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The Cation Exchanger

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The supernatant carrying the insulin precursor passes through the cation ... Product continues for further purification in the diafilter ... – PowerPoint PPT presentation

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Title: The Cation Exchanger


1
The Cation Exchanger
  • CHEE 450 Design Project
  • David Grant
  • Cynthia Mukoro
  • Jenna Smith
  • Vehniah Tjong

2
Overview
  • Purpose of cation exchangers
  • Principles of ion exchange chromatography
  • Design considerations
  • Vessel sizing
  • Cost analysis
  • Alternative options

3
The Cation Exchanger
  • Purpose
  • Separates insulin precursor produced in reactor
  • What happens?
  • The supernatant carrying the insulin precursor
    passes through the cation exchanger to remove
    impurities
  • Elution of the insulin precursor then follows to
    extract the precursor from the resin
  • A wash stream is passed through the column to
    remove any residual impurities
  • Product continues for further purification in the
    diafilter

4
Principles Behind Cation Exchange Chromatography
  • How does it work?
  • Ion-exchange chromatography revolves around the
    separation of molecules (ions, polar molecules,
    etc.) on the basis of a difference in charge
  • Specifically, cation exchange chromatography is
    useful for the separation of positively charged
    species in solution
  • Two phases
  • Stationary phase consists of a resin or gel
    matrix of covalently bound negatively charged
    groups
  • Mobile phase composed of a buffered aqueous
    solution of counter-ions (positively charged
    molecules) that is in equilibrium with the total
    charge of the resin

5
Principles Behind Cation Exchange Chromatography
  • Once the insulin precursor is selectively bound
    to the negative stationary phase, it is eluted by
    an decreasing pH gradient
  • This introduces a competitive environment for
    which the insulin precursor may bind and thus
    causes its elution from the vessel.
  • Commercial examples of resins with strong binding
    properties
  • CM Sephadexcarboxymethyl group with sodium
    counter-ion
  • SP Sephadexsulphopropyl group with sodium
    counter-ion

6
Design Considerations
  • Pressure drop Ergun equation
  • Flow characteristics Reynolds number
  • Laminar Flow

where
7
Design Considerations
  • Eluant
  • pH below the pI of insulin precursor
  • Sample buffers
  • Malonic acid (pKa 2.88)
  • Citric acid (pKa 3.13)
  • Residence time

8
Vessel Sizing
9
Cost Considerations
  • Capital Costs
  • Want a small exchanger to minimize unit cost
  • Have an efficient exchanger
  • Resin Cost
  • Recycling resins costs 60 less than new ones
  • Operating Costs
  • Operation at low pressure
  • Minimize pressure drop (short unit with fast
    flow)

10
Cost Analysis
  • Resin Cost 390,000 per vessel
  • Capital cost 250,000 per vessel
  • Operating costs approx. 40,000/yr
  • Total capital cost approx. 1.4 million

11
Alternative Options
  • High Performance Liquid Chromatography
  • Consists of a reservoir containing a mobile
    phase, a pump, an injector, a separation column
    and a detector
  • Compounds separated by injecting sample mixture
    into column
  • Different components pass through column at
    different rates due to differences in their
    partitioning behavior between the mobile and
    liquid phases

12
Alternative Options
  • Gel Filtration
  • Separation is based on size
  • Stationary phase consists of porous beads with a
    well defined range of pore sizes
  • The stationary phase has a fractionation range
  • It has moderate resolution and relatively low
    capacity for loaded proteins

13
Alternative Options
  • Membrane Chromatography
  • Uses microfilters with absorption properties
  • Increased flow rates compared to normal column
    chromatography
  • Increases yield, productivity and decreases
    capital cost
  • Easy to scale up while retaining characteristics
    and performance

14
Questions
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