Patent Application
20220184528
The present invention relates to the area of separation, such as recovery of analytes, and provides tools and methods for making sample preparation more efficient. More specifically, the invention relates to a microelution column; a plate including one or more such columns; and a sample preparation method that enables the use of smaller elution volumes.
Microelution techniques were developed primarily to address the need for a reduction in solvent use, and also in the size of extraction instrumentation. Typically, in such methods, the volume of the extracting phase is very small in relation to the volume of the sample, washing buffer and elution buffer.
Most commercially available microelution type plate products operate with elution volumes of 50 μL and larger. Often elution volumes are applied in two equal aliquots to recover materials from bed mass of 2 and 5 mg of material. One reason large elution volumes are used is to prevent low and/or inconsistent recovery of the analyte species from the column beds of the plate. There are several causes of low or inconsistent recovery. The column may channel due to non-uniform bed packing. Liquid flow may channel through the bed of the column leaving resin in the column or portions of the bed incompletely reacted untouched by sample, washing and/or elution solutions. Poor or inconsistent flow in any of these steps may require large buffer volumes, especially in the washing and elution steps, to ensure that all column media is contacted and reacted by the solvents/buffers. As the column bed size is decreased, uniformity of the packed bed is more difficult to achieve.
Any column used in top-down flow of a microelution column may contain air trapped or partially trapped in the bed of the column. In fact, this is an artefact on how plates operate and is part of standard practice. Air may unintentionally be introduced simply by the continuous top pressure, or bottom vacuum, applied to the column even after liquid has exited the bed.
Another way that air is unintentionally introduced to an adsorbent bed is by an air gap process. An “air gap” is the air trapped between the top of the column bed and the slug of liquid introduced to the top of the column bed. With an air gap present, as the liquid on top of the air gap is forced through the column by pressure at the top of the column bed or vacuum at the bottom of the column, air will be forced through the column bed. This may result in air being partially and unpredictable retained in the column bed.
This kind of undesired air in the column bed is known as entrained air. Air may be introduced in any of the liquid flow steps of conditioning, sample loading, sample washing or sample elution. Air in the bed can interrupt the flow of liquid so that flow through the column is neither consistent nor predictable, e.g. due to channeling of the flow. It can also change the flow rate of liquid flowing through the column. A plate based column may contain large dead volumes that must be cleared with the introduction of any buffer step. In this situation, large elution volumes will be required to give multiple chances of eluting and recovering the analytic species of interest while smaller elution volumes result in low recovery of material and also an inconsistent from column-to-column recovery of materials.
In the field of sample preparation, there exists a need to improve consistency of recovery as well as the mass recovery of analytes from plate type solid phase extraction columns. There is also a need for small elution volumes while maintaining complete mass recovery of the analyte from the resin in the plate type columns. As explained above, there exists a need to reduce the amount of entrained air in the column beds of a plate, and there is a need to avoid introducing air into the column beds of a plate. Finally, there exists a need to avoid the air gap when introducing liquid into the column beds of a plate.
WO 2005/070141 (Phynexus, Inc.) relates to extraction columns for the purification of an analyte, such as a peptide, protein or nucleic acid. The described columns may be characterized by low backpressure in use, and in some embodiments, it is stated that elution of analyte in a small volume of liquid may be obtained.
The column bodies may be made from a wide range of materials, such as plastic, glass, ceramics or metals. Further, the extraction columns include one or two frits, such as membrane screens, which may be characterized by low pore volume. The polarity of the membrane screen can be important a hydrophilic screen will promote contact with the bed and promote the air-liquid interface setting up a surface tension; while a hydrophobic screen would not promote surface tension and therefore the threshold pressures to flow would be different.
