Handbook of Size Exclusion Chromatography and Related ...

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The idea of making time-resolved measurements per se, for example, with time-dependent static light scattering (TDSLS), has been explored by a number of groups. Aggregation (1,2), gelation (3), degradation (4–6), dissolution of dry polymers (7), and phase separation have been followed with TDSLS. The notion of following polymerization reaction kinetics has been around at least since Flory’s original, manual measurements (8), and is now an active field including the use of near infrared (9–13), rheology (14–16), electron spin resonance (17,18), ultraviolet absorbance (19–21), and pulsed laser techniques (22,23). Automatic continuous online monitoring of polymerization reactions (ACOMP) was first introduced by the present author and his colleagues in 1998 (24). ACOMP allows simultaneous monitoring of weight-average molecular mass Mw, certain measures of polydispersity (25), monomer conversion, and intrinsic viscosity, and will be discussed in detail below. 1.1 Automatic Continuous Mixing (ACM) Automatic continuous mixing (ACM) differs from SEC and flow injection analysis in that it provides a continuous, diluted stream of sample to the detectors. Hence, there are no detector signal peaks, but rather a continuous record of the sample behavior. There is, however, a lag-time between the extraction/dilution and the detection. This is strictly dependent on flow rates and “plumbing,” and can range from tens to hundreds of seconds. Likewise, there is a finite response time for ACM. It is normally the integrated product of a Gaussian spreading of an extracted/ mixed volume on its way to the detector, and an exponential “mixing chamber” response time, related to any mixing chambers associated with ACM. Several configurations have been used for ACM. For ACM in equilibrium characterization, the simplest is the use of a simple syringe pump, or even a gravity feed, to dilute continuously a sample reservoir. The sample issuing from the detector lines can optionally recirculate to the sample, usually to conserve sample, or flow to waste. More refined methods can use a commercial tertiary or quaternary mixing pump, such as from ISCO (Lincoln, Nebraska, U.S.A.) or Waters (Milford, Massachusetts, U.S.A.). These were designed to provide gradients of different solvents for use in HPLC, but can also provide mixing of any desired, lowviscosity solutions for ACM (e.g., dilute polymer solutions, electrolytes, surfactants, colloids, and so on). Some mixing pumps allow the time profile of the gradient to be chosen, which can be very useful when samples respond in a logarithmic fashion to a component, for example, the reaction of polyelectrolyte conformations, interactions, and hydrodynamics to ionic strength. For situations where polymer reactions are to be monitored, the use of a programmable mixing pump is viable, as long as the solution viscosity in the reactor is not too high, that is, where solution viscosities do not exceed a few hundred centipoise (cP). Degradation and aggregation reactions are often carried © 2004 by Marcel Dekker, Inc.
out at low enough concentration that the viscosity poses no problem to a commercial mixing pump. For monitoring polymerization reactions, however, viscosities in the reactor can reach millions of cP (e.g., nylons), and even far more modest viscosities (in the many hundreds or thousands of cP) seriously compromise the performance of HPLC-grade piston pumps. Low-pressure mixing pumps (for example, an ISCO programmable mixer with an isocratic pump withdrawing from it) have proportioning valves that rely on timing for withdrawing the nominal percentage mix from two or more reservoirs. If one of the reservoirs is a reactor, and the viscosity of the reactor solution is increasing, then the preset percentage withdrawn from the reactor will decrease in time as viscosity increases. As long as at least two separate detector signals are available, so that the two unknowns, polymer concentration in the detector stream and percentage actually withdrawn from the reactor, can be solved for, accurate values for the polymer characterization will still be obtained. The lag and response times, however, increase as the percentage withdrawn from the reactor decreases, and can become unacceptably high in some cases. Another alternative is provided by high-pressure mixing. In this case two separate isocratic pumps can be used, one of which draws from the reactor, the other from the solvent reservoir. The two pumps then feed a micro-mixing chamber on the outlet side, so that high-pressure mixing occurs. In this case, the isocratic pump guarantees the selected withdrawal and flow rate at the expense of increasing pressure on the outlet side. Isocratic pumps are usually built to withstand at least 100–200bar, so that such pressures are not normally a problem, and the pump can be set to shut down if a certain pre-set limit is reached. The problem with this arrangement is that piston pumps cause cavitation of highviscosity liquids, so a point arises at which the pump will deprime, usually at moderate viscosities. Another problem that occurs with this scheme is bubbling. Many reactor liquids are bubbly, due to the exothermicity of the reactions, and bubbles entering the isocratic pump will cause it to lose prime. Hence, a variety of debubblers have been used. In these approaches it is important to be careful that no plugging of the pumps occurs, so a rapid return to pure solvent to flush polymer from pumps and detectors is required between experiments. Ultimately, high-performance ACM devices are required. These will not be based on piston or other suction-type pumps. Development based on hybrid schemes with gear and screw pumps is currently under way. 1.2 Detectors As mentioned, any number and variety of detectors can be used. A common configuration is a series containing a multi-angle light-scattering detector, a © 2004 by Marcel Dekker, Inc.
