Column Dimensions. GC Columns and Consumables. Mark Sinnott Application Engineer. March 12, 2010

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Secrets of GC Column Dimensions GC Columns and Consumables Mark Sinnott Application Engineer Folsom California March 12, 2010 Page 1

Secrets of GC Column Dimensions Do I have the right column phase? Resolution Equation Changes in Dimensions: Length Diameter Film Thickness Method Translation Software Carrier gas (if time) Page 2

Start with the Right Phase DB-1 15m x 0.32mm, 0.25µm Oven: 40 C for 2 min 40-120 C at 5 C/min 0 2 4 6 8 10 12 14 Time (min.) DB-Wax 15m, 0.32mm, 0.25µm Oven: 80-190 C at20 C/min 0 1 2 3 4 5 Time (min.) Page 3

Variables that affect chromatography Stationary Phase Temperature Programming Carrier Gas: type and linear velocity Column Length Film Thickness Internal Diameter There s no such thing as a free lunch Page 4

Resolution R N k α 1 k α = s 4 + 1 Efficiency ce cy Retention Selectivity N = ƒ (gas, L, r c ) k = ƒ (T, d f, r c ) α = ƒ (T, phase) L = Length r c = column radius d f = film thickness T = temperature Page 5

Column Dimensions Length Diameter Film Thickness Page 6

Resolution N k R = α 1 s 4 k + 1 α Efficiency Retention Selectivity N = ƒ (gas, L, r c ) k = ƒ (T, d f, r c ) α = ƒ (T, phase) L = Length r c = column radius d f = film thickness T = temperature Page 7

Column Length and Efficiency (Theoretical Plates) Length (m) N 15 69,450 30 138,900 60 277,800 0.25 mm ID n/m = 4630 (for k = 5) Page 8

Column Length and Resolution R α N α L Length X 4 = Resolution X 2 t α L Upside = Cut a bunch off during routine inlet maintenance and not lose a lot of Resolution Page 9

Column Length vs Resolution and Retention: Isothermal R=0.84 R=1.16 16 R=1.68 2.29 min 4.82 min 8.73 min 15 m 30 m 60 m Double the plates, double the time but not double the resolution Page 10

Column Length and Cost 15m 30m 60m $ $ $ $ $ $$ Page 11

Length Summary If you Increase Length: Efficiency Resolution Analysis Time Pressure Cost Increase Increase Increase Increase Increase Page 12

Resolution R N k α 1 k α = s 4 + 1 Efficiency ce cy Retention Selectivity N = ƒ (gas, L, r c ) k = ƒ (T, d f, r c ) α = ƒ (T, phase) L = Length r c = column radius d f = film thickness T = temperature Page 13

Column Diameter and Carrier Gas Flow Lower flow rates: Smaller diameter columns Higher flow rates: Larger diameter columns Low flow rates : GC/MS High flow rates: Headspace, purge & trap Page 14

Column Diameter Capillary Columns I.D. (mm) Common Name 053 0.53 Megabore 0.45 High speed Megabore 0.32 Widebore 0.20-0.25 Narrowbore 0.18 Minibore 0.10 Microbore 0.05 Nanobore Page 15

Column Diameter - Theoretical Efficiency Total Plates I.D. (mm) 5 m N ~ 112,000 0.05 n/m 23,160 10 m N ~ 112,000 20 m N ~ 112,000 30 m N ~ 112,000 0.10 0.18 0.20 0.25 0.32 0.45 11,580 6,660 5830 4630 3660 2840 Page 16 k = 5 053 0.53 2060

Different Column I. D. Equal Phase Ratios Column: DB-624 30 m, 0.53 mm, 3 m Carrier: Oven: Helium, 40(cm/sec) 65 C Injection: Split Detector: FID Column: DB-624 30 m, 032mm 0.32 mm, 18 1.8 m 0 5 10 15 20 Time (min) Page 17

PHASE RATIO (β) Film Thickness Column Dimensions Phase Ratio β 30 m x.53 mm x 3.0 μm 44 30 m x.32 mm x 1.8 μm 44 K C = k β β = r 2d f Page 18

High Resolution Megabore (0.45 mm diameter) Same outer diameter as the Megabore No special hardware required Smaller inner diameter (0.45mm) Maintain phase ratio (Beta) Methods are easy to translate!