U.S. Pat. No. 4,779,467 (Rainin Instruments Co., Inc.) relates to a liquid-end assembly for multichannel air-displacement pipettes having a modular construction, which enables individual components to be easily replaced when they become contaminated or worn. The assembly also enables selected piston and cylinder components to be selectively removed so that a number less than all of the channels can be employed for pipetting without first stabbing tips and then removing by hand or rearranging the tip array. More specifically, this is achieved by the liquid-end assembly further comprising modular piston means comprising a cylindrical rod having a first end and a second end, wherein the piston means comprises spring capturing means disposed proximate the first end of the rod.
US 2018/0252687 (Tecan) relates to microcolumns for extraction of an analyte from a liquid sample, and particularly extraction of an analyte from biological fluids. More specifically, an objective of US 2018/0252687 is to provide an extraction device which improves process throughput, removes a very high percentage of an analyte from a sample, is transportable, storable without damage, and inexpensive. It is also desirable that such device be compatible with existing automated equipment, and not leach into the biological or other fluid samples the eluent liquid or any compound that could interfere with the analytical results. Likewise, it is desirable to minimize the media bed volume and associated dead volumes to lower the volume of the wash eluent liquid.
According to US 2018/0252687, this can be achieved by an apparatus comprising a first microcolumn comprising a first passage, a flow distributor layer extending across the first passage; and a second microcolumn comprising a second passage, an extraction layer extending across the second microcolumn; wherein, the first microcolumn positioned above and in series with the second microcolumn with the first passage in fluid communication with the second passage.
US 2018/0238842 (Showa Denko) relates to a liquid chromatographic column and a liquid chromatographic apparatus including the same. More specifically, according to US 2018/0238842, an example of problems related to continuous use is that the filter of a column may become clogged with an injected sample component or impurities injected with the sample component, and pressure applied to the system may exceed the limit of an apparatus, which leads to analysis failure.
In order to deal with such problems, US 2018/0238842 describes a liquid chromatographic column comprising a cylindrical column body; an inflow-side filter that is disposed at an eluent inflow-side end of the column body; an outflow-side filter that is disposed at an eluent outflow-side end of the column body; and a filler that is filled between the inflow-side filter and the outflow-side filter, wherein the inflow-side filter has a two-layer structure consisting of a first resin filter member and a second resin filter member which are disposed in this order from a side of the filler, and the first resin filter member has an indentation elastic modulus lower than that of the second resin filter member.
Despite the products and art available, there is still a need in the area of sample preparation, and specifically in the area of solid phase microelution, for more efficient methods allowing fast analysis with as little use of liquids and reagents as possible, especially in automated parallel processing of multiple samples.
One aspect of the invention is a microelution column comprising a column body including a bottom frit and a top frit, wherein the column body includes adsorbent arranged between the bottom frit and the top frit, and an optional filter frit arranged above the top frit, wherein the top frit and/or the bottom frit has a pore volume of about 0.2 ρL. Further, the pore diameter of the the bottom frit may be smaller than that of the top frit.
Another embodiment of the invention is a microelution column comprising a column body including a bottom frit and a top frit, wherein the column body includes adsorbent arranged between the bottom frit and the top frit, without the presence of a filter frit.
Another aspect of the invention is a plate for parallel processing of samples, which includes a plurality of positions into which one or more columns according to the invention have been arranged.
A further aspect of the invention is a method of preparing a sample for subsequent analysis, wherein an aliquot of elution solvent in the range of 1-50 μl is applied to the top of the column according to the invention.
Further details, advantages and embodiments of the present invention will appear from the dependent claims as well as from the detailed description below.
The term “ microelution” is used herein in its broadest sense including small volume elution from extraction columns as the final step to recover desired materials.
The term “column” is used herein in its conventional meaning in the area of sample preparation that is a chamber arranged to receive an adsorbent.
The term “adsorbent” is used herein include a material whereby material are adsorbed to a solid phase media, normally a higher surface material. Adsorbent is sometimes referred to as the bed, or a resin.
The term “frit” as used herein in its conventional meaning in the area of sample preparation, i.e. for a porous material arranged for holding extraction media in place in a column. The frits are sometimes referred to herein as ‘screens’.
The term “filter frit” as used herein is a screen, membrane or frit material positioned above the inlet frit to remove particulate material from the liquid entering the column bed.
