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M.PRASAD NAIDU
Msc Medical Biochemistry,
Ph.D Research scholar.
introduction
The process by which a mixture of similar charged
ions can be separated by using an ion exchange resin
Ion exchange resin exchanges ions according to their
relative affinities.
There is a reversible exchange or similar charged ions
Mostly similar charged ions like cations or anions can
be separated by this technique
Principle
Reversible exchange of ions b/n the ions present in
the solution and those present in the ion exchange
resin.
Cation exchange:
Separation of cations
Solid-H+
+ M+
 Solid-M+
+ H+
(solution) (solution)
The cations retained by the solid matrix of ion
exchange resin can be eluted by using buffers of diff
strength and hence separation of cations can be
effected.
Anion exchange
Separation of anions using
Anion exchange resin
Solid-OH-
+ A-
 Solid-A-
+ OH-
(solution) (solution)
The anions retained by the solid matrix of ion
exchange resin can be eluted by using buffers of diff
strength
Classification of resins
 According to the chemical nature
 1. Strong cation exchange resin 2. Weak cation exchange resin
 3. Strong anion exchange resin 4. Weak anion exchange resin
 According to the source
 Natural: cation Zeolytes, clay etc
 anion  Dolomite
 Synthetic: inorganic & organic resins
 Organic resins are the most widely used
 Org ion exchange resins are polymeric resin matrix containing exchange
sites.
 The resin is composed of polystyrene & Divinyl benzene, polystyrene
contains sites for exchangeable functional groups
 Divinyl benzene acts as a cross linking agent & offers adequate strength
i.e, mechanical stability
Functional groups present in different ion
exchange resins
Strong cation exchange resin  SO3H
Weak cation exchange resin COOH, OH, SH, PO3H2
Strong anion exchange resin  N+
R3, NR2
Weak anion exchange resin  NHR, NH2
Common ion exchange resins
Class
of resin
Nature pH
range
applications
Cation-
strong
Sulfonated
polystyrene
1-14 Fractionation of
cations, inorganic
separions, peptides,
aminoacids, B vits
Cation
weak
Carboxylic
methacrylate
5-14 Fractionation of
cations, biochemical
separations, org
bases, antibiotics
Common ion exchange resins
Class
or
resin
Nature pH
range
Applications
Anion
–
strong
Quaternary
ammonium
polystyrene
0-12 Fractionation of anions
Alkaloids, vitamins,
fattyacids
Anion-
weak
Polyamine
polystyrene or
phenol
H-CHO
0-9 Fractionation of
anionic complexes,
anions of diff valency
vitamins, aminoacids
Structural types of ion exchange
resins
1. Pellicular type with ion exchange film
2. porous resin coated with exchange beads
3. macroreticular resin bead
4. surface sulfonated and bonded electrostatically
with anion exchanger
Structural types of ion exchange
resins
1. Pellicular type with ion exchange film:
The particles have a size of 30-40µ with 1-2µ film
thickness.
These have very low exchange capacity
Ion exchange efficiency: 0.01 – 0.1 meq/g of ion
exchange resin.
2. Porous resin coated with exchanger beads: size 5-
10µ -
They are totally porous & highly efficient
Exchange capacities 0.5-2 meq/g or ion exchange
resin
Structural types of ion exchange
resins
3. macroreticular resin bead: A reticular network of the
resin is seen superficially on the resin beads
They are not highly efficient & have very low exchange
capacities
4. surface sulfonated and bonded electrostatically with
anion exchanger:
The particles are sulfonated, & they are bonded
electrostatically with anion exchanger resin.
They are less efficient & have low exchange capacity
Exchange capacity is 0.02meq/g of exchange resin.
Physical properties or resins
1. Particle size: 50-200 mesh fine powder,
should allow free flow of mobile phase, should
contain more exchangeable functional groups
2. Cross linking & swelling:
When more cross linking agent is present, they are
more rigid, but swells less
When swelling is less, separation of ions of diff sizes
is difficult as they can’t pass through the pores
present.
Physical properties or resins
When less cross linking agent is present, they are less
rigid, but swell more
Separation will not be efficient as exchange of
functional groups does not take place due to wide
pore
Hence an optimum quantity of cross linking agent
should be added to the polymeric ion exchange resin
for the separation to be effective.
Practical requirements
1. column material & dimensions:
Glass, stainless steel or polymers which are resistant
to strong acids & alkalies
Length: diameter ratio 20:1 to 100:1
Selection of ion exchange resin
Depends upon
1. type of the ions to be separated – cations or anions
2. nature of the ions to be separated- strong or weak
3. efficiency of the resin: measured by ion exchange capacity
Ion exchange capacity is the total ion exchange capacity in terms
of the exchangeable functional groups expressed as meq/g of the
ion exchange resin
m.eq/g = 1000/eq.wt
4. particle size of the resin: 50-100 mesh or 100-200
5. structural type of the resin: porous, pellicular etc
6. Amount of cross linking agent present: which decides swelling
of the resin.
