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AEX & Purification

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Page 1: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

AEX & Purification

Page 2: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Purification update

• A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

• However, VLP morphology is not homogenous suggesting some large core-containing complexes are formed

• It is possible that these complexes only form transiently so the time of harvest may need optimisation

• A final “clean-up” step may be required

• Sucrose gradients have been used to generate material for in vivo studies but these are not GMP scaleable

• A combination of SEC and AEX would be ideal but has proven problematic

• Finally, we need to quantify both purity and morphology on a routine basis and so a matrix of data has been proposed

Page 3: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Optimal harvest time

Page 4: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H pHe7 HA2.3,(M2e)3C17-19S.SP UCL fermenter Runs assembly test

• Samples from UCL of fermenter runs 16 (K1,K1 NB1 Harvest sample only) and 20 (HA2.3,(M2e)3C17-19S.SP)

• Samples 1 pre-induction sample.3 samples taken over the induction period at

various times.1 Harvested cell paste sample.

• 2ml each sample run on CL4B XK16/20 in 20mM Tris Ph8.4, 5mM EDTA, 1M Urea

Page 5: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

UV 1_280_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... UV 2_254_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... UV 3_350_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e...Fraction_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... Injection_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2... Run Log_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e)...

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UV 1_280_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... UV 2_254_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... UV 3_350_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e...Fraction_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... Injection_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2... Run Log_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e)...

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KM71H pHe7 HA2.3,(M2e)3C17-19S.SP UCL fermenter Runs assembly test CL4B.

UV 1_280_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... UV 2_254_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... UV 3_350_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e...Fraction_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... Injection_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2... Run Log_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e)...

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UV 1_280_Chrom.1:21-11-14 KM71H phe7 HA2.3,(M2e... UV 2_254_Chrom.1:21-11-14 KM71H phe7 HA2.3,(M2e... UV 3_350_Chrom.1:21-11-14 KM71H phe7 HA2.3,(M2e...Fraction_Chrom.1:21-11-14 KM71H phe7 HA2.3,(M2e... Injection_Chrom.1:21-11-14 KM71H phe7 HA2.3,(M2... Run Log_Chrom.1:21-11-14 KM71H phe7 HA2.3,(M2e)...

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UV 1_280_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... UV 2_254_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... UV 3_350_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e...Fraction_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e... Injection_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2... Run Log_Chrom.1:21-11-14 KM71H pHe7 HA2.3,(M2e)...

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UV 1_280_Chrom.1:21-11-14 KM71H pHe7 K1,K1 16 H... UV 2_254_Chrom.1:21-11-14 KM71H pHe7 K1,K1 16 H... UV 3_350_Chrom.1:21-11-14 KM71H pHe7 K1,K1 16 H...Fraction_Chrom.1:21-11-14 KM71H pHe7 K1,K1 16 H... Injection_Chrom.1:21-11-14 KM71H pHe7 K1,K1 16 ... Run Log_Chrom.1:21-11-14 KM71H pHe7 K1,K1 16 H ...

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73.5hrs Harvest 75.25hrs

K1,K1 Harvest

Time 0 4.58hrs 26.9hrs

Page 6: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H pHe7 HA2.3,(M2e)3C17-19S.SP UCL fermenter Runs assembly test CL4B. Anti-core blot

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Time 0 4.58hrs 26.9hrs

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Harvest 75.25hrs1 min exposure

1 min exposure

1 min exposure 1 min exposure

1 sec exposure1 min exposure

VLP VLP VLP

VLP VLP VLP

Page 7: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H pHe7 HA2.3,(M2e)3C17-19S.SP UCL fermenter Runs assembly test CL4B. Silver stain of peak Void volume fraction (#4) from each run

• These data suggest that optimal expression is found around 24hrs post-induction

• This agrees with shake flask fermentation

• Expression decreases after this time

Vaccine candidate yeast can be grown in fermenters

Page 8: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Sucrose gradients

Page 9: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Purification of VLPs from CL4B-S1000 columns by sucrose gradientVLP samples (all from standard CL4B – S1000 column preps)• KM71H pHe7 K1,K1, 1.4mg/ml.• BL21 coHe7 HA2.3,e, 0.8mg/ml.• BL21 coHe7 HA2.9,e, 0.7mg/ml.

0.5ml each loaded onto 10 – 60% sucrose gradients (13ml) in 20mM Tris pH8.4, 5mM EDTA.

Centrifugation conditions:Beckman SW40 Ti rotor30,000 rpm 3hrs 4oC

RCF (avg) 113652RCF (max)160070k-Factor 244.1

0.5ml fractions collected from bottom.

