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HPLC 2006 Presentation K. Flook, S. Rao, J. Thayer, S. Xie, and C. A. Pohl, Dionex Corporation, Sunnyvale, CA, USA High Throughput Liquid Chromatography Using Polymeric ProSwift Monolithic Bioseparation Columns High Throughput Liquid Chromatography Using Polymeric ProSwift Monolithic Bioseparation Columns K. Flook, S. Rao, J. Thayer, S. Xie, and C. A. Pohl, Dionex Corporation, Sunnyvale, CA, USA INTRODUCTION Speed and resolution are two competing performance factors in chro- matography using conventional porous separation media. One feature is often achieved while the other is sacrificed. This is often the case during separation of proteins and peptides, since these large molecules exhibit low diffusivity which translates into higher mass transfer resistance. The net result is significant peak broadening especially at higher flow rates. A new generation of styrene-based reversed-phase separation media from Dionex, ProSwift polymer monoliths, is designed to address the above problem. They contain a network of large pores in which separation is achieved primarily by convective flow rather than diffusive flow. Highly improved mass transfer rates allow high speed analysis without band broadening or significantly sacrificing resolution thereby improving throughput and productivity. The new ProSwift phases use a patented process to produce a well defined polymer monolith. An in-situ polym- erization process allows excellent batch-to-batch reproducibility and column stability. Separations can be achieved at high flow rates without loss of resolu- tion. These columns have an excellent longevity and are stable over a wide pH range. We discuss the performance of three columns; two recently introduced phases, RP-2H and RP-3U, as well as our newest introduction, RP-1S. Ex- cellent separation of a wide variety of proteins and peptides is shown here. OBJECTIVES • Characterize the morphology and pore structure of the ProSwift monoliths. • Investigate the chromatographic properties of the ProSwift monoliths. • Develop applications for proteomic research. Eluents: (A) DI H 2 O / CH 3 CN (95:5 v/v) + 0.1% TFA (B) DI H 2 O / CH 3 CN (5:95 v/v) + 0.1% TFA Injection: 10 µL (unless otherwise stated) Figure 1. Manufacturing Process Column efficiency of the monolith base support is controlled by a one-step polymerization process. The simplicity of a one-step process results in highly reproducible products. Monomers Porogen Initiator Polymerization Wash 23133 Surface Modification Reversed-Phase Column Ion-Exchange Column Figure 2. SEM Images of ProSwift Monoliths Through Pores ProSwift RP-1S 23138 ProSwift RP-2H ProSwift RP-3U High permeability Low backpressure High flow rate Flow through pores Fast mass transfer High resolution Figure 3. Peptide Separation on ProSwift RP-1S 0 1 2 3 4 5 6 7 8 9 10 11 12 –10 600 mAU Minutes • ProSwift RP-1S allows separation of a wide range of molecular weights. 23217 4 mL/min 1 mL/min Sample: Standard Peptide Mix (Sigma # H2016) 1. Gly-Tyr (MW 238.2) 2. Val-Tyr-Val (MW 379.5) 3. Methionine Enkephalin Acetate (Tyr-Gly-Gly-Phe-Met) (MW 573.7) 4. Leucine Enkephalin (Tyr-Gly-Gly-Phe-Leu) (MW 555.6) 5. Angiotensin II acetate (Asp-Arg-Val-Tyr-Ile-His-Pro-Phe) (MW 1046.2) Injection: 5 µL Gradient: 1 - 25% B in 6 min at 1 mL/min, 1 - 25% B in 1.5 min at 4 mL/min
Transcript
  • HPLC2006Presentation �HPLC2006Presentation

    K. Flook, S. Rao, J. Thayer, S. Xie, and C. A. Pohl, Dionex Corporation, Sunnyvale, CA, USA

    High Throughput Liquid Chromatography UsingPolymeric ProSwift Monolithic Bioseparation ColumnsHigh Throughput Liquid Chromatography UsingPolymeric ProSwift Monolithic Bioseparation ColumnsK. Flook, S. Rao, J. Thayer, S. Xie, and C. A. Pohl, Dionex Corporation, Sunnyvale, CA, USA

    INTRODUCTIONSpeed and resolution are two competing performance factors in chro-matography using conventional porous separation media. One feature is often achieved while the other is sacrificed. This is often the case during separation of proteins and peptides, since these large molecules exhibit low diffusivity which translates into higher mass transfer resistance. The net result is significant peak broadening especially at higher flow rates.

