing of the capillary is typically done with water and acetone.
    Silanization is performed with a solution of about 1-20% by volume, preferably about 10% by volume of VMAPS dissolved in Xylene, but without the addition of any free radical inhibitor (DPPH) which has been commonly used in the art. The silanization reaction is carried out at about 60-70 ° C, preferably at about 65 ° C, for about 2-15 minutes, e.g. about 7 minutes.
    This is in contrast to 120 ° C and 6 hours commonly used in prior art silanization. Flushing is done with acetone.
    This prevents polymerization of VMAPS and allows more controlled and limited silanization. It also prevents the porous monolithic polymer structure from forming a thick layer at the wall, and is thus formed with a similar morphology at the wall as in the remaining part of the monolith. Equally important, however, is that this mild silanization process is still sufficient to effectively anchor the monolith. This was proved by the fact that the monolith was not expelled from the capillary even upon application of a pressure of 10,000 psi (68950 kPa).
    Polymerization As mentioned above, free radical polymerization is commonly used using AIBN as the thermal initiator to produce porous polymer monoliths. Divinylbenzene (DVB) is readily available as an industrial chemical with 80% purity (which also contains about 19% ethylvinylbenzene) and has previously been used to prepare polymer monoliths for liquid chromatographic separations. Unless otherwise stated, the term DVB as used herein refers to this DVB of technical quality with 80% purity.
    Most reported work with porous monolithic polymer columns uses a monomer concentration, which typically includes DVB and styrene, of almost 40% by volume. In the present invention, by using mainly DVB in the polymerization mixture, it is possible to lower the total monomer concentration to about 30-35% by volume or even lower.
    Initially, using such a low DVB concentration, precipitation and inhomogeneous polymer formation were obtained when studying the polymerization in vials. This also resulted in voids and inhomogeneous monolithic structure within the capillary.
    Accordingly, various porogens were examined to effect a more homogeneous polymerization.
    When only octanol was used as the macroporogen, precipitation and inhomogeneous polymerization were observed. Upon addition of isobutanol to the polymerization mixture, a more turbid and homogeneous polymerization was observed in the vials.
    This was unexpected, as isobutanol is theoretically not a good solvent for polydivinylbenzene. One possible explanation is that isobutanol keeps the polymer in dispersion, which allows the aggregated polymer clusters to form freely in solution without premature precipitation. The concentration and ratio of octanol to isobutanol can be used to adjust the morphology and macroporosity of the monolith.
    Usually a mixture of 20-40% by volume, preferably 25-35% by volume of octanol and 20-40% by volume, preferably 25-35% by volume of isobutanol is used. Isopropanol and cyclohexanol may also be included as macroporogens.
    Usually a microporogen in the form of either chloroform, tetrahydrofuran or Xylene is used in a concentration of about 1-10% by volume, especially 5-10% by volume. It is known from the literature that the concentration of the microporogen can be used to control the mesoporosity of the monolith. According to the present invention, it was found that the addition of a second monomer, isodecyl acrylate (IDA), was effective in controlling the porosity of the monolith. Without isodecyl acrylate, large macropores were observed, and the monolith was not well suited for peptide separation. By adding only a small amount of isodecyl acrylate, such as 1-5% by volume, comprising about 1:10 or so compared to the DVB concentration, the pore size was significantly reduced.
    Accordingly, isodecyl acrylate is a critical microporogen in the present invention.
    It should be noted that DVB itself is a liquid and can act as a microporogen.
    In addition, copolymerization of DVB with isodecyl acrylate will introduce alkyl chains on the polymer surface, which helps to improve the separation of peptides.
    It is expected that DVB reacts faster than isodecyl acrylate and thus creates most of the crosslinked internal structure, while isodecyl acrylate may be more present at the surface.
    An important observation made is that the use of higher concentrations of isodecyl acrylate led to polymerization with more particle formation, ie a suspension of gel or particles or loose rubber, which resembled glue instead of the desired monolithic structure. Accordingly, isodecyl acrylate appears to be effective in altering the morphology of the monolith in a manner other than other microporogens, such as tetrahydrofuran or chloroform.