High Resolution Megabore Column Dimensionsi Phase Ratio β 30 m x.53 mm x 3.0 μm 44 30 m x.45 mm x 2.55 μmm 44

High-SPEED Megabore Same Resolution - Faster Analysis! DB-5 30 m, 053mmID 0.53 I.D., 05µm 0.5 1 2 R = 3.33 3 4 5 36 cm/sec.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0 5.5 6.0 6.5 7.0 7.5 8.0 8.5 9.0 R = 3.32 DB-5 3 30 m, 0.45 mm I.D., 0.42 µm 45.9 cm/sec 1 2 4 5 1. Benzene 2. Toluene 3. Ethylbenzene 4. m,p-xylene 5. o-xylene.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0 5.5 6.0 6.5 7.0 7.5 8.0 8.5 9.0 BTEX Carrier: Helium Oven : 40 C for 3 min, 5 /min to 100 C

High SPEED Megabore Same Resolution - Faster Analysis! Increasing Sample Throughput With High-Speed Megabore Application note 5988-5271EN

Column Diameter and Capacity I.D. (mm) Capacity (ng) 0.05 1-2 0.10 6-13 018 0.18 25-5555 Like Polarity Phase/Solute 0.25 µm film thickness 0.20 35-70 0.25 80-160 032 0.32 110-220 0.45 600-800 0.53 1000-2000 Page 23

Column Diameter - Inlet Head Pressures (Helium) I.D (mm) Pressure (psig) 30 meters 0.05 275-400 0.10 90-130 018 0.18 30-45 0.20 25-40 0.25 15-25 032 0.32 10-20 Hydrogen pressures x 1/2 0.45 3-7 0.53 2-4 Page 24

Diameter Summary If you decrease the inside diameter: Efficiency Resolution Pressure Increase Increase Increase Capacity Decrease Flow rate Decrease Page 25

Resolution N k R = α 1 s 4 k + 1 α Efficiency Retention Selectivity N = ƒ (gas, L, r c ) k = ƒ (T, d f, r c ) α = ƒ (T, phase) L = Length r c = column radius d f = film thickness T = temperature Page 26

Film Thickness and Retention: Isothermal Thickness (µm) Retention Change 0.10 0.40 0.25 1.00 1.0 4.00 3.0 12.0 5.0 20.0 Constant Diameter Normalized to 0.25 µm Page 27

Film Thickness and Resolution When solute k < 5 d f R (early eluters) or T When solute k > 5 (later eluters) d f or T R Page 28

Other Retention - Adsorption Analysis of Noble & Fixed Gases Using HP PLOT MoleSieve 2 4 5 Column: Carrier: Oven: Sample: HP-PLOT/MoleSieve 30 m x 0.53 mm x 50 m HP part no. 19095P-MS0 Helium, 4 ml/min 35 C(3min) to 120 C (5 min) at 25 C/min 250 l, split (ratio 50:1) 6 1 3 1.Neon 2. Argon 3. Oxygen 4. Nitrogen 5. Krypton 6. Xenon 2 4 6 8 Time (min) Page 29

Film Thickness and Capacity Thickness (µm) Capacity (ng) 0.10 50-100 025 0.25 125-250250 0.50 250-300 1 500-1000 3 1500-3000 0.32 mm I.D. Like Polarity Phase/Solute 5 2500-5000 Page 30

Film Thickness and Bleed More stationary phase = More degradation products Page 31

Film Thickness and Inertness 0.25 1.0 3.0 active inactive active inactive active inactive Page 32

Film Thickness Summary If you increase the film thickness: Retention Resolution (k<5) Increase Increase Resolution (k>5) Decrease Capacity Bleed Inertness Efficiency Increase Increase Increase Decrease Page 33

GC Column Dimensions Examples. Page 34

Method 8270 30m x 0.25mm ID, 0.50 μm 25 min run time Page 35

Fast 8270 Semivolatile Analysis 12.5m X 100 μm ID HP-5ms column 7.5 min run time But.is this practical? See Agilent application note #5989-0207EN for more details. Page 36

Running Samples on 100 μm ID Columns Practical? Environmental type samples = high contaminant residue potential. Smaller ID columns have reduced capacity for matrix contaminants due to lower surface area, shorter length (less forgiving). Less surface area a 10 m x.10 mm column has 7.5X less overall surface area than a 30 m x 0.25 mm ID column. A more robust solution might be to switch to a 20 m x 0.18 mm ID column (nice middle-ground between 0.25 and 0.10). These columns could be used in splitless or in split mode, whereas the 0.10 mm ID columns are practically limited to split introduction. Page 37

Fast 8270 Semivolatile Analysis 20m x 0.18mm ID x 0.36um, DB-5.625 13.5 min run time Flow program or faster temperature program? Page 38

Spearmint Oil on DB-1 17.7 min Δ -9.7 97min 018mm 0.18 mm, HeCarrier 0.25 mm, He Carrier 27.4 min 3 8 13 18 23 28 Time (min) Page 39 GC Column Dimension Considerations