The term “solid phase extraction” as used herein is defined as a sample preparation process by which compounds that are dissolved or suspended in a liquid mixture are separated from other compounds in the mixture by adsorption to column media according to their physical and chemical properties.
The term “elution volume” as used herein is defined as the volume of elution liquid, sometimes known as desorption liquid, into which the analytes are desorbed and collected.
The term “biomolecule” as used herein refers to molecules derived from a biological system, such as proteins, peptides, and nucleic acids.
As appears from the above, the present invention relates to a method and an apparatus for the low i.e. small volume elution and recovery of materials e.g. from a solid phase extraction plates.
In a first aspect, as exemplified e.g. in
The columns of the invention are advantageously used in a plate format, advantageously for parallel processing in a top-down flow format when arranged in the plate. Thus, the flow through such a column of the invention will be applied from the top to the bottom.
Alternatiely, the columns may used as pipette tip columns, for example in a back and forth flow tip column format or in conventional pipetting.
To improve their use in the plate format, as exemplified e.g. in
Further, to prevent or at least substantially reduce its movement in X-direction when arranged in a plate, as exemplified e.g. in
Advantageously, the adsorbent 5 has been loaded in a volume that substantially avoids or at least minimizes void volume below the top frit 4, i.e. between the top frit and the adsorbent 5. Differently worded, in order to avoid the above-discussed problem of air entrainment, the loading of the adsorbent into the space between the bottom frit 3 and the top frit 4 is performed to minimize any free space or air. Thus, the adsorbent 5 is may be provided as a packed bed, rather than a fluidized bed. In one embodiment, the present invention does not allow free movement of adsorbent particles below the top frit 4; or at least substantially reduces any such movement to degree which has no impact on the column performance.
The bottom frit 3 may be of low porosity, such as the frits described in the above-discussed WO 2005/070141. In some embodiments, the pore volume of the frits may be 0.2 μL and smaller. Further, the bottom frit 3 may be water-wettable, i.e. substantially hydrophilic. To enable advantageous addition of sample, as will be discussed in more detail below, the top frit 4 may be water-wettable, i.e. substantially hydrophilic. The column body 2, or at least the inside of the column body, may be hydrophobic, or at least substantially hydrophobic. However, as an alternative that changes certain properties and performance, the inside of the column body 2 may be water-wettable i.e. substantially hydrophilic.
A column according to the invention may be configured for top-down column flow, in which case the filter frit 6 is configured to enable the removal of large particles such as contaminants originating from biological samples. In this context, it is understood that the term top-down flow is understood to mean the position of the column in conventional use in a plate, or as a pipette tip.
As appears from
In columns of the invention, the dead volume (i.e. the interstitial volume of liquid held in the filter pores) of the filter frit is in the range of 0.05 μl-5 μl. In some embodiments, the dead volume is in the 0.05 μl-2 μl. In some embodiments, the dead volume is in the 0.1 μl-1 μl.
The skilled person may select suitable porosity and other dimensions of the bottom, top and filter frit depending e.g. on the nature of the sample and the purpose of the microelution.
In another aspect of the invention, the invention relates to a plate 10 suitable for parallel processing of samples, which includes a plurality of positions 11 into which one or more of the columns according to the invention have been arranged.
Advantageously, each well of such a plate will comprise means 12 to engage with the annular ridge 7 of each column. Further, the plate of the invention may comprise means arranged to receive two or more flat surfaces 9 arranged in the upper part of each column, such as in or with a collar 8, as exemplified in
As appears from the above, the plate of the invention may be an interchangeable plate with optional removable pipette tip columns. The plate of the invention may be constructed to receive a plurality of columns arranged in parallel where the columns may be removed and used as tip columns. In one embodiment, the plate operates in a 96 column format in an 8×12 row configuration. Microelution of columns of the plates may be accomplished by controlling the frit polarity and plastics.
