Reducing Dilution and Analysis Time in Online Comprehensive Two

Dec 28, 2015 - Online comprehensive two-dimensional liquid chromatography (LC × LC) offers ways to achieve high-performance separations in terms of p...
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Reducing Dilution and Analysis Time in On-line Comprehensive Two-Dimensional Liquid Chromatography by Active Modulation Andrea F. G. Gargano, Mike Duffin, Pablo Navarro, and Peter J Schoenmakers Anal. Chem., Just Accepted Manuscript • DOI: 10.1021/acs.analchem.5b04051 • Publication Date (Web): 28 Dec 2015 Downloaded from http://pubs.acs.org on January 4, 2016

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Analytical Chemistry

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Reducing Dilution and Analysis

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Time in On-line Comprehensive

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Two-Dimensional Liquid

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Chromatography by Active

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Modulation

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Andrea F.G. Gargano1,2 Mike Duffin3, Pablo Navarro3, Peter J. Schoenmakers2

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Van 't Hoff Institute for Molecular Sciences, Science Park 904 1098 XH Amsterdam, Netherlands

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Syngenta, Jealott's Hill International Research Centre, Bracknell, Berkshire RG42 6EY, UK

TI-COAST, Van 't Hoff Institute for Molecular Sciences, Science Park 904, 1098 XH Amsterdam, Netherlands

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*[email protected]

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Tel: +31-20-525 7040 Science Park 904 |1098 XH Amsterdam Building C2, room 248A

Dr. Andrea Gargano Analytical Chemistry Van 't Hoff Institute for Molecular Sciences Universiteit van Amsterdam

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Keywords

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On-line comprehensive two-dimensional liquid chromatography, LC×LC, Active Modulation,

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UHPLC, Surfactant Analysis, Tristyrylphenol ethoxylate

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 Abstract

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On-line comprehensive two-dimensional liquid chromatography (LC×LC) offers ways to

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achieve high-performance separations in terms of peak capacity (exceeding 1000) and

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additional selectivity to realize applications that cannot be addressed with one-dimensional

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chromatography (1D-LC). However, the greater resolving power of LC×LC comes at the

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price of higher dilutions (thus reduced sensitivity) and, often, long analysis times (>100 min).

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The need to preserve the separation attained in the first dimension (1D) causes greater

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dilution for LC×LC, in comparison with 1D-LC, and long analysis times to sample the 1D with

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an adequate number of second dimension separations. A way to significantly reduce these

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downsides is to introduce a concentration step between the two chromatographic

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dimensions. In this work we present a possible active-modulation approach to concentrate

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the fractions of 1D effluent. A typical LC×LC system is used with the addition of a dilution

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flow to decrease the strength of the 1D effluent and a modulation unit that uses trap columns.

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The potential of this approach is demonstrated for the separation of tristyrylphenol ethoxylate

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phosphate surfactants, using a combination of hydrophilic-interaction and reversed-phase

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liquid chromatography. The modified LC×LC system enabled us to halve the analysis time

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necessary to obtain a similar degree of separation efficiency with respect to UHPLC based

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LC×LC and of 5 times with respect to HPLC instrumentation (40 compared with 80 and 200

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min, respectively), while at the same time reducing dilution (DF of 142, 299 and 1529,

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respectively) and solvent consumption per analysis (78, 120 and 800 mL, respectively).

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Analytical Chemistry

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 Introduction

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Two dimensional liquid chromatography is a technique that allows the characterization of

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samples that, due to their complexity, cannot be resolved using one-dimensional

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chromatography. The higher resolving power is a direct consequence of the consecutive

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separation of the sample components using two distinct chromatographic processes that

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exploit different selectivity principles. In comprehensive two-dimensional LC (LC×LC) the

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entire sample is subjected to the two different separations. In off-line LC×LC there are no

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restrictions on the speed of analysis in the second dimension, making this the best way to

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exploit the full resolving power of both the separation dimensions1,2. However, the resulting

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long overall analysis times make this technique impractical for routine analysis of large

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numbers of samples.

