Page 10 - Subyek Encyclopedia - Encyclopedia of Separation Science
P. 10

Sepsci*1*TSK*Venkatachala=BG
                                                                               I / AFFINITY SEPARATION  5


                                                             The beaded agaroses have captured over 85% of
                                                           the total market for biological macromolecule separ-
                                                           ations, and are regarded as the industry standard to
                                                           which all other supports are compared. They have
                                                           achieved this position by providing many of the desir-
                                                           able characteristics needed, and are also relatively
                                                           inexpensive. Beaded agaroses do have one severe lim-
                                                           itation } poor mechanical stability. For analytical
                                                           applications speed and sensitivity are essential, de-
                                                           manding mechanically strong, very small particles.
                                                           Beaded agaroses are thus of limited use analytically,
           Figure 1 Schematic diagram of affinity chromatography.
                                                           a gap Rlled by high performance liquid chromatogra-
                                                           phy (HPLC) using silica matrices. For preparative and
                                                           large scale operations other factors are more impor-
           Matrices
                                                           tant than speed and sensitivity. For example, mass
           By deRnition matrices must be inert and play no part  transfer between stationary phase and mobile phase is
           in the separation. In practice most play a (usually)  much less important when compared to the contri-
           negative role in the separation process. To minimize  bution from the chemical kinetics of the binding
           these disadvantages matrices have to be selected with  reaction between stationary phase and protein.
           great care. There is a theoretically perfect matrix,  Band spreading is also not a serious problem. When
           deRned as consisting of monodispersed perfectly  combined with the highly selective nature of the
           shaped spheres ranging from 5 to 500  m in dia-  afRnity mechanism, these factors favour the com-
           meter, of high mechanical strength, zero nonspeciRc  mon use of large sized, low mechanical strength par-
           adsorption and with a range of selectable pore sizes  ticles.
           from 10}500 nm, a very narrow pore size distribution  In recent years synthetic polymeric matrices have
           and low cost. This idealized matrix would then pro-  been marketed as alternatives. Although nonbiodeg-
           vide the most efRcient separation under all ex-  radable, physically and chemically stable, with good
           perimental conditions. As always, a compromise has  permeabilities up to molecular weights greater than
                                                             7
           to be reached, the usual approach being to accentuate  10 Da, the advantages provided are generally off-
           the most attractive characteristics while minimizing  set by other quite serious disadvantages, exempliRed
           the limitations, usually by manipulating the experi-  by high nonspeciRc adsorption. Inorganic matrices
           mental conditions most likely to provide the optimum  have also been used for large scale protein separ-
           result.                                         ations, notably reversed-phase silica for large scale
             The relative molecular masses of proteins vary  recombinant human insulin manufacture (molecular
           from the low thousands to tens of millions, making  weight approximately 6000 Da), but are generally
           pore size the most important single characteristic of  not preferred for larger molecular weight pro-
           the selected matrix. Very large molecules need very  ducts. A very slow adoption of synthetic matrices is
           open and highly porous networks to allow rapid and
           easy penetration into the core of the particle. Struc-
           tures of this type must therefore have very large pores,  Table 2 Support matrices
           but this in turn indicates low surface areas per unit
           volume, suggesting relatively low numbers of surface  Support matrix             Operational
                                                                                            pH range
           groups to which ligands can be covalently attached.
           The matrix must also be biologically and chemically  Agarose                     2}14
           inert. A special characteristic demanded from biolo-  Cellulose                  1}14
           gical macromolecular separations media is an ability  Dextran                    2}14
           to be sanitized on a routine basis without damage.  Silica                       (8
           This requires resistance to attack by cleansing re-  Glass                       (8
                                                           Polyacrylamides
                                                                                            3}10
           agents such as molar concentrations of strong alkali,  Polyhydroxymethacrylates  2}12
           acids and chaotropes. In contrast to analytical separ-  Oxirane}acrylic copolymers  0}12
           ations, where silica-based supports are inevitably  Styrene}divinylbenzene copolymers  1}13
           used, silica cannot meet these requirements and is  Polyvinyl alcohols           1}14
           generally not favoured for protein separations.  N-Acryloyl-2-amino-2-hydroxy-1, 2-propane  1}11
                                                                                            Unaffected
                                                           PTFE
           Table 2 contains examples of support matrices used
           in afRnity separations.                         PTFE, polytetrafluoroethylene.
   5   6   7   8   9   10   11   12   13   14   15