As discussed briefly above, the columns of the invention may be a combination of components that include water-wettable screen frits and optional water wettable polymer wall. In some embodiments of the invention non water wettable polymer screen frits may be used including polyethylene terephthalate (PET), polypropylene (PP), polyether ether ketone (PEEK), polyethylene naphthalate (PEN), polytetrafluoroethylene (PTFE), polyvinylidene fluoride (PVDF), polybutylene terephthalate (PBT) and others.
The frits of the invention have pore size and porosity. The pore size or pore diameter is the effective opening in the frit that will allow materials of the defined pore size to pass through or mostly pass through the frit. The frit is constructed with polymer threads or other polymer material causing these areas to be closed i.e. not porous. The porosity of the frit is defined by the amount of open area of the frit from the pores divided by the total area multiplied by 100.
In some embodiments of the invention, the pore size or diameter of the bottom outlet frit is smaller than the top or inlet frit. It was discovered that samples containing particulate material could plug the fits and flow through the column would be limited or stopped. Sample particles that were larger than the top frit pore size would remain on top of the column bed. However, sample particles that were smaller than the pore size of the top frit would pass through and may lodge in the column. If the particles lodged in the pores of the bottom frit, flow through the column could be reduced and even stopped. In some embodiments of the invention, it was discovered that particles from the sample that passed through the top frit could be prevented from plugging the column by decreasing the pore size of the bottom frit relative to top frit. In these samples, particles that passed through the column would not lodge or plug the lower outlet frit and flow would not be impeded.
The columns are constructed and used to avoid air gaps with the introductions of liquids, especially low volume liquids to the top of the column. If air becomes entrained in the column, hydrophilic fits on both ends of the column and low dead spaces within the column allow the expulsion of much of the air with the introduction of the next liquid volume. The plate is a true low volume plate format that can optionally be a flexible plate/tip format. More than 90% of the elution volume introduced into the column bed may be recovered, even with elution volumes less than 50, 45, 40, 35, 30, 25, 20, 15 and even 10 μL for a 2 mg mass column bed. More than 90% of the elution volume introduced into the column bed may be recovered, even with elution volumes less than 50, 45, 40, 35, 30, 25, 20, 15, 10 and even 5 μL for a mass column bed in the range of 0.2-2 mg. More than 90% of the elution volume introduced into the column bed may be recovered, even with elution volumes less than 50, 45, 40, 35, 30, 25 and even 20 μL for a mass column bed in the range of 2-20 mg.
The bed mass of columns located in the columns of the plate may be in the 2, 5, 10 or 20 mg range. The bed mass of columns located in a 96 column plate may be in the 0.1-10 mg and the 0.2-5 mg ranges.
Columns of the invention allow the removal of air gap so that introduction of air in the column bed can be avoided. In one embodiment this is accomplished by the frit and column wall being hydrophilic so that liquid added slides down the wall and the column and covers the frit not allowing air to enter the column bed. In another embodiment this is accomplished by having a hydrophilic frit and dropping liquid into the bed where the diameter of the drop is less than the diameter of the column above the frit. In another embodiment this is accomplished by depositing the drop of liquid so that the bottom of the drop touches and covers the hydrophilic frit.
In a further aspect, the invention relates to a method of preparing a sample for subsequent analysis, wherein at least one sample having a volume in the range of 100-400 μl is applied to a column according to the invention.
Low or micro elution volumes are possible with plates of the invention. Thus, the sample may applied to a column 1 loaded with adsorbent 5, and elution may be performed in a subsequent step by applying an eluent having a volume in the range of 1-50 μl. For example, columns in the mass weight of 2-5 mg of adsorbent weight may be eluted in elution volumes of 50 μL and below, where the ratio of elution volume/recovery volume is in the range of 0.9-1.0.
The method may be a top-down column flow method, wherein the sample is applied to filter frit 6.
Alternatively, the method is a pipetting method, wherein the sample is aspirated and passes the bottom frit 3 to contact the adsorbent 5 arranged between the bottom frit 3 and the top frit 4.