    Another interesting aspect of using isodecyl acrylate is the exceptionally low glass transition temperature (-60 ° C) for pure isodecyl acrylate homopolymer compared to other acrylates. This would suggest that isodecyl acrylate introduces a rubber-like copolymerization by reducing the chain stiffness of the overall polymer structure. Thus, a small amount of isodecyl acrylate in the polymer is likely to impart extra strength and stability to the monolith through a so-called gum-curing process. Rubber icing makes the polymer less brittle when loaded and is thus beneficial in preventing the monolith from breaking when the capillary is bent.
    A typical polymerization composition for use in the present invention comprises (wt%, w / w): DVB 20-40%, preferably 30-40% Isodecyl acrylate 1-15%, preferably 1-5% Isobutanol 20-40 %, preferably 25-3 5% Octanol 20-40%, preferably 25-3 5% Chloroform 1-15% (The same percentage range applies on a volume basis (volume / volume), except for chloroform where the range is 1-10% by volume. ) To the above composition, AIBN is added to a concentration of 0.15-1.5% by weight, and a ratio of AIBN to monomers of 0.5-5% by weight.
    The conditions for filling and polymerizing a porous polymer monolith within the limits of a very narrow quartz glass capillary are not trivial. The process of the present invention uses, as mentioned above, an increased pressure to fill the capillary with the polymerization mixture, preferably using a special device briefly described above (under the heading "Liquid filling set-up") designed for this purpose and which will be described in more detail in the Experimental part below. The optimal choice of pressure for the polymerization is of course a consequence of the viscosity of the polymerization mixture.
    Another important observation was the possibility that capillary forces and static electricity affected the polymerization mixture. At higher pressures, droplet repulsion was observed at the outlet of the capillary, i.e. droplets were drawn upwards on the outside, indicating charge transfer to the polymerization liquid flowing through the silanized capillary. By increasing the viscosity or using a lower pressure during filling, the repulsion decreased. It was expected that phase separation could also take place during filling due to capillary forces acting on the liquid.
    Consequently, the time required to fill the capillary homogeneously appears to be significant. Usually at least 30 minutes, and in some cases 60-120 minutes, can be used to fill the capillary to ensure a homogeneous content on the inside. It may also be appropriate to fill the capillary when immersed in a hot water bath to speed up the manufacturing process. The time, temperature, pressure and also knocking or shaking of the capillary during filling were identified as important parameters in the process of the present invention to ensure homogeneous and bubble-free filling before polymerization. It is also important to prevent undissolved initiator, pieces of quartz glass or other debris from entering the capillary.
    The filling pressure varies with the inner diameter of the capillary column. While, for example, 2 bar (200 kPa) may be used to fill a 50 μm capillary tube, 4 bar (400 kPa) may be required for a 30 μm tube, and 5 bar (500 kPa) for a 20 μm tube.
    After filling and closing the capillary outlet, the pressure can be further increased before the polymerization is started by increasing the temperature. The polymerization is usually carried out by immersing only the filled capillary in hot water (60-80 ° C), preferably at a temperature of 65-69 ° C, and a pressure from about 1 bar (100 kPa) to about 10 bar (1000 kPa). ).
    As mentioned above, the polymer monolith produced is not bound to be enclosed in quartz glass capillaries but can also be incorporated into other types of nanoscale separation devices, such as chip-based systems.
    In the following, the invention will be further elucidated with some non-limiting exemplary embodiments.
    EXPERIMENTAL PART Experimental array To fill liquids in quartz glass capillaries, an array illustrated in Figure 1 was used. In this array, a quartz glass capillary coil 1 is attached to a test tube 2, here 100 X 10 mm outer diameter, containing liquid 3, via an internal manufactured coupling of SWagelokTM high pressure connections. More precisely, the tube 2 is attached to a SWagelokTM 10 mm to 1/8 ”connector 4 and attached with a 10 mm ferrule of TeflonTM. This connector 4 is in turn via a pipeline 5 with 1/8 ”outer diameter of stainless steel attached to a SWagelokTM T-coupling 6. The latter is attached to and seals the quartz glass capillary 1 with 0.36 mm outer diameter via a SWagelokTM 1/8 "To 1/16" connector, to which a sleeve of PEEK with 1/16 "10 15 20 25 30 16 outer diameter and 0.38 mm inner diameter is connected with a 1/16" ferrule of PEEK (not shown). A line 7 connects the T-coupling 6 to a source of compressed nitrogen gas (not shown) via a stop and outlet valve 8 through Which nitrogen pressure of 0 to 10 bar (0 to 1000 kPa) can be applied. In the illustrated case, the quartz glass capillary 1 is closed with a rubber stopper 9 and immersed in a thermostated water bath 10.