Page 10: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Location of core in gradients by dot and western blot

“Goldilocks” VLP region

Page 11: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Summary of results

• The presence of sucrose, particularly in early samples negatively impacted TEM analysis due to low adherence of proteins to the grids and poor staining.

• PHe7K1K1 VLPs increased in numbers from fractions 14 to 18. However, the lower numbers of VLPs in the earlier fractions may have been due to higher concentrations of sucrose (up to 4 %) in these diluted samples. Further dilution is unlikely to improve analysis as the resulting concentration of VLPs would be too low for TEM analysis.

• For the E.coli expressed VLPs, no VLPs were seen in fraction numbers lower than 16. Again, this is most likely due to the high concentration of sucrose in these fractions.

• BL21 CoHe7HA2.3: Large VLP assemblies were seen in fraction 16 with increasing debris present in later fractions.

• BL21 CoHe7HA2.9: VLPs were only seen in fraction 18 but these tended to be within aggregates or clumps.

Page 12: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

YEAST produced VLPs passed over sucrose gradient post FPLC: SDS-PAGE/Western Blot of fractions.

Fractions pooled for each construct and sucrose concentration reduced from ~40% to <1% by dilution and re-concentration on 10kDa cut off spin filters.

Fractions of KM71H pHe7 HA2.3,(M2e)3C17.19S.SP also pooled and sucrose reduced to <1% in same way.

Final concentration and volumes.

VLP pool (#): 1.0mg/ml. 1.5ml. Total yield 1.5mgDirty pool (#):2.3 mg/ml. 1.5ml. Total yield 3.4mg

Page 13: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

pHe7 HA2.3,(M2e)3C17,19SSucrose gradient purified VLP

Goldilocks VLP region Three bears VLP region

Sucrose cushions can be used to improve the homogeneity of yeast VLP morphology

This process is not perfect but should allow in vivo testing to continue

Page 14: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

AEX development-AEX polish of SEC purified VLP

Page 15: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H K1,K1 VLP AEX on CIM-DEAE

UV 1_280_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP C... UV 2_254_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP C... UV 3_350_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP C...Fraction_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP C... Injection_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP ... Run Log_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP CI...

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All protein bound but nothing eluted by salt gradient or 1M NaOH

UV 1_280_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP p...UV 2_254_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP p...Cond_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP pH7.0...Conc B_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP pH7...PreC pressure_Chrom.1:25-9-14 KM71H pHe7 K1,K1 ... Fraction_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP p...Injection_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP ... Run Log_Chrom.1:25-9-14 KM71H pHe7 K1,K1 VLP pH...

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• Using prep from high copy clone.• VLP positive fractions from S1000 (41-50)

concentrated to 0.58mg/ml.• Run on CIMmultus QA-1 monolith column (1ml

column)• Buffer A – 20mM Tris pH 8.4, 5mM EDTA• Buffer B – 20 mM Tris pH 8.4, 5mM EDTA,

1M NaCl• Final wash – 1M NaOH, 1M NaCl• 2ml sample loaded

• Method run (based on column volumes)• Column pre-equilibration (5 CV

Buffer A)• Sample load (2ml)• Column wash (5 CV Buffer A)• Elution (10 CV 0 – 50% linear

gradient Buffer B.• Step to 100% Buffer B (10 CV) • High salt wash (5 CV 100% Buffer

B)• Low salt wash (5 CV Buffer A)• NaOH wash (5 CV 1M NaOH)•

Page 16: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H K1,K1 VLP AEX on CIM-DEAE

UV 1_280_Chrom.1:Manual Run 010 Cond_Chrom.1:Manual Run 010 Conc B_Chrom.1:Manual Run 010 PreC pressure_Chrom.1:Manual Run 010Run Log_Chrom.1:Manual Run 010

11511010510095908580757065605550454035302520151050

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20

10

0

-10

-20ml

mAU

Ma

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al R

un

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CIM-DEAE regeneration protocol• Wash 1M NaCl, 1M NaOH (20

CV)• Hold over night in 1M NaCl, 1M

NaOH• Wash 1M NaCl, 1M NaOH (10

CV)

• Wash H2O (20 CV)

• Wash 30% 2-Propanol (20 CV)

• Wash H2O (20 CV)

Hold O/N

Protein is tightly bound to matrix, only partially released by over-night soak in NaOH.Most seems to be bound by hydrophobic interaction since released by 2-Propanol

Page 17: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H HA2.3,(M2e)3C17-19S.SP VLP AEX on CIM-QA

Input run directly through UV detector before loading onto CIM-QA

All protein bound but only 25% of OD280 in input eluted by salt gradient or even after 1M NaOH, 1M NaCl. Therefore, protein lost on column.

