Pore size separation

Each column type has its own place of use. Column variety is what gives HPLC its versatility. It really depends on your compound and application. Approximately 80% of all separations are done on 5-10-jUm reverse phase Ci8 silica columns. Much of this is tradition. Reverse phase columns offer high-resolution separations for a wide variety of compounds and can be run in aqueous mobile phases. Ion exchange separations require salt solutions for separations, and these are not compatible with mass spectrometers. Size separations have lower resolving power and longer run times, but may be the only way to separate proteins solutions that will irreversibly stick to reverse phase columns. Use small pore size separation columns to remove salt from effluent from other chromatography separations. Zirconium and polymeric column are newer and offer possibilities for unique separations. 

Adsorptive sequestration It is possible to retain particles smaller than the filter s indicated pore size Separation of colloidal substances is possible In some case, pyrogens can be removed Highly influenced by product specific properties Separated particles can be shed by varying process conditions Saturation of the active sites cannot be determined, no warning Unspecific adsorption will result in product losses and fouling Lower reliability in terms of absolute separation... 

Size exclusion chromatography A type of chromatography in which the packing is a finely divided solid having a uniform pore size separation is based on the size of analyte molecules. 

Process Type of Membranes Average Pore Size Separation Mechanism Driving Force... 

Nghiem, L.D. Hawkes, S. (2007) Effects of membrane fouling on the nanofiltration of pharmaceutically active compounds (PhACs) mechanisms and role of membrane pore size. Separation and Purification Technology, 57 (1), 182-190. 

At the level of a single pore the strategy introduces a concept of the state of the aqueous phase in a water-filled pore. More specifically, it utilizes the fact that for capillary tubings of a polygonal cross-section there exists a threshold value of the capillary pressure (and, consequently, also of the pore size) separating two different wetting regimes (of. Joanny, 1985) for the capillary pressure weaker than the threshold value, all the pore surface... 

Particulate interferents can be separated from dissolved analytes by filtration, using a filter whose pore size retains the interferent. This separation technique is important in the analysis of many natural waters, for which the presence of suspended solids may interfere in the analysis. Filtration also can be used to isolate analytes present as solid particulates from dissolved ions in the sample matrix. For example, this is a necessary step in gravimetry, in which the analyte is isolated as a precipitate. A more detailed description of the types of available filters is found in the discussion of precipitation gravimetry and particulate gravimetry in Chapter 8. 

Two classes of micron-sized stationary phases have been encountered in this section silica particles and cross-linked polymer resin beads. Both materials are porous, with pore sizes ranging from approximately 50 to 4000 A for silica particles and from 50 to 1,000,000 A for divinylbenzene cross-linked polystyrene resins. In size-exclusion chromatography, also called molecular-exclusion or gel-permeation chromatography, separation is based on the solute s ability to enter into the pores of the column packing. Smaller solutes spend proportionally more time within the pores and, consequently, take longer to elute from the column. 

Mobil MTG and MTO Process. Methanol from any source can be converted to gasoline range hydrocarbons using the Mobil MTG process. This process takes advantage of the shape selective activity of ZSM-5 zeoHte catalyst to limit the size of hydrocarbons in the product. The pore size and cavity dimensions favor the production of C-5—C-10 hydrocarbons. The first step in the conversion is the acid-catalyzed dehydration of methanol to form dimethyl ether. The ether subsequendy is converted to light olefins, then heavier olefins, paraffins, and aromatics. In practice the ether formation and hydrocarbon formation reactions may be performed in separate stages to faciHtate heat removal. 

Deep Bed Filters. Deep bed filtration is fundamentally different from cake filtration both in principle and appHcation. The filter medium (Fig. 4) is a deep bed with pore size much greater than the particles it is meant to remove. No cake should form on the face of the medium. Particles penetrate into the medium where they separate due to gravity settling, diffusion, and inertial forces attachment to the medium is due to molecular and electrostatic forces. Sand is the most common medium and multimedia filters also use garnet and anthracite. The filtration process is cycHc, ie, when the bed is full of sohds and the pressure drop across the bed is excessive, the flow is intermpted and solids are backwashed from the bed, sometimes aided by air scouring or wash jets. 

The great quantity of very fine fibers in a meltblown web creates several unique properties such as large surface areas and small (<1 fiva) pore sizes. These have been used in creating new stmctures for hospital gowns, sterile wrap, incontinence devices, oil spill absorbers, battery separators, and special requirement filters. It is expected that much innovation will continue in the design of composite stmctures containing meltblown webs. 

The individual membrane filtration processes are defined chiefly by pore size although there is some overlap. The smallest membrane pore size is used in reverse osmosis (0.0005—0.002 microns), followed by nanofiltration (0.001—0.01 microns), ultrafHtration (0.002—0.1 microns), and microfiltration (0.1—1.0 microns). Electro dialysis uses electric current to transport ionic species across a membrane. Micro- and ultrafHtration rely on pore size for material separation, reverse osmosis on pore size and diffusion, and electro dialysis on diffusion. Separation efficiency does not reach 100% for any of these membrane processes. For example, when used to desalinate—soften water for industrial processes, the concentrated salt stream (reject) from reverse osmosis can be 20% of the total flow. These concentrated, yet stiH dilute streams, may require additional treatment or special disposal methods. 

Truly porous, synthetic ion exchangers are also available. These materials retain their porosity even after removal of the solvent and have measurable surface areas and pore size. The term macroreticular is commonly used for resins prepared from a phase separation technique, where the polymer matrix is prepared with the addition of a hq-uid that is a good solvent for the monomers, but in which the polymer is insoluble. Matrices prepared in this way usually have the appearance of a conglomerate of gel-type microspheres held together to... 

The factors to consider in the selection of cross-flow filtration include the cross-flow velocity, the driving pressure, the separation characteristics of the membrane (permeability and pore size), size of particulates relative to the membrane pore dimensions, and the hydrodynamic conditions within the flow module. Again, since particle-particle and particle-membrane interactions are key, broth conditioning (ionic strength, pH, etc.) may be necessary to optimize performance. 

We showed that these mesoporous silica materials, with variable pore sizes and susceptible surface areas for functionalization, can be utilized as good separation devices and immobilization for biomolecules, where the ones are sequestered and released depending on their size and charge, within the channels. Mesoporous silica with large-pore-size stmctures, are best suited for this purpose, since more molecules can be immobilized and the large porosity of the materials provide better access for the substrates to the immobilized molecules. The mechanism of bimolecular adsorption in the mesopore channels was suggested to be ionic interaction. On the first stage on the way of creation of chemical sensors on the basis of functionalized mesoporous silica materials for selective determination of herbicide in an environment was conducted research of sorption activity number of such materials in relation to 2,4-D. 

Separation of C oand C70 can be achieved by HPLC on a dinitroanilinopropyl (DNAP) silica (5pm pore size, 3(X)A pore diameter) column with a gradient from H-hexane to 50% CH2CI2 using a diode array detector at wavelengths 330nm (for C q) and 384nm (for C70). [J Am Chem Soc 113, 2940, 1991.]... 

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