In some embodiments, high pressure is used to force liquid through the column in the plate. This high pressure serves to remove entrained air that may be contained in the bed thus improving the contact of liquids to the media contained in the column beds. However, high pressures also serve to increase dramatically the liquid flow rate and the linear velocity of liquid through the bed. Pressures of 2-30 psi, 3-25 psi, 4-20 psi, 5-15 psi and 5-10 psi may be used in plates of the invention while retaining capture of the molecules to the solid phase media. It is surprising that these high pressure ranges can be used in the column plates of the invention because high linear velocity normally will limit capture of molecules due to slow capture kinetics.
In one embodiment of the invention, columns and plate of the invention with columns in the sorbent mass weight range of 2-5 mg for an individual column bed; elution may be performed with less than 50 μL elution volumes with recoveries of analytes in the 90-100% range. In another embodiment of the invention, for elution volumes less than 50 μL the ratio of applied elution volume/recovered volume is in the range of 0.9-1.0. In another embodiment of the invention, for elution volumes less than 50, 45, 40, 35, 30, 25, 20 and 15 μL the ratio of applied elution volume/recovered volume is in the range of 0.9-1.0. Less than 50 μL elution volumes applied to the top of the columns in the plate of the invention allow complete flow of the volume bed and is not trapped by dead spaces that may be contained within the column bodies, beds or fits. Surprisingly, even with entrained air in the bed of the columns of the invention, these small elution volumes can be used and recoveries up to 90-100% may be achieved.
The columns are designed to be able to add elution volumes of less than 50, 40, 30, 25, 20, 15, 10 and 5 μL to the top frit of the column without introducing an air gap to the top of the column.
The plate containing columns may be configured into an 8×12 (96 column) format but the plate is not limited to this configuration. Plates of the invention can have any number of rows and columns. The plate can be processed in a 96 well plate type format. In some embodiments of the invention, the columns may not be removed from the plate format. In some embodiments, the tip columns may be removed from the plate and can be processed in 1-2, 1-4, 1-8, 1-12 or 1-96 pipette pump format. Pipette tip column from the plate of the invention may be process in 2, 4, 8 multichannel pipette format. In some terminology columns may be referred to as wells or column wells within a plate format. However, the column well must retain the format having a bottom or outlet frit, a top or inlet frit and media contained within these two frits.
The elution volumes may be as low as 25-50 μL, 20-50 μL, 15-50 μL or the 10-50 μL range. Elution volumes may be added in one aliquot. The elution volume (EV) in μL to bed mass (BM) in mg ratio (the EV:BM ratio) may be less than 25, 20, 15, 10, 5, 4, 3, or 2 for column bed mass of 20, 15, 10, 5, 4, 3, 2, 1 and 0.5 mg. Surprisingly smaller mass beds in the plate and column of the invention can accommodate smaller EV:BM ratios as the bed mass is decreased. This is the opposite of would be expected by someone skilled in the art.
In some embodiments, the column beds are expressed in volume rather than mass. In this case, the elution volume (EV) in μL to bed volume (BV) in μL ratio (the EV:BV ratio) may be less than 10, 5, 4, 3, or 2 for column bed volumes of 50, 40, 30, 20, 15, 10, and 5 μL. Similarly, small volume beds in the plate and column of the invention can accommodate smaller EV:BV ratios as the bed volume is decreased.
The columns are removable from the plate and may be used in a back and forth flow tip column format.
The columns are designed to be able to add elution volumes of less than 50, 40, 30, 25, 20, 15, 10 and 5 μL to the top frit of the column without introducing an air gap to the top of the column.
The plate is configured into an 8×12 format but is not limited to this configuration. It can have any number of rows and columns. The plate can be processed in a 96 well plate type format or tip columns from the plate can be process in 1-2, 1-4, 1-8, 1-12 or 1-96 pipette pump format. Tips removed from the plate may be process with multichannel pipette heads in the 2, 4, 8 and 12 channel pipette format.