    Preparation of polymer monolith columns 600 mm long column with 0.05 mm ID A 600 mm long polymer monolith column with 0.05 mm ID was prepared by following the procedure described below. ø (Wear safety goggles for personal safety) 0 Approximately 940 mm length of quartz glass capillary is cut and inserted into the PEEK sleeve and pushed through the pressure connections. The inside (glass tube side) is inspected with a microscope for debris, and in the presence of such makes a new cut. The test tube containing 2M NaOH is attached by tightening the TeflonTM ferrule and lowering the capillary. Pressure is applied (2 bar; 200 kPa) gauge pressure), and after 5 minutes of flushing, the capillary coil is immersed in a thermostated water bath (65-68 ° C) for 5 minutes, during which the flow can be left on. The capillary coil is then lifted out of the water bath, the pressure connection is ventilated and the glass tube is removed and replaced with a tube containing purified water (18 MOhm). The capillary is flushed for 5 minutes at 2 bar (200 kPa), then ventilated and flushed using the glass tube with acetone for 5 minutes at 2 bar (200 kPa). The pressure connection is then ventilated and a glass tube containing 10% VMAPS in Xylene is attached. The capillary is flushed for 5 minutes at 2 bar (200 kPa), and the spiral column is immersed in the thermostated water bath (65-68 ° C) for 7 minutes, leaving fl fate on. The capillary coil is lifted out of the water bath, the pressure connection is vented, and the glass tube is removed and replaced with a tube containing acetone. The capillary is flushed for 5 minutes at 2 bar (200 kPa). The polymerization mixture is prepared by adding 15.5 mg of AIBN to a glass tube, after which 850 μl of divinylbenzene, 90 μl of isodecyl acrylate, 90 μl of chloroform, 10 μl of 800 μl of octanol and 800 μl of isobutanol are added. Weighing between the additives allows documentation of the exact work composition. The glass tube is mixed with vortex mixer for 1 minute, sonicated for 5 minutes and finally mixed with vortex mixer for 1 minute. Care must be taken to ensure that there is no debris or residual AIBN. The pressure connection is then ventilated and the glass tube containing the polymerization mixture is fixed. The capillary is flushed for 5 minutes at 2 bar (200 kPa) at room temperature, and the capillary coil is immersed in the thermostated water bath (68 ° C) for 10 minutes for efficient hot flushing (the flow is left on). The capillary outlet is then lifted out of the water bath and closed securely by inserting the capillary 4-5 mm into a rubber stopper or septum. The entire capillary coil is then immersed in the water bath for polymerization to take place over a period of 40 minutes. The time required for polymerization has been found to be entirely dependent on the concentration of AIBN. As a guide, concentrations of AIBN relative to monomers of 1.25, 1.75 or 2% by weight may require polymerization times of 80, 40 and 30 minutes, respectively. However, this relationship can be changed with variation in the polymerization mixture and temperature, with the purity of AIBN, with the quartz glass capillary ID or with other parameters. After the polymerization, the capillary is taken out of the water bath, the pressure connection is ventilated and the capillary is cut below the immersion level. Approximately 650 nm of the capillary should be polymerized. This capillary is attached to a 360 μm high pressure connection (IDEX) for quartz glass with nano-liquid supplied from the injector with a quartz glass capillary with 20 μm inner diameter and 360 μm outer diameter. The polymer monolith column is purged with acetonitrile for about 30 minutes at 6000 psi (41370 kPa), then for about 30 minutes using a leaching rate of 400 nl / min. The polymer monolith is then ready for use as a liquid chromatography column and can be cut to a length of 600 mm. A length of 50 mm can be used as a trap column. 600 mm long column with 0.03 mm ID A 600 mm long polymer monolith column with 0.03 mm ID was prepared in the same way as described above for the column with 0.05 mm ID but with increased pressure correspondingly from 2 to 4 bar (200 to 400 kPa) for all operations. Using the procedures described above, five monolithic polymer columns were prepared using the compositions and conditions set forth for Examples 1 to 5 in Table 1 below, namely three columns with 0.05 mm ID (Examples 1-3), one column with 0, 03 mm ID (Example 4), and a column with 0.02 mm ID (Example 5).