Spearmint Oil on DB-1, (App. Note 5989-7509EN) 10.6 min Δ -16.8 min 018mm 0.18 mm, H 2 Carrier 17.7 min Δ -9.7 min 0.18 mm, He Carrier 0.25 mm, He Carrier 27.4 min 3 8 13 18 23 28 Time (min) Page 40 GC Column Dimension Considerations

Spearmint Oil on DB-1 Resolution Check Δ -16.8 min (0.18 mm, H 2 Carrier) 10.6 min Δ -9.7 min (0.18 mm, He carrier) 17.7 min (0.25 mm, He Carrier) 27.4 min GC Column Dimension Considerations Page 41

Food/Fragrance Method translation, Hydrogen Page 42 GC Column Dimension Considerations

OK, Test Time Fusel Oil Simple Standard DB-624 25 m x.53 mm I.D. x 3.0 μm 1 2 Inlet: 250 o C, split FID: 300 o C Carrier: H 2, 50 cm/sec Oven: 40 o C for 5 min. 10 o C/min to 250 o C 1. acetaldehyde 2. methanol 3. 3-methyl-butanol (isoamyl alcohol) 4. 2-methyl-butanol (active amyl alcohol) How would you try to get better R for this? k, α, N? 3 4 C1099 Page 43 0 2 4 6 8 10 Time (min)

Need Plates? Length AND Column Diameter Column Dimensions Theoretical Plates 25 m x.53 mm x 3.0 μm 34,530 60 m x.25 mm x 1.4 μm 181,860 Page 44

Fusel Oil Standard DB-624 60 m x.25 mm I.D. x 1.4 μm Inlet: 250 o C, split FID: 300 o C Carrier: H 2, 50 cm/sec Oven: 40 o C for 5 min. 10 o C/min to 250 o C 1 3 2 4 5 1. acetaldehyde 2. methanol 3. ethanol 4. acetone 5. 1-propanol 6. ethyl acetate 7. isobutanol 8. 1-butanol 9. 3-pentanol (IS) 10. 3-methyl-butanol (isoamyl alcohol) 11. 2-methyl-butanol (active amyl alcohol) 12. hexanol 13. phenylethanol Rs=18 1.8 7 8 9 11 6 10 12 13 C1100 0 5 10 15 20 Time (min) Page 45

CARRIER GAS Carries the solutes down the column Selection and velocity influences efficiency and retention time Page 46

RESOLUTION VS. LINEAR VELOCITY Helium Resolution of 1.5 = baseline resolution 4.50 3.84 3.36 R = 1.46 R = 1.31 R = 0.97 30 cm/sec 35 cm/sec 40 cm/sec 4.4 psig 5.1 psig 5.8 psig DB-1, 15 m x 0.32 mm ID, 0.25 um 60 C isothermal 1,3- and 1,4-Dichlorobenzene Page 47

VAN DEEMTER CURVE OPGV = Optimum Practical Gas Velocity 1.00 H 0.75 0.50 0.25 u opt OPGV 10 20 30 40 50 60 u (cm/sec) Page 48

μ opt and OPGV μ opt : opt Maximum efficiency OPGV: Optimal practical gas velocity Maximum efficiency per unit time 1.5-2x u opt Page 49

COMMON CARRIER GASES Nitrogen Helium Hydrogen Page 50

VAN DEEMTER CURVES 1.00 N 2 H 0.75 0.50 Small 0.25 Large He H 2 10 20 30 40 50 60 u (cm/sec) Page 51 Group/Presentation Title Month ##, 200X

CARRIER GAS Helium vs. Hydrogen Helium (35 cm/sec) Hydrogen (73 cm/sec) 1 3 2 1 4 7 8 2 3 6 5 9 4 6 7 8 5 9 0 2 4 6 8 10 12 Time (min.) 0 2 4 6 8 Time (min.) DB-1, 15 m x 0.25 mm i.d., 0.25 µm 50 C for 2 min, 50-110 C at 20 /min 10.5 min 78 7.8 min Page 52

CARRIER GAS Gas Advantages Disadvantages Nitrogen Cheap, Readily available Long run times Helium Good compromise, Safe Expensive Hydrogen Shorter run times, Cheap Explosive* *Hydrogen is difficult to explode under GC conditions Page 53

Conclusions Make sure what you are doing make sense Try not to make a big change in diameter, take small steps A good place to start is to switch from 0.53 to 0.45 mm id, or 0.32 to 0.25 mm Remember that with a decrease in diameter you will also have a decrease in capacity and flow Avoid 0.100 mm id columns unless you are proficient in 0.18 mm id Use Method Translator Page 54

Thank you! Agilent Technical support can be reached at: 1-800-227-9770 3 3 1 Questions? Page 55