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Online LC×LC has the advantage of significantly decreasing the analysis time necessary to

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obtain a high peak capacity. However, the tight constraints imposed by the coupling of the

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two chromatographic processes seriously limit the separation efficiency. The second

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dimension separations (2D) must be fast to allow frequent sampling of the first separation

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(1D), while providing sufficient resolving power. Studies have demonstrated that the optimal

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number of fractions per 1D peak is somewhere between 2 and 43–6.Moreover, to reduce the

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volumes collected for injection onto the 2D column, the 1D separation has to be run at low,

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often suboptimal7, linear flow velocities and thus long run times are required to deliver

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efficient gradients (spanning at least five column volumes). Other restrictions are related to

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the compatibility of the mobile phases used in the two dimensions8 and to the volume of

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sample that can be injected on the 2D column9,10.

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If online LC×LC is to become more frequently adopted for routine analysis, robust high-

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throughput analysis exploiting orthogonal selectivities will need to be developed. In this

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context it is important to develop strategies that enable fast and efficient separations.

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Significant shortening of the analysis time can be achieved by reducing the 2D cycle time

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using ultra-high-pressure LC (UHPLC)11–13, increased temperatures14 or parallel 2D15,16

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technologies that are now available in commercialized LC×LC systems. However, to reduce

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the injection band broadening in the second dimension, these systems use combinations of

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long and narrow 1D columns (e.g. 1 or 2.1 mm I.D.) and short and wide 2D columns (e.g. 4.6

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mm I.D). Using such configurations it is possible to minimize the ratio between the volume of

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the fractions collected from the first dimension and the 2D column volume5, typically injecting

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less than 10% of the 2D column volume. As a consequence, high peak capacities are

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obtained at the price of high dilutions and thus loss in sensitivity.

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Alternative column couplings have been suggested to limit the injection band broadening

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without increasing the dilution and allow combinations of chromatographic modes that make 3 ACS Paragon Plus Environment

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use of incompatible solvents. Examples include interfaces with trap columns instead of

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loops17–23, vacuum evaporation24 and thermally-assisted modulation21,25. These technologies

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have proven, with different degrees of success, their effectiveness at reducing problems

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connected with the injection of strong or incompatible solvents in the 2D system, but they

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have not yet reached a level of maturity that would allow their use in routine LC×LC

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applications.

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In this work we present an active-modulation approach (LC/a×m/LC), in which the fractions

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collected from the 1D are concentrated prior to injection in the 2D. This is achieved using a

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HPLC×UHPLC system that was modified to include a dilution flow to decrease the mobile

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phase strength of the 1D effluent and a modulation unit that uses trap columns. This

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configuration allows, in comparison with the conventional loop interface (“passive-

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modulation”), linear velocities closer to the optimum in the 1D without using flow splitters7,26.

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The LC/a×m/LC system also reduces the effects of the 1D dead times (consequences of low

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flow rates in the first dimension), dwell volumes and 2D injection band broadening (thanks to

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the reduction of the volumes collected from the 1D). Together these result in a considerably

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shorter time necessary to obtain a specified separation efficiency.

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The feasibility of LC/a×m/LC is demonstrated for the separation of tristyrylphenol ethoxylate-

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phosphate (TSP) surfactants (polymeric compounds), using a combination of hydrophylic

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interaction LC and reversed-phase LC (HILIC×RPLC). Thanks to the independent

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selectivities offered by this method the sample can be separated according to its ethoxyate

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chain length (HILIC) and the degree of styrene and phosphate substitution (RP).

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 Experimental Section Chemicals

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The samples used for this study are: tristyrylphenol ethoxylate (TSP; CAS 99734-09-05)

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commercially available under the names Agent 3152-90 and Termul 3150; tristyrylphenol

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ethoxylate phosphate (TSP phosphate CAS 90093-37-1) as Agnique PE TSP 16A, Agent

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3152-92 and Soprophor 3D33. The chemical structure of the compounds is reported in

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Figure 1. The solvents used were Milli-Q grade water (18.2 mΩ) and liquid-chromatography-

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grade acetonitrile (ACN), methanol (MeOH), tetrahydrofuran (THF) and 1-butanol, obtained

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from Avantor Performance Materials B.V. (Deventer, NL). Ammonium acetate (Bioxtra

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grade, 99% purity) was purchased from Sigma-Aldrich (Zwijndrecht, NL). All materials were

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used as received and the mobile phases were not filtered prior to use.