    TABLE 1 Example number 1 2 3 4 5 Quartz glass capillary ID (mm) 0.05 0.05 0.05 0.03 0.02 Length (mm) 940 940 940 940 940 Volume isobutanol (ml) 0.8 0.8 .8 0.8 0.8 Volume of octanol (ml) 0.8 0.8 0.8 0.8 0.8 Volume of chlorotorm (ml) 0.09 0.18 0.09 0.09 0.09 Volume of isodecyl acrylate (ml) 0.09 0.07 0.09 0.09 0.09 Volume 80% divinylbenzene technical grade (ml) 0.9 0.8 0.85 0.85 0.85 Estimated composition of isobutanol (% vol / vol) 29.85 30.42 30.42 80.42 30.42 Estimated composition of octanol (% vol / vol) 29.85 30.42 30.42 30.42 30.42 Estimated composition of chlorotorm (% vol / vol) 3.38 8.08 3.42 3.42 3.42 Estimated composition of isodecyl acrylate (% vol / vol) 3.38 2.88 3.42 3.42 3.42 Estimated composition divinylbenzene 80% technical quality ( % v / v) 33.58 30.42 32.32 32.32 32.32 Measured weight azoisobutyronitrile, AIBN (mg) 18.3 10.3 15.5 15.5 15.5 Measured weight isobutanol (mg) 872 .7 853.52 881.5 881.5 881.5 Measured weight octanol (mg) 898.2 877.35 890.38 890.38 890.38 Measured weight chlorolorm (mg) 148.8 281.79 148.85 148.85 148.85 Measured weight isodecyl acrylate (mg) 91.4 78.31 87.03 87.03 87.03 Measured weight divinylbenzene 80% technical quality (mg) 815 737.01 782, 17 782.17 782.17 Total weight of all components (mg) 2440.2 2418.28 2405.23 2405.23 2405.23 Estimated composition of azoisobutyronitrile, AIBN (% w / w) 0.75 0.43 0.84 0.84 0.84 Estimated composition of AlBN relative to monomers (% w / w) 1.98 1.25 1.75 1.75 1.75 Estimated composition of isobutanol (% w / w) 27.57 27.18 28, 52 28.52 28.52 Estimated composition of octanol (% w / w) 28.53 28.15 28.89 28.89 28.89 Estimated composition of chloroorm (% w / w) 8.01 10.88 8, 22 8.22 8.22 Estimated composition of isodecyl acrylate (% w / w) 3.75 3.17 3.84 3.84 3.84 Estimated composition of divinylbenzene 80% technical quality (% w / w) 33.40 30.83 32.73 32.73 32.73 Nitrogen pressure during tilling and polymerization measured as gauge pressure (bar) 2.0 2.0 2.0 4.0 5.0 Filling and polymerization temperature (° C) 88.4-89.2 85, .5-88.1 88.4-87.1 88.7-88.8 88.8-88.9 Filling time (min) 10 18 8 10 10 Polymerization time (min) 21 81 40 41 31 612 10 15 20 25 30 35 20 Separation experiments Separation of tryptic peptides from cerebrospinal fluid (CF S) A monolithic polymer column, prepared as described above using a similar composition and conditions given for Example 2 in Table 1, was applied to separate peptides from tryptic digestion of cerebrospinal fluid (CSF). The sample was injected using a loop injector (loop size 2 μl) mounted as Standard Equipment on a commercial nano-UPLC system (Waters, USA).
    Injection: 2 ul at 400 nl / min 0-19 min Flow: 200 nl / min 20-70 min Movable phase: A) 0.1% formic acid B) 0.1% formic acid in acetonitrile Gradient: 2% B 0-20 min 30% B 50 min 70% B 60 min The result is shown in Figure 3, chromatogram B.
    For comparison, the same sample was also separated on a commercial 150 mm long nanoAcquity column with 0.075 mm inner diameter (Waters, USA), packed with 1.7 hr particles. In this case, a trap column was used to accelerate the injection, so elution of peptides occurred about 20 minutes earlier than with direct injection on the polymer monolith.
