s-sepharose c-101 andy hunter alec mackenzie trevor seelert
TRANSCRIPT
S-SepharoseC-101Andy HunterAlec MackenzieTrevor Seelert
Purpose of UnitSeparate Proinsulin and other
proteins from basic impuritiesPrepare the stream for further
downstream purification
Cation exchange Chromatography
EquilibrateLoadRinseEluteWashRegenerate
Process Flow Sheet
Process Flow Sheet
NewDesign
Process Flow Sheet
NewDesign
S-Sepharose DesignScale-up keeping constant values
Constant Parameter
Vairable Parameters
Column Height Column diameter
Residence time Volumetric flow rates
Linear velocities Amount of eluent
Rinse bed volume
S-Sepharose Design
Parameter Lab Scale Process Scale
Column Height 0.8 m 0.8 m
Residence time 0.376991h 0.376991h
Load linear velocity 212.207 cm/h 212.207 cm/h
Eluent linear velocity 11 936.62 cm/h 11 936.62 cm/h
Column Diameter 0.1 m 1.574 m
Load Volumetric Flowrate
N/A 4.1288 m3/h
Scaled-up from US 101013 Patent
S-Sepharose Design
GE Chromaflow GE AxiChrom
S-Sepharose DesignGE Chromaflow ColumnCurrently max D = 1200mm, H =
30cmCustom Design available for D >
1200mm
Economics and Suppliers
Unit Component Unit Cost
S-Sepharose $1000/L
Annual Report 601.35 L/yr
Total $601 350/yr
Chromatography column $241 000
Other plant direct costs $488 000
First Year TOTAL $1330350
S-Sepharose available from GE Healthcare
Chromaflow supplied by GE
IEC AlternativesSP-Sepharose: Sulphopropyl
–O–CH2CHOHCH2OCH2CH2CH2SO3–
S-Sepharose: Sulphoethyl no longer produced –O–CH2–CH2–SO3–
Replaced by SP-SepharoseAnion exchange resin
Q-sepharose DEAE
HIC ColumnsSEC/Gel Filtration
IEC Alternatives
DEAE: in accordance with German Patent 26 29 568
S-sepharose: in accordance with US Patent 5 101 013
Exchanger DEAE anion exchanger S-Sepharose cation exchanger
Matrix Vinyl polymer Crosslinked agarose gel
Buffer, gradient pH 9, 0.1-0.25 M NaCl pH 3.5, 0.15-0.35M NaCl
Loading 1 g/l 3 g/l
Yield 60% 80%
Purity 80-85% 90-95%
Separation Incomplete separation Base line separation
Comparison of IEC
No Questions Allowed
Disclaimer: The views presented in this slide are not necessarily those of any or all team members.
Just Kidding!