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Anion Exchanger
M. Awais Yaqoob
2011-ch-32
(University of Engineering and Technology, Lahore)
Outline
 Background
 Why an anion exchanger?
 Alternatives
 Design
 Resins
 Cost of chosen design
 Questions
Background
 Ions are electrostatically bound to an
insoluble and chemically inert matrix
– Anion exchangers bear positively charged
functional groups that bind negatively charged
particles.
 During elution the anion exchanger can be
described by the following chemical
equation:
Why an anion exchanger?
Assumptions
•Denatured insulin had a 0% binding efficiency
•Insulin-Ester had a 100% binding efficiency and 90% recovery
•Isoelectric point of Denatured Insulin is higher than Insulin-Ester
Component
Flowrate
(kg/batch)
Mass Percent
(%)
Conc.
(g/L)
Denatured Insulin 0.4359 0.03 0.30
Insulin-Ester 296.38 20.22 202.25
Water 1168.65 79.75 797.46
Anion Exchanger Advantages
 Capable of handling
large volumes
 Efficient, precise
separation
– Accurate separation of
Insulin ester and
denatured Insulin
1
 Large pressure drop
– Require expensive pumps
 High resolution requires small beads
– Small beads decrease flow rate
 Each cycle requires several stages
– Charging, sample input, washing, elution,
cleaning
Anion Exchanger Disadvantages
Alternatives
 Membrane Chromatography
 Exclusion Chromatography
 Affinity Chromatography
2 3 4
Membrane Chromatography
 Allows for much larger throughput (about 100
times that of ion exchange) and a higher
efficiency
 Uses microporous membrane
 Small pressure drop compared to traditional
ion exchangers
 Scaling up separation is simplified
Exclusion Chromatography
 Separates on basis of
Molecular Mass
 Column is filled with semi-
solid beads of a polymeric
gel
– The porosity of the gel can
be changed as to exclude
molecules of a set size
 Useful for samples
containing many types of
proteins 5
Affinity Chromatography
 Matrix anchored ligand
– Specifically binds to
protein of interest
 Can exploit protein’s
unique biochemical
properties instead of
charge in ion exchange
 Requires low flowrates
8
Anion Exchanger Design
 Ergun Equation for pressure drop in a packed
bed
( ) µε
ρ
⋅−
⋅



⋅
=
1
Re
A
QDp
75.1
Re
150
+=Pf
( )ε
ε
ρ
−
⋅




⋅⋅
=∆
⋅
1
2
P
solutionp
D
A
QLf
P
Design Considerations
Property Dimension
Bead Diameter, DP
35μm
Column Lenth, L 3.47m
Column Diameter, D 1.3 m
Pressure Drop, ΔP 1718 kPa
Void Fraction, ε 0.4
Vessel Volume 4604 L
All constants were taken from Perry’s Chemical Engineering Handbook
7
Vessel Sizing
 Exchanger is very large
– Much larger than needed, however, this will save
on pumping costs
 Total flow rate through the anion exhanger is
1.721 x 10-5
m3
/s
– Based on 80h batch time and 826kg/batch
– Scaled up by a factor of 6
Vessel Schematic
P&ID
1
Resins
 Serves as the media for stationary phase
– Polymeric matrix with immobilized charged
functional groups
 Quaternary Ammonium functional group
 Diethylaminoethane functional group
 Can be regenerated in the columns and
used for many production cycles
– anionic resin: 500 - 1,000 cycles
8
Estimated Costs for Anion Exchanger
Unit Cost/Unit # of Units Total
Anion Exchanger $261,000 1 $261,000
Resin ~9 $/L 110 $910
Peripheral Equip. $50,000 N/A $50,000
Shipping $2,000 1 $2,000
Installation $100,000 N/A $100,000
Controls/Software $25,000 1 $25,000
Total Equip. Cost $438,910
Estimated Operation Costs / Year
Operation Total
Utilities $10,000
Maintenance $5,000
Supplies $1,000
Total Operations $16,000
*Overhead costs,
taxes and insurance
costs have not been
included in this
estimate
The total cost associated with the purchase of an Anion
Exchanger with one year of operation is approximately
$454,910.
References
[1] PowerMax, 2006
http://www.usfilter.com/
[2] Pall Corporation, 2006
(http://www.pall.com/datasheet_biopharm_36585.asp)
[3] Protein Chemistry, 2006
(http://fig.cox.miami.edu/~cmallery/255/255tech/255techniques.htm)
[4] Voet & Voet Biochemistry 3rd
Edition, Wiley, 2004
[5] Waters Corporation, 2006 (http://www.waters.com/watersdivision/)
[6] Novasep Technologies, 2006
(http://www.novasep.com/technologies/ion-exchange.asp)
[7] Graver Technologies, 2006
(http://www.gravertech.com/pdfs/literature/ionex/IonExchangeResinSelection.pdf)
[8] OR-Live, 2003
http://www.biopharminternational.com/
Questions ?