UV 1_280_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)3... Cond_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)3.C17... Conc B_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)3.C...PreC pressure_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(... Fraction_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)3... Injection_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)...UV 1_280@01,BASEM_Chrom.1:9-1-15 KM71H pHe7 HA2... Run Log_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)3....

2.32.22.121.91.81.71.61.51.41.31.21.110.90.80.70.60.50.40.30.20.10

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UV 1_280_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)3... UV 2_254_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)3... Cond_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)3.C17...Conc B_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)3.C... Fraction_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)3... Injection_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)...Run Log_Chrom.1:9-1-15 KM71H pHe7 HA2.3,(M2e)3....

65605550454035302520151050

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Page 18: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H HA2.3,(M2e)3C17-19S.SP VLP AEX on CIM-QACIM-QA acid wash regeneration protocol• 20mM Tris pH 7.0, 5mM EDTA • 50% Acetic acid• 20mM Tris pH 7.0, 5mM EDTA • 50% Acetic acid• 20mM Tris pH 7.0, 5mM EDTA

UV 1_280_Chrom.1:Method Run 008 UV 2_254_Chrom.1:Method Run 008 Conc B_Chrom.1:Method Run 008 PreC pressure_Chrom.1:Method Run 008Run Log_Chrom.1:Method Run 008

8580757065605550454035302520151050

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Missing protein eluted in 1st acid wash

Although protein levels are low, nucleic acid still appears to be bound to the column

Page 19: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H HA2.3,(M2e)3C17-19S.SP VLP AEX on CIM-QA

CIM-QA Benzonase regeneration protocol• 50mM Tris pH 7.4, 2mM MgCl2,

0.1M NaCl • 200u/ml Benzonase• Hold over-night 37oC (#)• 50mM Tris pH 7.4, 2mM MgCl2,

0.1M NaCl UV 1_280_Chrom.1:Manual Run 010 UV 2_254_Chrom.1:Manual Run 010 Conc B_Chrom.1:Manual Run 010 PreC pressure_Chrom.1:Manual Run 010Injection_Chrom.1:Manual Run 010 Run Log_Chrom.1:Manual Run 010

302826242220181614121086420-2-4-6-8-10-12-14-16-18-20

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UV 1_280_Chrom.1:13-1-15 CIMmultus QA-1 column ... UV 2_254_Chrom.1:13-1-15 CIMmultus QA-1 column ... Cond_Chrom.1:13-1-15 CIMmultus QA-1 column post...Conc B_Chrom.1:13-1-15 CIMmultus QA-1 column po... PreC pressure_Chrom.1:13-1-15 CIMmultus QA-1 co... Run Log_Chrom.1:13-1-15 CIMmultus QA-1 column p...

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CIM-QA acid wash regeneration protocol following Benzonase treatment• 20mM Tris pH 7.0, 5mM EDTA • 50% Acetic acid• 20mM Tris pH 7.0, 5mM EDTA • 50% Acetic acid• 20mM Tris pH 7.0, 5mM EDTA

Post Benzonase treatment acid wash elutes protein (small amount) and further nucleic acid

Page 20: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H HA2.3,(M2e)3C17-19S.SP VLP AEX on CIM-QA at pH 7.0

Input run directly through UV detector before loading onto CIM-QA

Nucleic acid content not significantly reduced by AmS04 ppt

All protein boundNo OD280 in input eluted by salt gradient

VLP precipitated by 40% AmSO4 in attempt to reduce nucleic acid content

UV 1_280_Chrom.1:13-1-15 KM71H pHe7 HA2.3,(M2e)... UV 2_254_Chrom.1:13-1-15 KM71H pHe7 HA2.3,(M2e)... Cond_Chrom.1:13-1-15 KM71H pHe7 HA2.3,(M2e)3 SP...Fraction_Chrom.1:13-1-15 KM71H pHe7 HA2.3,(M2e)... Injection_Chrom.1:13-1-15 KM71H pHe7 HA2.3,(M2e... Run Log_Chrom.1:13-1-15 KM71H pHe7 HA2.3,(M2e)3...

2.32.22.121.91.81.71.61.51.41.31.21.110.90.80.70.60.50.40.30.20.10

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60

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56

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56545250484644424038363432302826242220181614121086420

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Page 21: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H VLP stability at lower pH

• Intention to use CIM-DEAE to purify yeast VLPs at lower pH. To allow this SEC purified VLPs (stored in 20mM Tris, 5mM EDTA pH 8.4) were buffer exchanged to 20mM Tris pH 7.0 or 50mM Na-Citrate buffer pH 6.0 using CL-4B (XK16/20).

• VLPs are expected to elute in void volume.