    A new generation of styrene-based reversed-phase separation media from Dionex, ProSwift™ polymer monoliths, is designed to address the above problem. They contain a network of large pores in which separation is achieved primarily by convective flow rather than diffusive flow. Highly improved mass transfer rates allow high speed analysis without band broadening or significantly sacrificing resolution thereby improving throughput and productivity. The new ProSwift phases use a patented process to produce a well defined polymer monolith. An in-situ polym-erization process allows excellent batch-to-batch reproducibility and column stability.

    Separations can be achieved at high flow rates without loss of resolu-tion. These columns have an excellent longevity and are stable over a wide pH range.

    We discuss the performance of three columns; two recently introduced phases, RP-2H and RP-3U, as well as our newest introduction, RP-1S. Ex-cellent separation of a wide variety of proteins and peptides is shown here.

    OBJECTIVES• Characterize the morphology and pore structure of the ProSwift

    monoliths.• Investigate the chromatographic properties of the ProSwift monoliths.• Develop applications for proteomic research.

    Eluents: (A) DI H2O / CH3CN (95:5 v/v) + 0.1% TFA (B) DI H2O / CH3CN (5:95 v/v) + 0.1% TFAInjection: 10 µL (unless otherwise stated)

    Figure 1. Manufacturing Process

    • Column efficiency of the monolith base support is controlled by a one-step polymerization process.• The simplicity of a one-step process results in highly reproducible products.

    Monomers

    Porogen

    InitiatorPolymerization Wash

    23133

    Surface Modification

    Reversed-PhaseColumn

    Ion-Exchange Column

    Figure 2. SEM Images of ProSwift Monoliths

    Through Pores

    ProSwift RP-1S

    23138

    ProSwift RP-2H

    ProSwift RP-3U

    High permeability Low backpressure High flow rate

    Flow through pores Fast mass transfer High resolution

    Figure 3. Peptide Separation on ProSwift RP-1S

    0 1 2 3 4 5 6 7 8 9 10 11 12–10

    600

    mAU

    Minutes

    • ProSwift RP-1S allows separation of a wide range of molecular weights.

    23217

    4 mL/min

    1 mL/min

    Sample: Standard Peptide Mix (Sigma # H2016) 1. Gly-Tyr (MW 238.2) 2. Val-Tyr-Val (MW 379.5) 3. Methionine Enkephalin Acetate (Tyr-Gly-Gly-Phe-Met) (MW 573.7) 4. Leucine Enkephalin (Tyr-Gly-Gly-Phe-Leu) (MW 555.6) 5. Angiotensin II acetate (Asp-Arg-Val-Tyr-Ile-His-Pro-Phe) (MW 1046.2)Injection: 5 µL

    Gradient: 1 - 25% B in 6 min at 1 mL/min, 1 - 25% B in 1.5 min at 4 mL/min

    AnutaNew Stamp

  • 2 HighThroughputLiquidChromatographyUsingPolymericProSwiftMonolithicBioseparationColumns

    Figure 5. Protein Separation on ProSwift RP-2H

    0 1 2 3 4 5 6 7 8 9 10 11–300

    600

    mAU

    Minutes

    • ProSwift RP-2H column’s faster separation enables higher productivity.