    Injection: 2 ul at 10 ul / min (trap column) Flow: 300 nl / min Moving phase: A) 0.1% formic acid B) 0.1% formic acid in acetonitrile Gradient: 2% B 0-2 min 30% B 30 min 80% B 40 min The result is shown in Figure 3, chromatogram A. 10 15 20 25 30 21 To shorten the injection time for the separation in chromatogram B in Figure 3 (approximately 20 min), using a higher fl velocity rate during the sample injection, was constructed an arrangement shown in Figure 2 containing a trap column.
    Here, a trap column of polymer monolith 20 in the form of a short piece of the polymer monolith with 0.05 mm ID is arranged as an analytical column between the injector 21 and the analytical capillary column 22 via a capillary 23 (20 μm ID), a connection 29 and a T-coupling 24, which is also connected to an outlet 25 via a capillary 26 (20 μm ID). The analytical column 22 is further connected via a nanoelectrospray emitter 27 (Pico-Tip®) to a Q-TOF mass spectrometer.
    High voltage is applied to the liquid via through the T-coupling 30. The outlet 25 is connected to the spill 28 at the time of injection, 3-5 pl / min (4000 - 6000 psi; 27580 - 41370 kPa), and plugged after the injection to lead the till to the analytical column 22.
    This is similar to the standard layout for the commercial Acquity nanoUPLC columns (Waters, USA). Various low volume compounds were used and dead volumes were minimized at each point. The cut ends of both the transport capillary and the polymer monolith capillary were observed with a microscope before coupling.
    Tryptic peptides from CFS were injected at high fate on this trap column and further separated on the 600 mm long polymer monolith with 0.05 mm ID.
    Since the analytical fl velocity rate was as low as 200 nl / min, the time for the gradient to reach the column should be quite long. Therefore, the gradient was started using a higher fl velocity (400 nl / min) for 9 min, thus placing the gradient in the residence volume in front of the column before setting the fl velocity of 200 nl / min.
    Injection: 2 μl at 3 μl / min for 5 min / (trap column) Movable phase: 0.1% formic acid B) 0.1% formic acid in acetonitrile Flow 400 nl / min 1-9 min 200 nl / min 10- 50 min 10 15 20 25 30 22 Gradient: 2% B 0-1 min 8% B 8 min 10% B 10 min 30% B 30 min 80% B 40 min The result is shown in Figure 4.
    Comparison of peak profiles For comparison of peak profiles, ion chromatograms were taken for different peptide masses. Figure 5 shows the separation of two single charged species with m / z 416.2 separated on A) commercial Acquity nanoUPLC (Waters, USA), and on B) a polymer monolith prepared as described above. Figure 6 shows the corresponding separation of a single charged species with m / z 613.8 separated on A) Acquity nanoUPLC, and on B) polymer monolith prepared as described above.
    Separation of procyanidins Using a 600 mm long polymer monolith column with 0.05 mm ID, prepared as described above, a selection of procyanidins extracted from fruits were separated and detected by mass spectrometry using a trap column array. The result is illustrated in Figure 7.
    Separation of tryptic peptides from cerebrospinal fluid (CSF) with 600 mm long polymer monolith column with 0.03 mm ID Separation of CSF was performed with a 600 mm long polymer monolith column with 0.03 mm ID, prepared as Example 4 in Table 1 above. Separation of the same sample of tryptic peptides from CSF as above was performed at a lethal phase velocity of 100 nl / min and 200 nl / min. The results are shown in chromatograms A and B, respectively, in Figure 8.
    The present invention is not limited to the preferred embodiments described above. Various alternatives, modifications and equivalents can be used.
    The embodiments described above should therefore not be construed as limiting the scope of the invention, which is defined by the appended claims.
    权利要求:
    Claims (19)
    [1]
    A process for producing a separation capillary column, or separation channel in a microfabricated device, comprising the steps of: providing an unfilled quartz glass capillary column, or channel in a microfabricated device, etching the inner surface of the column or channel with an etchant, silanizing the column wall or channel with a silanizing agent, filling the column with a polymerization solution comprising monomers, at least one porogen and a polymerization initiator, and polymerizing the mixture to form a rigid monolithic polymer plug in the column or channel, characterized in that the monomers comprise a mixture of divinylbenzene as main monomer and isodecyl acrylate said at least one porogen comprises isobutanol.