• Exchanging K1,K1 to pH 6.0 retains integrity of VLPs as shown by elution in expected region.

But

• Exchanging HA2.3,(M2e)3.C17.19S.SP VLP to pH 6.0 appears to cause VLPs to dissociate to constituent units.

• Exchanging HA2.3,(M2e)3C17.19S.SP VLP to pH 7.0 appears to be causing an intermediate level of instability.

• A secondary observation is that Nucleic acid also moves to the small molecule region of the column. This provides further evidence that the nucleic acid present in the VLP region is there due to it being part off or attached to VLPs.

Page 22: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H VLP stability at lower pH

UV 1_280_Chrom.1:16-1-15 KM71H pHe7 K1,K1 CL4B ... UV 2_254_Chrom.1:16-1-15 KM71H pHe7 K1,K1 CL4B ... Fraction_Chrom.1:16-1-15 KM71H pHe7 K1,K1 CL4B ...Injection_Chrom.1:16-1-15 KM71H pHe7 K1,K1 CL4B... Run Log_Chrom.1:16-1-15 KM71H pHe7 K1,K1 CL4B S...

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leted)>

K1,K1 pH 8.4 → 6.0

Fractions from Void peak held at pH 6.0 for 72 hrs and then re- run on CL4BShows that K1,K1 is also unstable at low pH over extended periods

Page 23: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H HA2.3,(M2e)3C17-19S.SP VLP AEX on CIM-DEAE pH 7-4 Step Gradient

Page 24: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H HA2.3,(M2e)3C17-19S.SP VLP AEX on CIM-DEAE pH 7-4 1M NaCl Step Gradient

Core eluted at pH7 1M NaCl is lost on concentration – suggesting aggregation

Page 25: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H HA2.3,(M2e)3C17-19S.SP VLP AEX on CIM-DEAE pH 7-4 1M NaCl Step Gradient

• pH 7 0-1M NaCl gradient • Step pH 4 for 5 CV• Re-ran pH 7 0-1M NaCl gradient

Page 26: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

AEX development-AEX on lysate

Page 27: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Fract

ion 3

Fract

ion 4

Fractio

n 18

Fractio

n 19

Fract

ion 1

6

Fract

ion 1

5

rHBc

(50n

g)

Mar

ker

Inpu

t

Fract

ion 6

Fra

ction

17

Fractio

n 20

Note – Only detectable core signal is from fraction at end of sample loading period. Indicating that at this point column had become saturated in ability to bind core. Coomassie stain confirms this for other proteins also.

5 sec exposure 10 min exposure

KM71H HA2.3,(M2e)3C17-19S.SP VLP lysate without urea. AEX on CIM-DEAE 1M NaCl gradient pH 8.4

Page 28: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H HA2.3,(M2e)3C17-19S.SP VLP lysate in 1M urea. AEX on CIM-DEAE 1M NaCl gradient pH 8.4

UV 1_280_Chrom.1:22-1-15 KM71H pHe7 HA2.3,(M2e)... UV 2_254_Chrom.1:22-1-15 KM71H pHe7 HA2.3,(M2e)... Conc B_Chrom.1:22-1-15 KM71H pHe7 HA2.3,(M2e)3....Fraction_Chrom.1:22-1-15 KM71H pHe7 HA2.3,(M2e)... Injection_Chrom.1:22-1-15 KM71H pHe7 HA2.3,(M2e... Run Log_Chrom.1:22-1-15 KM71H pHe7 HA2.3,(M2e)3...

65605550454035302520151050-5

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mAU

Waste^

29

28

27

Waste^

25

24

23

^^

20

19

18

17

16

15

14

^

12

11

10

765432

Meth

od R

un 1

/22

/201

5 1

1:3

0:2

3 A

M +

00:0

0 M

eth

od: C

IMm

ultus D

EA

E-1

AE

X R

esult: /D

efa

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om

e/A

KT

Apure

(...

>

End

_B

lock (

Issue

d)

(Pro

ce

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g)

(Com

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_B

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End

_B

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(Pro

ce

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_B

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(Pro

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(Com

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End

_B

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Issue

d)

(Pro

ce

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(Com

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ted

)>

End

_B

lock (

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(Pro

ce

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g)

(Com

ple

ted

)>

End

_B

lock (

Issue

d)

(Pro

ce

ssin

g)

(Com

ple

ted

)>

End

_B

lock (

Issue

d)

(Pro

ce

ssin

g)

(Com

ple

ted

)>

End

_B

lock (

Issue

d)

(Pro

ce

ssin

g)

(Com

ple

ted

)>

Fract

ion 3

Fract

ion 4

Fractio

n 19

Fractio

n 20

Fract

ion 1

7

Fract

ion 1

6

rHBc

(50n

g)