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Anionexchanger

  • 1. Anion Exchanger M. Awais Yaqoob 2011-ch-32 (University of Engineering and Technology, Lahore)
  • 2. Outline  Background  Why an anion exchanger?  Alternatives  Design  Resins  Cost of chosen design  Questions
  • 3. Background  Ions are electrostatically bound to an insoluble and chemically inert matrix – Anion exchangers bear positively charged functional groups that bind negatively charged particles.  During elution the anion exchanger can be described by the following chemical equation:
  • 4. Why an anion exchanger? Assumptions •Denatured insulin had a 0% binding efficiency •Insulin-Ester had a 100% binding efficiency and 90% recovery •Isoelectric point of Denatured Insulin is higher than Insulin-Ester Component Flowrate (kg/batch) Mass Percent (%) Conc. (g/L) Denatured Insulin 0.4359 0.03 0.30 Insulin-Ester 296.38 20.22 202.25 Water 1168.65 79.75 797.46
  • 5. Anion Exchanger Advantages  Capable of handling large volumes  Efficient, precise separation – Accurate separation of Insulin ester and denatured Insulin 1
  • 6.  Large pressure drop – Require expensive pumps  High resolution requires small beads – Small beads decrease flow rate  Each cycle requires several stages – Charging, sample input, washing, elution, cleaning Anion Exchanger Disadvantages
  • 7. Alternatives  Membrane Chromatography  Exclusion Chromatography  Affinity Chromatography 2 3 4
  • 8. Membrane Chromatography  Allows for much larger throughput (about 100 times that of ion exchange) and a higher efficiency  Uses microporous membrane  Small pressure drop compared to traditional ion exchangers  Scaling up separation is simplified
  • 9. Exclusion Chromatography  Separates on basis of Molecular Mass  Column is filled with semi- solid beads of a polymeric gel – The porosity of the gel can be changed as to exclude molecules of a set size  Useful for samples containing many types of proteins 5
  • 10. Affinity Chromatography  Matrix anchored ligand – Specifically binds to protein of interest  Can exploit protein’s unique biochemical properties instead of charge in ion exchange  Requires low flowrates 8
  • 11. Anion Exchanger Design  Ergun Equation for pressure drop in a packed bed ( ) µε ρ ⋅− ⋅    ⋅ = 1 Re A QDp 75.1 Re 150 +=Pf ( )ε ε ρ − ⋅     ⋅⋅ =∆ ⋅ 1 2 P solutionp D A QLf P
  • 12. Design Considerations Property Dimension Bead Diameter, DP 35μm Column Lenth, L 3.47m Column Diameter, D 1.3 m Pressure Drop, ΔP 1718 kPa Void Fraction, ε 0.4 Vessel Volume 4604 L All constants were taken from Perry’s Chemical Engineering Handbook 7
  • 13. Vessel Sizing  Exchanger is very large – Much larger than needed, however, this will save on pumping costs  Total flow rate through the anion exhanger is 1.721 x 10-5 m3 /s – Based on 80h batch time and 826kg/batch – Scaled up by a factor of 6
  • 16. Resins  Serves as the media for stationary phase – Polymeric matrix with immobilized charged functional groups  Quaternary Ammonium functional group  Diethylaminoethane functional group  Can be regenerated in the columns and used for many production cycles – anionic resin: 500 - 1,000 cycles 8
  • 17. Estimated Costs for Anion Exchanger Unit Cost/Unit # of Units Total Anion Exchanger $261,000 1 $261,000 Resin ~9 $/L 110 $910 Peripheral Equip. $50,000 N/A $50,000 Shipping $2,000 1 $2,000 Installation $100,000 N/A $100,000 Controls/Software $25,000 1 $25,000 Total Equip. Cost $438,910
  • 18. Estimated Operation Costs / Year Operation Total Utilities $10,000 Maintenance $5,000 Supplies $1,000 Total Operations $16,000 *Overhead costs, taxes and insurance costs have not been included in this estimate The total cost associated with the purchase of an Anion Exchanger with one year of operation is approximately $454,910.
  • 19. References [1] PowerMax, 2006 http://www.usfilter.com/ [2] Pall Corporation, 2006 (http://www.pall.com/datasheet_biopharm_36585.asp) [3] Protein Chemistry, 2006 (http://fig.cox.miami.edu/~cmallery/255/255tech/255techniques.htm) [4] Voet & Voet Biochemistry 3rd Edition, Wiley, 2004 [5] Waters Corporation, 2006 (http://www.waters.com/watersdivision/) [6] Novasep Technologies, 2006 (http://www.novasep.com/technologies/ion-exchange.asp) [7] Graver Technologies, 2006 (http://www.gravertech.com/pdfs/literature/ionex/IonExchangeResinSelection.pdf) [8] OR-Live, 2003 http://www.biopharminternational.com/

Editor's Notes

  1. Difficult for our process since insulin-ester and denatured insulin are similar in size