The placement of the end of the column (or bottom frit) relative to the bottom of the collection well is within about 5 mm of the bottom of a 350 μL collection plate thus avoiding splashing, aerosol formation due to high flow rates.
The diameter of top frit and elution frits for 96 column plate is in the range of 0.1 to 4 mm and in the range of 1 to 2 mm.
The columns can be sealed into plate format with an annular ridge while individual tip columns are also removable from the plate.
Plate solid phase extraction with a 5 mg or less bed mass where the sample addition is performed using a filtration aid.
The optional modular dual column format used tip columns that are compatible with 96 at a time plate format and a 1-96 pipette tip column format having:
A sample prepared by a method according to the invention may be further analysed in a subsequent step e.g. by mass spectrometry, such as by LC-MS or LC-MS/MS.
Experimental
The present examples are provided for illustrative purposes only, and are not to be construed as limiting the invention as defined by the appended claims. All references provided below and elsewhere in the present application are hereby included herein via reference.
Columns:
The low volume format (LVF) columns according to the invention used in the examples below were prepared from high purity polypropylene in a shape corresponding to
The frits (denoted screens below) arranged in the columns used herein were all made from nylon in accordance with standard methods, and presented the following properties:
Bottom and Top Fits:
25:19 (given as pore diameter (um): % open)
Filter frit:
105:52 (given as pore diameter (um): % open)
The adsorbents (denoted resins below) used in the examples were commercially available from Biotage (https://biotage.com/), unless otherwise indicated. Adsorbent was loaded in the columns between the bottom frit and the top frit until substantially no space was left between the adsorbent and the top frit.
Low Volume Format (LVF) columns as described in
A variety of top and bottom screens were investigated based on the particle size of the EVOLUTE ABN 20 μm and 30 μm material.
The shortest processing times and lowest applied pressures were observed using ABN 30 μm resin. For both resins the shortest processing times and lowest pressures were observed using single top ‘105:52’ screens (though the differences were often minimal) and processing times were faster than when performed manually on the pressure+.
Materials
EVOLUTE ABN 20 μm and 30 μm, 5 μL was provided in PhyNexus PhyTips (2 mg) (https://phynexus.com/) wherein a bottom frit, a top frit and a filter frit above the top frit had been arranged as described in the present specification.
Below, the term “LVF” which is an abbreviation for Low Volume Format will be used interchangeably with the term “microelution columns of the invention”. When a microelution column of the invention has been arranged as fixed (non-removable) in a base plate for parallel processing, it may also be denoted an “LVF well”.
The diameter of the top screen frit was 0.120 inches and the diameter of the bottom screen frit was 0.086 inches. The diameters are the outside diameter and include the column wall thickness of approximately 0.020 inches. To calculate the diameter of the effective frit diameter, 0.040 inches is subtracted from each diameter.
Methods
Triplicate LVF wells for each particle diameter and screen configuration were populated in row A of a Biotage LVF base plate (
Samples
Urine samples obtained from human healthy volunteers were treated in accordance with standard procedures for plasma samples.
LVF wells were processed using the Biotage EVOLUTE ABN on an Extrahera in manual mode. A positive pressure setting of 2.0 bar was used for all steps as this was judged to initiate flows when run on a used set of 20 μm tips. The pressure was increased to 5.0 bar for 30 seconds prior to the final elution step though this did not result in any additional drops coming off of the tips.
Flows were judged by measuring the time from when the pressure head comes down to when the last full drip comes off of each tip measuring the range from the earliest of the three tips to pass the solvent to the last of the three. These times were determined accurately by videoing each step and monitoring each tip individually by reviewing the film. Close-up images from a selection of tips were also taken at various time points. Some solvents were slightly dyed in colour to try and make them more visible though this did result in the colour concentrating on the tip media on occasions.