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Samples were prepared by dissolving the surfactant in a mixture of 94% ACN 5% THF and

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1% 12.5-mM ammonium acetate at the concentrations reported in Table 1 for the HILIC×RP 4 ACS Paragon Plus Environment

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Analytical Chemistry

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separations or at 1 mg/ mL for the HILIC study reported in Figure 2, 3. The performance of

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the different RP materials (Figure 4) was studied with a 1 mg/mL solution of surfactants in

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H20/ACN 1/1 v/v.

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Instrumentation & Data Analysis

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HPLC×HPLC Instrumentation and data analysis.

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An LC×LC instrument composed of an Agilent (Waldbronn, Germany) 1100 quaternary (1D)

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pump (Model G1311A) and a 1260 quaternary (2D) pump (Model G1311B), two degassers

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(Model G1322), thermostats (Model G1316A), detectors (Model G4212B with 13 µL flow

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cell), one autosampler (Model G1329B) and a 10-port two-position switching valve (Agilent

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G4232A and G1170A support unit) with 60-µL loops was used for our experiments. The

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valve was configured for back-flush injection27 and all Agilent modules were controlled using

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Agilent Chemstation B.04.03 software on two different computers, the first was used to

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control the autosampler, 1D pump and thermostat, and detector while the second controlled

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the switching valve, 2D pump and detector. The data were exported as comma-separated

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files and processed using a recently published Matlab-2014b (The Mathworks, Inc., Natick,

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MA, USA) script28,29.

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A Kromasil 60 Si-OH 1D column (250 × 3 mm i.d.; 5-µm particles; 60-Å pore size; Hichrom

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Ltd, Reading, United Kingdom) was used, followed by a stainless-steel tee (Model U-428,

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IDEX Corp; DaVinci, Rotterdam NL) to split the flow before the switching valve. Stainless-

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steel tubing of the same I.D. and length (75 µm I.D. x 200 mm) were used on the two sides

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of the tee, to approach a split ratio of 1:1. As 2D column we used a Phenomenex Kinetex

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C18 (50 x 4.6 mm; 2.6-µm; 100-Å, Phenomenex, Macclesfield, United Kingdom). Operation

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conditions and further details are reported in Table 1.

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HPLC×UHPLC and HPLC/a×m/UHPLC

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An Agilent 1200 degasser (G1379), a 1200 SL binary pump (Model G1312, with the original

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mixer replaced by a 50-µL mixer from Waters) an autosampler (Model G4226A) and column

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thermostat compartment (Model G1316C) were used for the 1D. The 2D was composed of

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UHPLC binary pumps (Model G4220A configured with a JetWeaver V35 mixer) a

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thermostatted column compartment (Model G1316C) and a diode-array UV detector (DAD,

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Model G4212A) with a standard flow cell (13 µL volume). The valve schematically shown in

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Figure 5 is a 4-port duo 2-position valve (Model 5067-4214) installed in the 2D thermostat.

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Loops of 40 µL were used with valve configuration for back-flush injections.

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We used an Acquity UPLC BEH HILIC (150 x 2.1 mm; 1.7-µm; 130-Å; Waters, Elstree, UK)

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1

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Additionally, we tested a Hypersil GOLD C-18 (50 x 1 mm; 1.9-µm; ThermoFisher Scientific,

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Breda, NL) column. The comparison between the different columns is reported in Figure 4.

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The HPLC/a×m/UHPLC set-up used the same hardware described above and, in addition, a

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stainless-steel tee connection (Model U-428, IDEX Corp) to add a dilution flow after the first-

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separation dimension using an isocratic pump (Model G1310B). The modulation interface

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was configured for forward-flush operation and the loops where substituted by two C-18 pre-

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column cartridges (2.1 x 2 mm with sub-2 µm particles, SecurityGuard Ultra AJ0-8782,

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Phenomenex, Utrecht, NL) directly installed in the switching valve and connected to the port

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receiving effluent from the 1D by a 50 mm x 50 µm I.D. connection. A schematic

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representation of the setup is shown in Figure 5.

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All Agilent modules of this configuration were controlled and programmed using Agilent

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Chemstation C.01.04. Data analysis was performed using GC image R 2.5 software

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(GCimage, Lincoln, USA). Operation conditions are reported in the Chromatographic

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Conditions section and Table 1.

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D column and an Acquity UPLC HSS C18 2D column (50 x 2.1 mm; 1.8-µm; 100-Å).