Mar

ker

Inpu

t

Fract

ion 6

Fra

ction

18

Fractio

n 23

Note – loaded at half total protein load compared to previous sample.No apparent breakthrough of core, coomassie indicates breakthrough of other proteins.Some core signal detected in gradient at ~40% salt (0.4M NaCl)

10 min exposure

Fracti

on 1

6

Fracti

on 1

7

Fractio

n 17 1

M ur

ea

Fractio

n 18 1

M ur

ea

Fracti

on 2

0

Fracti

on 1

9

rHBc (

50ng

)

Mar

ker

Fracti

on 1

5

Fracti

on 1

8 Fra

ction

16

1M u

rea

Fractio

n 19 1

M ur

ea

10 min exposure

After concentration (4x), core signal was detectable.• Sample

without urea treatment eluting over 55 – 88% salt. Some eluting at 100%.

• Sample with urea treatment eluting at 40%.

Page 29: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H K1,K1 VLP lysate without urea AEX on CIM-DEAE 1M NaCl gradient pH 8.4

UV 1_280_Chrom.1:29-1-15 KM71H pHe7 K1,K1 lysat... UV 2_254_Chrom.1:29-1-15 KM71H pHe7 K1,K1 lysat... Conc B_Chrom.1:29-1-15 KM71H pHe7 K1,K1 lysate ...Fraction_Chrom.1:29-1-15 KM71H pHe7 K1,K1 lysat... Injection_Chrom.1:29-1-15 KM71H pHe7 K1,K1 lysa... Run Log_Chrom.1:29-1-15 KM71H pHe7 K1,K1 lysate...

65605550454035302520151050-5

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0

-50ml

mAU

Waste^

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Waste^

25

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23

^^

20

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18

17

16

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14

^

12

11

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765432

Meth

od R

un 1

/29/2

015 1

0:0

9:5

2 A

M +

00:0

0 M

eth

od:

CIM

multus D

EA

E-1

AE

X R

esult:

/Defa

ultH

om

e/A

KTA

pure

(..

.>

End_B

lock (

Issued)

(Pro

cessin

g)

(Com

ple

ted)

>

End_B

lock (

Issued)

(Pro

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(Com

ple

ted)

>

End_B

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(Pro

cessin

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(Com

ple

ted)

>

End_B

lock (

Issued)

(Pro

cessin

g)

(Com

ple

ted)

>

End_B

lock (

Issued)

(Pro

cessin

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(Com

ple

ted)

>

End_B

lock (

Issued)

(Pro

cessin

g)

(Com

ple

ted)

>

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lock (

Issued)

(Pro

cessin

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(Com

ple

ted)

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End_B

lock (

Issued)

(Pro

cessin

g)

(Com

ple

ted)

>

End_B

lock (

Issued)

(Pro

cessin

g)

(Com

ple

ted)

>

Fract

ion 3

Fract

ion 4

Fractio

n 18

Fractio

n 20

Fract

ion 1

6

Fract

ion 1

5

rHBc

(50n

g)

Mar

ker

Inpu

t

Fract

ion 6

Fra

ction

17

Fractio

n 23

• Significant core in all of flow-through indicating that column has saturated in ability to bind core (possibly higher core content of K1,K1 or lower affinity for DEAE of K1,K1.)

• Core signal eluting over 20 – 54% salt.

• At higher salt increase in high molecular weight aggregate seen.

1 sec exposure 10 min exposure

Page 30: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H K1,K1 VLP lysate in 1M urea AEX on CIM-DEAE 1M NaCl gradient pH 8.4

UV 1_280_Chrom.1:29-1-15 KM71H pHe7 K1,K1 VLP 1... UV 2_254_Chrom.1:29-1-15 KM71H pHe7 K1,K1 VLP 1... Conc B_Chrom.1:29-1-15 KM71H pHe7 K1,K1 VLP 1M ...Fraction_Chrom.1:29-1-15 KM71H pHe7 K1,K1 VLP 1... Injection_Chrom.1:29-1-15 KM71H pHe7 K1,K1 VLP ... Run Log_Chrom.1:29-1-15 KM71H pHe7 K1,K1 VLP 1M...