Observations
a) ABN 30 μm, 5 μL PhyTip LVF Extrahera Processing
All of the tips were comfortably processed using a positive pressure of 2 bar. When viewing all varieties at the same time there was generally little difference of flow from one variety of tip to another however the 30 μm were faster than the corresponding 20 μvariant. When studying individual batches the single screen tips are very slightly faster eluting than the double screen and 105:52 tips slightly faster eluting than the 25:19 equivalents. Even later in the extraction procedure where the differences are maximised the effect it has on flow speeds is unlikely to be significant.
b) ABN 20 μm, 5 μL PhyTip LVF Extrahera Processing
All of the tips were comfortably processed using a positive pressure of 2 bar. When viewing all varieties at the same time there was generally little difference of flow from one variety of tip to another however the 20 μm tips were slower. When studying individual batches the single screen tips are very slightly faster eluting than the double screen and 105:52 tips slightly faster eluting than the 25:19 equivalents. Even later in the extraction procedure where the differences are maximised the effect it has on flow speeds is unlikely to be significant.
Low Volume Format (LVF) tips and OASIS μElution wells were processed to determine flow characteristics using two types of pre-treated plasma.
Typical flow characteristics were observed using fresh plasma with/without centrifugation and aged plasma with centrifugation.
Materials
EVOLUTE ABN 30 μm, 5 μL, 105 μm+25 μm top screens (PTE 93-05-XX)
OASIS HLB μElution 30 μm
WBS plasma #5260 (aged, high precipitation)
WBS plasma #413 (fresh, low precipitation)
(WBS=Welsh Blood Service)
Methods
An aliquot of each batch of plasma was centrifuged at 6500×g for 10 minutes. The supernatant was transferred to a new container and any pellet discarded.
An aliquot of each batch of plasma without centrifugation (−C) and with centrifugation (+C) was diluted 1:1 with 1% formic acid.
LVF columns were populated in a Biotage LVF base plate. 200 μL sub-aliquots of each batch of pre-treated plasma (−C/+C) were transferred to duplicate LVF tips (due to numbers available) and triplicate μElution wells.
LVF columns were processed with a Pressure+96 positive pressure manifold using the maximum flow (coarse) setting; the μElution plate was processed using the variable flow (fine) setting. Processing pressures and times were recorded.
Processing of μElution wells was more straightforward, loading completed and flow ceased as expected using the fine setting. Processing LFV tips using the coarse setting resulted in completed tips exceeding the ‘bubble point’ of the components.
The present example describes Solid Phase Extraction (SPE) recoveries of a range of analytes obtained in LC-MS performed on samples prepared by SPE using either prior art columns (30 and 10 mg, respectively) or columns according to the present invention (2 mg LVF)
This example was set up to show the high recoveries obtained with the microelution columns according to the invention using low elution volumes.
The LVF columns described in the Materials and Methods were used.
The sample was discard human plasma from the Welsh Blood Service, UK.
In this example, Mix 9 is an internal test mix for acids, basic and neutral drugs:
Acetaminophen (neutral drug) Naltrexone Metoprolol Mianserin (basic drugs) Prednisolone (netural steroid) Ketoprofen Warfarin Sulindac Indomethacin (acidic drugs) for recovery determination of low elution volume SPE plate.
Solid phase resin: EVOLUTE ABN
Method
1. Condition: MeOH
2. Equilibrate: 0.1% formic acid aq
3. Load: 5 ng in 200 μL (1:1, plasma: 1% formic acid)
4. Wash: 95/5 H2O/MeOH
5. Elute: 50 μl MeOH
6. Dry: stream of air
7. Reconstitute: 1 mL of mobile phase (80/20 H2O/MeOH)
8. Analyze Waters Acquity UPLC interfaced to a Premier XE triple quadrupole Mass spectrometer, 10 μL injections
9. Data analysis using internal and external standards
The same example 3a with 2 mg LVF except a single aliquot of less than 50 μL is used to elute the analytes. The aliquot is successful in elution of the analyte with a single aliquot of 20, 30, 40 or 45 μl of methanol.