Packing of the column
Wet packing
The resin is mixed with the mobile phase & packed in
the column uniformly
The sample to be separated is dissolved in the mobile
phase and introduced all at once into the column.
Mobile phase
Organic solvents are less useful & they are not used at
all.
Only diff strengths of acids, alkalies & buffers are
used as eluting solvents
Eg: 0.1N HCl, 1N NaOH, phosphate buffer acetate
buffer, borate buffer, phthalate buffer .etc.,
Development of the chromatogram & elution
1. isocratic elution technique
2. gradient elution technique
Analysis of the elute
Spectrophotometric method
Polarographic method
Conductometric method
Amperometric method
Flame photometric method
Radiochemical methods (GM counter, ionization
chamber method)
Regeneration of the ion exchange resin
The ion exchange resin after separation may not be useful for next
separation as exchangeable functional groups are lost
But due to cost of the ion exchange resins they cannot be disposed
off
Hence reactivation, regeneration
Regeneration makes the used ion exchange resin to be as efficient
as a virgin resin.
Regeneration: replacement of the exchangeable cations or anions
present in the original resin
Hence regeneration of the cation exchage resin is done by the
charging the column with strong acid like HCl
Vice versa
Factors affecting ion exchange separations
1. Nature & properties of ion exchange resins:- Cross
linking & swelling
2. Nature of exchanging ions:
A) Valency of ions: at low conc & ordinary temp ,
extent of exchange increases with increase in valency
Na+
< Ca2+
< Al3+
< Th4+
Factors affecting ion exchange separations
 B) Size of ions: for similar charged ions, exchange increases with
decrease in the size of hydrated ion.
Li < H+
< Na+
< NH4+
< K+
< Rb+
< Cs+
C) Polarizability: exchange is preferred for greater polarizable ion
Eg: I-
< Br-
< Cl-
< F-
D) conc of solution: in dilute solutions, polyvalent anions are
generally adsorbed preferentially
E) conc and charge of ions: if resin has higher +ve charge and
solution has lower +ve charge , exchange is favoured at higher
conc.
If the resin has lower +ve charge and solution has high +ve charge ,
then exchange is favoured at low conc.
applications
Softening of water
Demineralisation or deionisation of water
Purification of some solutions to be free from ionic
impurities
Separation of inorganic ions
Organic separations: mixture of pharmaceutical
compounds ca be separated
Biochemical separations like isolation of drugs or
metabolites from blood, urine etc
Conc of ionic solutions
Ionexchange appln

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Ionexchange appln

  • 1. M.PRASAD NAIDU Msc Medical Biochemistry, Ph.D Research scholar.
  • 2. introduction The process by which a mixture of similar charged ions can be separated by using an ion exchange resin Ion exchange resin exchanges ions according to their relative affinities. There is a reversible exchange or similar charged ions Mostly similar charged ions like cations or anions can be separated by this technique
  • 3. Principle Reversible exchange of ions b/n the ions present in the solution and those present in the ion exchange resin. Cation exchange: Separation of cations Solid-H+ + M+  Solid-M+ + H+ (solution) (solution) The cations retained by the solid matrix of ion exchange resin can be eluted by using buffers of diff strength and hence separation of cations can be effected.
  • 4. Anion exchange Separation of anions using Anion exchange resin Solid-OH- + A-  Solid-A- + OH- (solution) (solution) The anions retained by the solid matrix of ion exchange resin can be eluted by using buffers of diff strength
  • 5. Classification of resins  According to the chemical nature  1. Strong cation exchange resin 2. Weak cation exchange resin  3. Strong anion exchange resin 4. Weak anion exchange resin  According to the source  Natural: cation Zeolytes, clay etc  anion  Dolomite  Synthetic: inorganic & organic resins  Organic resins are the most widely used  Org ion exchange resins are polymeric resin matrix containing exchange sites.  The resin is composed of polystyrene & Divinyl benzene, polystyrene contains sites for exchangeable functional groups  Divinyl benzene acts as a cross linking agent & offers adequate strength i.e, mechanical stability
  • 6. Functional groups present in different ion exchange resins Strong cation exchange resin  SO3H Weak cation exchange resin COOH, OH, SH, PO3H2 Strong anion exchange resin  N+ R3, NR2 Weak anion exchange resin  NHR, NH2
  • 7. Common ion exchange resins Class of resin Nature pH range applications Cation- strong Sulfonated polystyrene 1-14 Fractionation of cations, inorganic separions, peptides, aminoacids, B vits Cation weak Carboxylic methacrylate 5-14 Fractionation of cations, biochemical separations, org bases, antibiotics
  • 8. Common ion exchange resins Class or resin Nature pH range Applications Anion – strong Quaternary ammonium polystyrene 0-12 Fractionation of anions Alkaloids, vitamins, fattyacids Anion- weak Polyamine polystyrene or phenol H-CHO 0-9 Fractionation of anionic complexes, anions of diff valency vitamins, aminoacids
  • 9. Structural types of ion exchange resins 1. Pellicular type with ion exchange film 2. porous resin coated with exchange beads 3. macroreticular resin bead 4. surface sulfonated and bonded electrostatically with anion exchanger
  • 10. Structural types of ion exchange resins 1. Pellicular type with ion exchange film: The particles have a size of 30-40µ with 1-2µ film thickness. These have very low exchange capacity Ion exchange efficiency: 0.01 – 0.1 meq/g of ion exchange resin. 2. Porous resin coated with exchanger beads: size 5- 10µ - They are totally porous & highly efficient Exchange capacities 0.5-2 meq/g or ion exchange resin
  • 11. Structural types of ion exchange resins 3. macroreticular resin bead: A reticular network of the resin is seen superficially on the resin beads They are not highly efficient & have very low exchange capacities 4. surface sulfonated and bonded electrostatically with anion exchanger: The particles are sulfonated, & they are bonded electrostatically with anion exchanger resin. They are less efficient & have low exchange capacity Exchange capacity is 0.02meq/g of exchange resin.