65605550454035302520151050-5

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Waste^

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^^

20

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18

17

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14

^

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Meth

od R

un 1

/29/2

015 1

1:1

1:4

3 A

M +

00:0

0 M

eth

od:

CIM

multus D

EA

E-1

AE

X R

esult:

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om

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KTA

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colle

ction s

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dju

ste

d f

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e U

V c

ell

path

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1/2

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015 4

:34:0

1 P

M +

00:0

0 (

Issued)

(Manual)

>

Inle

t A

A2 (

Issued)

(Manual)

>

End 1

/29/2

015 6

:01:0

0 P

M +

00:0

0 (

Issued)

(Manual)

>

Note – by end of this run back-pressure on had increased to a level at which column can no longer be used

Fract

ion 3

Fract

ion 4

Fractio

n 20

Fractio

n 23

Fract

ion 1

7

Fract

ion 1

6

rHBc

(50n

g)

Mar

ker

Inpu

t

Fract

ion 6

Fra

ction

18

Fractio

n 24

1 sec exposure10 min exposure

• Flow through exhibits strange behaviour, core signal decreasing, this cannot happen on AEX unless material is aggregating and fouling column – decrease in signal corresponds to rapid increase in back-pressure.

• Core signal eluting between 40 – 60% salt

Page 31: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H pHe7 K1,K1 High Copy Number Clone lysate and lysate after 1M urea loaded onto CIMmultus DEAE AEX fractions desalted and 4 fold concentrated

Fract

ion 1

6

Fract

ion 1

7

Fractio

n 17 1

M

ureaFrac

tion 1

8 1M

urea

Fract

ion 2

3

Fract

ion 2

0

rHBc

(50n

g)

Mar

ker

Fract

ion 1

5

Fract

ion 1

8 Fra

ction

16

1M u

rea

Fractio

n 20 1

M ur

ea

• K1,K1 binds with lower affinity than HA2.3,(M2e)3C17-19S.SP

• Sample without urea elutes mainly ~ 20 - 50% salt

• With urea elutes over similar salt range.

• Urea does not seem to lower affinity of K1,K1 for DEAE 1 sec exposure 10 min exposure

Page 32: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H HA2.3,(M2e)3C17-19S.SP and K1,K1 VLP Lysate with and without 1M urea AEX on CIM-DEAE

Overall conclusions

• Both constructs bind DEAE

• K1,K1 has lower affinity than HA2.3,(M2e)3C17-19S.SP

• Urea treatment of HA2.3,(M2e)3C17-19S.SP reduces affinity to similar value as K1,K1

• Overall recovery is low for both proteins – large amount of material appears to foul column

• Urea treated K1,K1 loading of column resulted in complete blockage of column – but it is possible that this was result of cumulative fouling rather than specific to K1,K1.

Page 33: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Is urea necessary for SEC preparation?

Page 34: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H pHe7 HA2.3,(M2e)3C17-19S.SP High Copy Clone VLP prep without urea

• Using High Copy clone (as defined by qPCR). Yeast induced without prior starvation period.

• 26g cells resuspended in 320ml lysis buffer (20mM Tris pH 8.4, 2mM AEBSF, 5mM DTT, 3000U Benzonase (93u/g)) lysed by pressure homogenisation 500 bar, 3 passes

• Soluble core extracted from crude lysate with 0.1% Triton X-100 for 1 hr and then centrifuged ~20k x g, 30mins, 4oC

• Supernatant (320ml) diluted with 320ml 20mM Tris pH 8.4, 10mM EDTA, to give a final buffer of 20mM Tris pH 8.4, 5mM EDTA. Note – 1M Urea was omitted from this buffer. Vacuum filtered through 0.8µm, 0.45µm and 0.22µm membrane filters

• Final filtrate washed on 1MDa Pellcon TFF, reducing volume to 25ml. MDa retentate sonicated 2 x 10 sec at 50% power.

• Then filtered through 0.2µm syringe filter followed by 0.1µm syringe filter (filter washes with SDS buffer after use). Significant back pressure observed on passage through 0.2µm and 0.1µm filter. Stored overnight at 4oC. Soincated 2 x 10 sec, Then re-filtered (0.2µm).

• VLPs purified using 2-step Automated AKTAPure program• Filtrate applied to Sepharose 4B column (XK26/92) in 20mM Tris pH 8.4, 5mM EDTA,

Note – no Urea in this stage. • Void volume material (160-205ml corresponding to fractions 4 – 8 in previous method,

45ml) applied to Sephacryl S1000 column (XK50/92) in 20mM Tris pH 8.4, 5mM EDTA,

Page 35: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H pHe7 HA2.3,(M2e)3C17-19S.SP High Copy Clone VLP +/- urea: CL4B comparison to same scale

• Without urea void region is 70% of + Urea, Small protein regions are equal +/- urea• Without urea more large size material is being removed on filters

Page 36: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H pHe7 HA2.3,(M2e)3C17-19S.SP High Copy Clone VLP prep without urea: CL4B Void on XK 50/92 S1000

UV 1_280_Chrom.1:13-2-15 KM71H pHe7 HA2.3,(M2e)... UV 2_254_Chrom.1:13-2-15 KM71H pHe7 HA2.3,(M2e)... UV 3_350_Chrom.1:13-2-15 KM71H pHe7 HA2.3,(M2e)...Fraction_Chrom.1:13-2-15 KM71H pHe7 HA2.3,(M2e)... Injection_Chrom.1:13-2-15 KM71H pHe7 HA2.3,(M2e... Run Log_Chrom.1:13-2-15 KM71H pHe7 HA2.3,(M2e)3...