    22903

    Protein standards

    8 mL/min4 mL/min

    2 mL/min1 mL/min

    Sample: 1. Ribonuclease A (1.5 mg/mL) 2. Cytochrome c (0.5 mg/mL) 3. BSA (1.5 mg/mL) 4. Carbonic Anhydrase (0.9 mg/mL) 5. Ovalbumin (1.5 mg/mL)Injection: 5 µL

    Gradient: 1% B for 2 min, 1 - 75% B in 6 min at 1 mL/min

    1% B for 1 min, 1 - 75% B in 3 min at 2 mL/min

    1% B for 0.5 min, 1 - 75% B in 1.5 min at 4 mL/min

    1% B for 0.25 min, 1 - 75% B in 0.75 min at 8 mL/min

    0 2 4 6 8 10 12 14–10

    500

    mAU

    Minutes23134

    1

    2

    34

    56

    7

    8

    9

    10

    11

    12

    13

    14

    Figure 6. Cytochrome c Tryptic Digest Separation on ProSwift RP-1S

    Flow: 1.0 mL/min

    Sample: Cytochrome c Tryptic Digest (2 mg Cytochrome c, 20 µg trypsin per mL) Injection: 20 µL

    Gradient: 1% B for 2 min, 1 - 50% B in 12 min

    • High resolution allows easy separation of digest peptides.

    Minutes0 2 4 6 8 10 12 14 16.1

    –100

    300

    mAU

    Flow = 1 mL/minFlow = 4 mL/min

    22909

    Figure 7. Separation of Snake Venom Proteins/Peptides• The ProSwift RP-2H column’s uniquely engineered pore size allows separation of samples with a wide molecular weight range.

    Gradient: 1 - 75% B in 12 min at 1 mL/min 1 - 75% B in 3 min at 4 mL/min

    Minutes0 2 4 6 8 10 12 14 16

    –200

    1,200

    mAU

    BSA

    IgG

    22908

    Figure 8. Separation of IgG and Albumin from Bovine Serum• The ProSwift RP-2H column has large flow through channels that result in high resolving power for large proteins.

    Flow = 1 mL/minFlow = 4 mL/min

    Sample: 1 part Bovine Serum, 4 parts Eluent A

    Gradient: 1 - 75% B in 12 min at 1 mL/min 1 - 75% B in 3 min at 4 mL/min

    Figure 9. Batch-To-Batch Reproducibility of ProSwift RP-2H

    0 1 2 3–10

    mAU

    Minutes23135

    5

    2

    1

    4

    ProSwift reversed-phase media are manufactured by a patented in situ manufacturing process which has the least number of variables affecting the reproducibility among all technologies. It does not require additional sieving, coating, multiple surface modification, and packing processes.

    Flow: 2.5 mL/min

    Sample: 1. Angiotensin II (30 µg/mL) 2. Substance P (30 µg/mL) 3. Ribonuclease A (30 µg/mL) 4. Cytochrome C (30 µg/mL) 5. BSA (30 µg/mL)

    Gradient: 1 - 60% B in 3 min

    100

    3

    Figure 4. Peptide and Protein Separation

    RP-3U

    RP-2H

    RP-1S

    0 2 4 6 8 10 12–5

    250

    mAU

    Minutes23132

    Flow: 1.5 mL/min

    Sample: 1. Methionine Enkephalin acetate (Tyr-Gly-Gly-Phe-Met) (MW 573.7) 2. Leucine Enkephalin (Tyr-Gly-Gly-Phe-Leu) (MW 555.6) 3. Angiotensin II acetate (Asp-Arg-Val-Tyr-Ile-His-Pro-Phe) (MW 1046.2) 4. Physalaemin (Glu-Ala-Asp-Pro-Asn-Lys- Phe-Tyr-Gly-Leu-Met) (MW 1265.4) 5. Substance P acetate (Arg-Pro-Lys-Pro- Gln-Gln-Phe-Phe-Gly-Leu-Met) (MW 1347.6) 6. Ribonuclease A 7. Cytochrome C 8. Carbonic Anhydrase 9. Bovine Serum Albumin 30 µg/mL each