  • 12. Physical properties or resins 1. Particle size: 50-200 mesh fine powder, should allow free flow of mobile phase, should contain more exchangeable functional groups 2. Cross linking & swelling: When more cross linking agent is present, they are more rigid, but swells less When swelling is less, separation of ions of diff sizes is difficult as they can’t pass through the pores present.
  • 13. Physical properties or resins When less cross linking agent is present, they are less rigid, but swell more Separation will not be efficient as exchange of functional groups does not take place due to wide pore Hence an optimum quantity of cross linking agent should be added to the polymeric ion exchange resin for the separation to be effective.
  • 14. Practical requirements 1. column material & dimensions: Glass, stainless steel or polymers which are resistant to strong acids & alkalies Length: diameter ratio 20:1 to 100:1
  • 15. Selection of ion exchange resin Depends upon 1. type of the ions to be separated – cations or anions 2. nature of the ions to be separated- strong or weak 3. efficiency of the resin: measured by ion exchange capacity Ion exchange capacity is the total ion exchange capacity in terms of the exchangeable functional groups expressed as meq/g of the ion exchange resin m.eq/g = 1000/eq.wt 4. particle size of the resin: 50-100 mesh or 100-200 5. structural type of the resin: porous, pellicular etc 6. Amount of cross linking agent present: which decides swelling of the resin.
  • 16. Packing of the column Wet packing The resin is mixed with the mobile phase & packed in the column uniformly The sample to be separated is dissolved in the mobile phase and introduced all at once into the column.
  • 17. Mobile phase Organic solvents are less useful & they are not used at all. Only diff strengths of acids, alkalies & buffers are used as eluting solvents Eg: 0.1N HCl, 1N NaOH, phosphate buffer acetate buffer, borate buffer, phthalate buffer .etc.,
  • 18. Development of the chromatogram & elution 1. isocratic elution technique 2. gradient elution technique
  • 19. Analysis of the elute Spectrophotometric method Polarographic method Conductometric method Amperometric method Flame photometric method Radiochemical methods (GM counter, ionization chamber method)
  • 20. Regeneration of the ion exchange resin The ion exchange resin after separation may not be useful for next separation as exchangeable functional groups are lost But due to cost of the ion exchange resins they cannot be disposed off Hence reactivation, regeneration Regeneration makes the used ion exchange resin to be as efficient as a virgin resin. Regeneration: replacement of the exchangeable cations or anions present in the original resin Hence regeneration of the cation exchage resin is done by the charging the column with strong acid like HCl Vice versa
  • 21. Factors affecting ion exchange separations 1. Nature & properties of ion exchange resins:- Cross linking & swelling 2. Nature of exchanging ions: A) Valency of ions: at low conc & ordinary temp , extent of exchange increases with increase in valency Na+ < Ca2+ < Al3+ < Th4+
  • 22. Factors affecting ion exchange separations  B) Size of ions: for similar charged ions, exchange increases with decrease in the size of hydrated ion. Li < H+ < Na+ < NH4+ < K+ < Rb+ < Cs+ C) Polarizability: exchange is preferred for greater polarizable ion Eg: I- < Br- < Cl- < F- D) conc of solution: in dilute solutions, polyvalent anions are generally adsorbed preferentially E) conc and charge of ions: if resin has higher +ve charge and solution has lower +ve charge , exchange is favoured at higher conc. If the resin has lower +ve charge and solution has high +ve charge , then exchange is favoured at low conc.
  • 23. applications Softening of water Demineralisation or deionisation of water Purification of some solutions to be free from ionic impurities Separation of inorganic ions Organic separations: mixture of pharmaceutical compounds ca be separated Biochemical separations like isolation of drugs or metabolites from blood, urine etc Conc of ionic solutions