22002100200019001800170016001500140013001200110010009008007006005004003002001000

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2

0 ml

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^

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Method R

un 2/13/2

015 10:2

7:04 AM

+00:00 M

ethod: S1

000 SEC

XK 50-92

Multi-step

Result: /D

efaultHom

e/A...

>

End_Bloc

k (Issued)

(Process

ing) (Com

pleted)

>

Data colle

ction setti

ngs adjust

ed for cur

ve UV 1_

280.>

End_Bloc

k (Issued)

(Process

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Data colle

ction setti

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End_Bloc

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(Process

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pleted)

>

UV 1_280_Chrom.1:20-1-15 KM71H pHe7 HA2.3,(M2e)... UV 2_254_Chrom.1:20-1-15 KM71H pHe7 HA2.3,(M2e)... UV 3_350_Chrom.1:20-1-15 KM71H pHe7 HA2.3,(M2e)...Fraction_Chrom.1:20-1-15 KM71H pHe7 HA2.3,(M2e)... Injection_Chrom.1:20-1-15 KM71H pHe7 HA2.3,(M2e... Run Log_Chrom.1:20-1-15 KM71H pHe7 HA2.3,(M2e)3...

22002100200019001800170016001500140013001200110010009008007006005004003002001000

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65

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55

50

45

40

35

30

25

20

15

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5

0 ml

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78

^

76

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74

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72

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70

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Waste^̂̂

Method R

un 1/20/2

015 10:4

0:10 AM

+00:00 M

ethod: S1

000 SEC

XK 50-92

Multi-step

Result: /D

efaultHom

e/AKT...

>

End_Bloc

k (Issued)

(Process

ing) (Com

pleted)

>

Data colle

ction setti

ngs adjust

ed for cur

ve UV 1_

280.>

End_Bloc

k (Issued)

(Process

ing) (Com

pleted)

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ngs adjust

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ve Cond.

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pleted)

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0

100

0

200

No Urea

1M Urea

Page 37: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H pHe7 HA2.3,(M2e)3C17-19S.SP High Copy CloneVLP prep without urea CL4B VoidRun on S1000 XK50/92

rHBc

(50n

g)Mar

ker

#70

#38

#44

#47

#50

#53

#56

#59

#41

#65

rHBc

(50n

g)Mar

ker

#2 (I

nput

)#8 #10#18

#20

#23 #26

#29

#32

#35 rH

Bc (5

0ng)

Mar

ker

#70

#38

#44

#47

#50

#53

#56

#59

#41

#65

rHBc

(50n

g)

Mar

ker

#2 (I

nput

)#8 #10#18

#20

#23 #26

#29

#32

#35

No Urea 1M Urea

Increased degradation in absence of urea

Page 38: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Purification of VLPs from CL4B-S1000 columns by sucrose gradient

rHBc

(50n

g)

Mar

ker

#26

#7 #12

#14

#16

#18

#20

#22

#10

#24

rHBc

(50n

g)

Mar

ker

#26

#7 #12

#14

#16

#18

#20

#22

#10

#24

KM71H pHe7 K1,K1

60% 10%

KM71H pHe7 HA2.3,(M2e)3C17.19S.SP

1M Urea Yield = 0.04mg/g

rHBc

(50n

g)

Mar

ker

#26

#7 #12

#14

#16

#18

#20

#22

#10

#24

KM71H pHe7 HA2.3,(M2e)3C17.19S.SP

No Urea Yield = 0.05mg/gWithout Urea more core in ‘Goldilocks’ zone but more degradation – need EMs

Page 39: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Data reporting matrix

Page 40: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H pHe7 HA2.3,M2e Twin High Copy Clone VLP prep

• Using High Copy (~) clone (as defined by qPCR). Yeast induced without prior starvation period.