    Gradient: 1 - 64% B in 17 min

  • HPLC2006Presentation �

    Figure 10. Robustness of the ProSwift RP-1S

    Injection 6

    Injection 506

    Injection 206

    Injection 106

    Injection 306

    Flow: 4 mL/min

    Sample*: 1. Ribonuclease A (1.5 mg/mL) 2. Cytochrome c (0.5 mg/mL) 3. BSA (1.5 mg/mL) 4. Carbonic Anhydrase (0.9 mg/mL) 5. Ovalbumin (1.5 mg/mL)Injection: 5 µL

    Gradient: 1% B for 1 min, 1 - 75% B in 2.5 min

    *Sample is injected every 50 gradient cycles

    2,000

    –20

    mAU

    3210 4Minutes

    23136

    • Durability and robustness are ProSwift characteristics. The ProSwift monoliths exhibit stability and reproducibility over many runs.

    Figure 11. pH Stability of the ProSwift RP-3U

    No treatment

    0.1M HCl48 hrs

    1M NaOH48 hrs

    The ProSwift RP monolith column is stable with treatment of 1 M NaOH and 0.1 M HCl in the regeneration process. It is shown to be stable at pH 2 to 12 at normal temperature and flow for long periods. This figure shows the resolution of four protein standards before and after base and acid regeneration treatments.

    Flow: 4 mL/min

    Sample: 1. Ribonuclease A (0.1 mg/mL) 2. Cytochrome c (0.05 mg/mL) 3. BSA (0.1 mg/mL) 4. Carbonic Anhydrase (0.1 mg/mL)

    Gradient: 15 - 80% B in 3 min

    325

    0.6 0.90.3 1.2Minutes

    23137

    0–5

    mAU

    1.5

    CONCLUSIONCharacteristics of Polymeric Monolithic Columns • High resolution • High flow velocity and low backpressure • High capacity • Highly reproducibility • Much more chemically stable than silica-based media

    Applications • High-throughput, high-resolution separation of proteins,

    peptides, and other biomolecules

    REFERENCEhttp://www1.dionex.com/en-us/columns_accessories/life_science_pharma/cons35517.html

    ProSwift is a trademark of Dionex Corporation.

    0

    500

    1000

    1500

    2000

    2500

    3000

    3500

    0 2 4 6 8 10

    Colu

    mn

    Back

    pres

    sure

    (psi)

    ProSwift RP-1S

    ProSwift RP-2H

    ProSwift RP-3U

    Polymer Beads, 8 µm

    Figure 12. Column Backpressures

    • The backpressures of ProSwift RP-2H and RP-3U columns are significantly lower than columns packed with beads. This allows the use of a higher flow rate for a much faster separation.

    • The ProSwift RP-1S column can be operated at higher flow rates than columns packed with polymer beds without compromising the column.

    Eluent: 30% B

    Flow Rate (mL/min)23131

    North America

    Sunnyvale, CA (408) 737-8522 Westmont, IL (630) 789-3660 Houston, TX (281) 847-5652 Atlanta, GA (770) 432-8100 Marlton, NJ (856) 596-0600 Canada (905) 844-9650

    Europe

    Austria (43) 1 616 51 25 Belgium (32) 3 353 4294 Denmark (45) 36 36 90 90 France (33) 1 39 30 01 10 Germany (49) 6126 991 210 Italy (39) 06 66 51 5052 The Netherlands (31) 161 43 43 03 Switzerland (41) 62 205 99 66 United Kingdom (44) 1276 691722

    Asia Pacific

    Australia (61) 2 9420 5233 China (852) 2428 3282 India (91) 22 28475235 Japan (81) 6 6885 1213 Korea (82) 2 2653 2580

    LPN 1862-01 06/06©2006 Dionex Corporation

    Dionex Corporation

    1228 Titan Way P.O. Box 3603 Sunnyvale, CA 94088-3603 (408) 737-0700

    Passion. Power. Productivity.

    www.dionex.com


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