The same as example 1 with 2 mg LVF except a single aliquot of 25 μL buffer is applied to the top of the plate column with hydrophobic wall and hydrophilic frit. With an hydrophilic wall, the sample, washing solution and eluent are applied to the column with the liquid traveling down the wall of the column and reducing the air gap. Less air is introduced to the column bed as the column is processed.
The same as example 1 with 2 mg LVF except a single aliquot of 25 μL buffer is applied to top of the plate column with hydrophobic wall and hydrophilic frit where the diameter of the droplet is less than the diameter of the column above the frit. The process prevents the introduction of the air gap into the column as the liquid is introduced into the column.
The same as example 1 with 2 mg LVF except a single aliquot of 25 μL buffer is applied to the top of the plate column with hydrophobic wall and hydrophilic frit where the droplet touches the frit. The aliquot is applied in 1, 2 or more droplets and flow to cover the top of the column bed frit. The process prevents the introduction of the air gap into the column as the liquid is introduced into the column.
The low volume format (LVF) columns having a bottom frit and a top frit (but no filter frit) according to the invention used in the examples below were prepared from high purity polypropylene in a shape corresponding to
The column dimensions were as follows: 2 mg.
The frits (denoted screens below) arranged in the columns used herein were all made accordance with standard methods, and presented the following properties:
Frits:
Bottom: 15:10 Nylon (given as pore diameter (μm): % open)
Top: 33: 21 Polyester (given as pore diameter (μm): % open)
The adsorbents (denoted resins below) used in the examples were commercially available from Biotage (https://biotage.com/), unless otherwise indicated. Adsorbent was loaded as a packed bed in the columns between the bottom frit and the top frit allowing slight space between the adsorbent and the top frit according to diameter of top frit.
The present example describes Solid Phase Extraction (SPE) recoveries of a range of analytes obtained in LC-MS/MS performed on samples prepared by SPE using either prior art columns (10 mg) or columns according to the present invention (2 mg LVF).
This example was set up to show the high recoveries obtained with the microelution columns according to the invention using low elution volumes. The LVF columns described in the Materials and Methods were used.
The sample was stripped human serum from Golden West Biologicals, USA. Stripped serum was used in this example due to the endogenous nature of the target panel. Analysis compared blank serum (n=1) then serum spiked pre (n=7) and post extraction (n=4) for repeatability.
In this example, a panel of endogenous steroid hormones: 18-hydroxycorticosterone, cortisone, cortisol, 11-deoxycortisol, corticosterone, 21-deoxycortisol, estradiol, DHEA, estrone, androstenedione, 11-deoxycorticosterone, 17-hydroxyprogesterone, progesterone, 17-hydroxypregnenolone, pregnenolone, testosterone, DHT, for recovery determination of low elution volume SPE plate.
Solid phase resin: EVOLUTE ABN
Method
1. Condition: MeOH
2. Equilibrate: 0.1% formic acid aq
3. Load: 1 ng in 200 μL (1:1, plasma: 1% formic acid); equivalent to 10 ng/mL
4. Wash 1: H2O
5. Wash 2: 60/40 (v/v) H2O/MeOH
5. Elute: 20-50 μl MeOH
6. Dry: stream of air
7. Reconstitute: 200 μL of 50/50 H2O/MeOH
8. Analyze Shimadzu Nexera UHPLC interfaced to an 8060 triple quadrupole Mass spectrometer, 5 μL injections
9. Data analysis using internal and external standards
Recovery data and RSDs are presented in
The same example 4b with 2 mg LVF except a single aliquot of less than 50 μL is used to elute the analytes. Elution of the analyte is successful with a single aliquot of solvent with 20, 30, 40 or 50 μl of methanol.
The results of using the very small elution volumes enabled by the present invention are presented as steroid panels in
The same example 4b with 2 mg LVF using a single aliquot of 30 μL to elute the analytes compared with 150 μL for the 10 mg FWP. In
| Number | Date | Country | Kind |
|---|---|---|---|
| 19167592.5 | Apr 2019 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2020/059549 | 4/3/2020 | WO | 00 |