• 26g cells resuspended in 320ml lysis buffer (20mM Tris pH 8.4, 2mM AEBSF, 5mM DTT, 3000U Benzonase (93u/g)) lysed by pressure homogenisation 500 bar, 3 passes

• Soluble core extracted from crude lysate with 0.1% Triton X-100 for 1 hr and then centrifuged ~20k x g, 30mins, 4oC

• Supernatant (480ml) diluted with 320ml 20mM Tris pH 8.4, 10mM EDTA, 2M Urea to give a final buffer of 20mM Tris pH 8.4, 5mM EDTA 1M Urea. Vacuum filtered through 0.8µm, 0.45µm and 0.22µm membrane filters

• Final filtrate washed on 1MDa Pellicon TFF, reducing volume to 25ml. Unlike other higher copy clones no detectable back pressure detected.

• Then filtered through 0.2µm syringe filter followed by 0.1µm syringe filter (filter washes with SDS buffer after use). Significant back pressure observed on passage through 0.2µm and 0.1µm filter (2 x 0.1µm units used)

• Stored overnight at 4oC. Sonicated 2 x 10 sec, Then re-filtered (0.2µm). • VLPs purified using 2-step Automated AKTAPure program• Filtrate applied to Sepharose 4B column (XK26/92) in 20mM Tris pH 8.4, 5mM EDTA,

1M Urea. • Void volume material (160-205ml corresponding to fractions 4 – 8 in previous method,

45ml) applied to Sephacryl S1000 column (XK50/92) in 20mM Tris pH 8.4, 5mM EDTA,

Page 41: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H pHe7 HA2.3,M2e Twin High Copy Clone VLP prep

20K

s/n

20K

pell

et D

il s/n

0.1

filtra

te

Perm

etat

eM

Da Son

icate

d

CL4B In

put

0.1

filter

SDS w

ash

MDa

0.2

filtra

te

rHBc

(50n

g)

Mar

ker

Crude

lysa

te

1 sec exposure

100 200 300 400 500 600 700 800 900 10000

1

2

3

4

5

6

f(x) = 4.78434844391888 x^-0.500280863942421R² = 0.970418764248172

Flux ml/min

Flux ml/...

Permeate (total vol) ml

Flu

x ra

te (

ml/

min

)

TFF

CL4B

Page 42: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

KM71H pHe7 HA2.3,M2e Twin High Copy Clone VLP prep: CL4B Void on XK 50/92 S1000

Fractions pooled and concentrated to 10ml on 1MDa Pellicon. Then to 3ml on 10kDa spin filter.

VLP Pool = #41 - 53, protein concentration 8mg/ml, total yield 24mg

VLP

VLP

Page 43: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Purification of VLPs from CL4B-S1000 columns by sucrose gradient: SDS-PAGE/Western Blot of fractions.

rHBc

(50n

g)

Mar

ker

#26

#7 #12

#14

#16

#18

#20

#22

#10

#24

60% 10%

Fractions pooled and sucrose concentration reduced from ~40% to <1% by dilution and re-concentration on 10kDa cut off spin filters.

Final concentration and volumes.

VLP pool (#): 0.57mg/ml. 1.5ml. Total yield 0.86mgDirty pool (#): 0.35mg/ml. 1.5ml. Total yield 0.53mg

Page 44: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Biochemistry summary data

Parameter Value Units

Volume of culture 1.8 L

Wet weight pellet 26 g

Band visible on initial gel? Y (Y/N)

TFF y = 4.7843x-0.5

R² = 0.9704Equation

AUC (S1000 fractions) 27.5 mAu*ml

Purity (image analysis) 20% %

Amount recovered 24 mg

Yield 0.09 %

Purity sucrose (image analysis) 20% %

Amount recovered sucrose 0.86 mg

Yield sucrose 0.003 %

EM (image analysis) % VLP

Page 45: AEX & Purification. Purification update A reproducible method for VLP purification has been developed which routinely produces material of 80% plus purity

Image analysis

S1000 Sucrose

1 648.719 398.284 337.042 2202.77 2119.2052 2115.276 2130.548 2327.861 1584.234 1052.2343 2555.205 2089.598 1987.355 2838.225 1394.447

TC 2494.933 1792.497 1778.355 2164.175 2136.9125 1430.154 2281.962 2519.569 190.263 1617.0546 400.527 133.385 2362.1257 1752.497 2016.125 400.3358 1854.154 851.284 3009.832

Total 13251.47 11693.68 14722.47 8979.667 8319.852% purity 18.8% 15.3% 12.1% 24.1% 25.7% 19.2%

1 1942.598 1846.719 2116.891 2018.0622 3274.912 3911.083 3326.669 3846.79

TC 2152.255 2266.719 1980.184 1596.1844 757.456 899.698 728.163 616.4565 477.335 514.113 382.213 899.1846 1873.912 1464.083 1118.548 259.092

Total 10478.47 10902.42 9652.668 9235.768% Purity 20.5% 20.8% 20.5% 17.3% 19.8%