    [2]
    The method of claim 1, wherein the capillary column, or channel of a microfabricated device, has an inner diameter of about 0.05 mm or less.
    [3]
    The method of claim 1 or 2, wherein the ratio of isodecyl acrylate to divinylbenzene is in the range of from about 1: 6 to about 1:40 (v / v), preferably from about 1:10 to about 1:20 (v / v). / vol.).
    [4]
    A process according to claim 1, 2 or 3, wherein said at least one porogen is selected from isobutanol and a mixture of isobutanol and octanol.
    [5]
    A process according to any one of claims 1 to 4, wherein the total monomer concentration in the polymerization solution is in the range from about 20% to about 50% by volume, preferably from about 30% to about 40% by volume.
    [6]
    A process according to any one of claims 1 to 5, wherein the concentration of isodecyl acrylate in the polymerization solution is in the range from about 1 to about 15% by volume, preferably from about 1 to about 5% by volume.
    [7]
    The method of any one of claims 1 to 6, wherein the porogens further comprise at least one microporogen selected from chloroform, tetrahydrofuran and Xylene. 10 15 20 25 30 35 24
    [8]
    A process according to any one of claims 1 to 7, wherein the silanization is carried out at a temperature of from about 40 to about 70 ° C for from about 2 to about 15 minutes.
    [9]
    The method of claim 8, wherein the silanizing agent comprises 1 to 20% by volume of V- (trimethoxysilyl) propyl methacrylate.
    [10]
    A method according to any one of claims 1 to 9, wherein the etchant is an aqueous solution of sodium hydroxide at a concentration of 0.5 to 2 M and the etching is carried out at a temperature of from about 40 to about 70 ° C.
    [11]
    A process according to any one of claims 1 to 10, wherein the polymerization is carried out at from about 60 to about 80 ° C and a positive pressure from about 1 to about 10 bar (about 100 to about 1000 kPa).
    [12]
    The process of claim 11, wherein the polymerization is carried out for about 20 to about 120 minutes.
    [13]
    A process according to any one of claims 1 to 12, wherein the polymerization initiator is 2,2'-azobisisobutyronitrile (AIBN).
    [14]
    Separation capillary column, or separation channel in a microfabricated device, obtainable by the method according to any one of claims 1 to 13.
    [15]
    Separation capillary column, or a microfabricated device comprising one or more channels, wherein the column, or at least one channel in the microfabricated device, has been filled with a monolithic polymer by the method according to any one of claims 1 to 13.
    [16]
    Use of a separation capillary column, or separation channel in a microfabricated device, according to claim 14 or 15 for nanoscale peptide separation.
    [17]
    Use of a separation capillary column, or separation channel in a microfabricated device, according to claim 14 or 15 for preparative peptide separation. 25
    [18]
    A polymerization composition comprising: 20-40% by volume divinylbenzene, preferably 30-40% by volume, 1-15% by volume isodecyl acrylate, preferably 1-5% by volume, 20-40% by volume isobutanol, preferably 25-35% by volume %, 20-40% by volume of octanol, preferably 25-35% by volume, 1-10% by volume of chloroform.
    [19]
    The polymerization composition of claim 18, further comprising 0.15-15.5% by weight of 2,2'-azobisisobutyronitrile (AIBN).
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    同族专利:
    公开号 | 公开日
    JP6193375B2|2017-09-06|
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    EP2900365A1|2015-08-05|
    SE537053C2|2014-12-16|
    CA2922825A1|2014-02-27|
    US20150299409A1|2015-10-22|
    CN104902993B|2017-09-08|
    JP2015531070A|2015-10-29|
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    法律状态:
    2021-03-30| NUG| Patent has lapsed|
    优先权:
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    SE1250948A|SE537053C2|2012-08-23|2012-08-23|Process for the preparation of monolith columns|SE1250948A| SE537053C2|2012-08-23|2012-08-23|Process for the preparation of monolith columns|
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    CA2922825A| CA2922825A1|2012-08-23|2013-08-23|Method for the preparation of monolithic columns|
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