Chromatographic Conditions

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The 1D separations were performed using a mobile phase A: 94% ACN, 5% THF, 1% 12.5

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mM ammonium formate, to mobile phase B: 12.5 mM ammonium acetate. In the 2D the

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mobile phase used was A: 99% 12.5 mM ammonium formate, 1% 1-butanol and B: 99%

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MeOH, 1% 1-butanol30. Butanol was used to reduce the equilibration time. The separation

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performed using the LC/a×m/LC set-up used a dilution flow composed of 12.5-mM

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ammonium acetate.

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The conditions used for the HPLC×HPLC (graphical abstract and Table 1) were: 1D flow rate

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of 0.1 mL/min at T=10˚C and gradient elution from 0% B to 60% B in 140 min, 20 min at 60%

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B. At 180 min the flow rate was set to 1 mL/min and run at 0% B till 200 min. For the 2D

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separation we used a flow rate of 4 mL/min, T=40˚C using, gradient elution from 40% B to

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80% in 0.01 min, from 80% to 100% at 0.76 min, kept at 100% B till 0.86 min and

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equilibrated at 40% B for 0.14 min. Modulation volume= 50 µL. The HPLC×UHPLC

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separation described in Table 1 was performed using a 1D flow rate of 0.04 mL/min, T= 5˚C,

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gradient elution from 2% B to 20% B in 20 min, then to 50% B at 50 min, 55% B at 60 min,

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2% B at 70 min. Flow rate increased to 0.2 mL/min at 78 min. The 2D was run at 50˚C at a

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flow rate of 1.5 mL/min, gradient elution from 35% B to 80% in 0.01 min, 85% to 100% at

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0.35 min, 0.03 min 100% B and at 0.4 min re-equilibration at 40% B. Modulation volume= 20

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µL. The HPLC×UHPLC and HPLC/a×m/UHPLC reported in Figure 6, 7 runs were performed

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Analytical Chemistry

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using a 1D flow rate of 0.08 mL/min, T= 5˚C, gradient elution from 2% B to 20% B in 10 min,

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then to 50% B at 25 min, 55% B at 30 min, 2% B at 39.99 min. Flow rate increased to 0.2

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mL/min at 40 min. In the 2D T=50˚C, gradient elution from 35% B to 80% in 0.01 min, then to

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100% at 0.29 min, 100% B at 0.30 min, followed by 0.06 min re-equilibration at 35% B (0.35

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min modulation time). The 2D flow rate was of 1.5 mL/min in the HPLC×UHPLC setup and

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1.35 mL/min in the HPLC/a×m/UHPLC. The dilution flow in used in the /a×m/ setup was 0.6

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mL/min and this incremented the 1D back pressure off approximately 100 bar. All the LC×LC

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separation where monitored at 220 nm using 80 Hz scan rate.

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Calculations

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The following paragraph describes the equations adopted to obtain the results reported in

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Table 1.

Peak Capacity

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The peak capacity (nc) was determined from the average width at half height (    ) applying  Eq. (1).

 =

+    ) . ∙( 

1

(1)

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For the calculation of the 1D peak capacity the average width was obtained from the

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integration of five peaks at the beginning of the chromatogram (indicated in red in Figure 2b)

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and five peaks in the area of elution of the phosphate species (green in Figure 2b). The 2D

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peak capacity was obtained as average of all the (5 to 15, depending on tG) peaks present in

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the chromatograms.

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The predicted peak capacity for each LC×LC system was calculated as:

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, =  ∙ 

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(2)

Using  values obtained from one dimensional runs under the same conditions as the

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LC×LC runs (see Table 1 for the respective parameters) and  .calculated from the

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Equation (2) is not taking into account 1D undersampling and band broadening associated

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average  of multiple 2D run (2D nc parameter of Table 1)

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with the modulation process3,4,6.

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Two different approaches were used to correct for these effects, using the equation

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proposed by Davis-Li et al.6,31,32

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,

!

=



"# ∙ "# $

=



"# ∙ "#

%&'.'(∙)

* +  # # , *

(3)

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220 221 222

223 224

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where - is the undersampling correction factor . is the modulation cycle and ./ the

dimension gradient time; and that proposed by Vivó et al. for loop-based LC×LC5 ,

!

=



123 45

0



 5 *# ; 6789: ; &