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MARCEL DEKKER Handbook of Size Excl
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CHROMATOGRAPHIC SCIENCE SERIES A Se
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60. Modern Chromatographic Analysis
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Preface to the Second Edition Gel p
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Preface to the First Edition Molecu
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Contents Preface to the Second Edit
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17. Size Exclusion Chromatography o
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James F. Curry Analytical Departmen
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Iwao Teraoka, Ph.D. Othmer Departme
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The graphical data display typicall
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polymer molecule can elute. The tot
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individual states) allowed to them.
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unsaturation while the IR detector
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Sampleconcentrationshouldbeminimize
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averagesdefinedintermsofthemolecula
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information regarding appropriate M
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Analytical. Two models, the KMX-6 a
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Figure 6 Overlay of time-sliced pea
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accurately for very large and very
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4 GENERAL REFERENCES The interested
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46. TA Chamberlin, HE Tuinstra. US
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materials are commercially availabl
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Table 1 Commercial Column Packing M
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necessarily comparable. For this re
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adjusted such that the pore size di
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narrowmolecular weight range, indiv
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Figure 8 Effect of particle size on
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Figure 9 SEC calibration using poly
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Table 4 Typical Eluent Systems for
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Figure 12 Analysis of poly-2-vinyl
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24. E Meehan, S O’Donohue. The ro
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into accepted laboratory techniques
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Table 1 Trace Metal Impurities in C
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mass and biological activity, for m
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Experimental efficiency vs. velocit
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Table 3 Properties of SEC Silica Ge
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operate at aflow rate that can easi
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Figure 3 Efficiency of amide-bonded
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mechanically stable packing materia
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Figure 5 Pore size distributions of
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Figure 6 Separation of polystyrenes
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60-120 A ˚ are large enough to be
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Table 6 Selected Silica-Based Colum
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Table 7 Separation Ranges for Polym
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the decline in permeability is perm
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sample components can be varied by
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Figure 10 Diol bonding reactions. I
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ecause of the higher relative molec
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valuesfork1,k2,anda,theunknownmolec
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water-soluble and detergent-soluble
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the importance of secondary retenti
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discussed in Table 8(33). Based on
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individual dispersion processes ins
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The detector time constant can dist
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5.3 Mobile Phase A mobile phase is
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less steep and still linear at high
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35. P Bristow, J Knox. Chromatograp
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112. K Gooding, K Lu, G Vanecek, F
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for branched polymers or copolymers
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Figure 1 “Bridge design” flow-r
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Figure 3 A light-scattering photome
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Figure 5 SEC universal calibration
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where hn is the hydrodynamic volume
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It should be noted that dn=dc also
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sensitivity for many samples compar
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that is, log[h] vs. logM,generated
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Figure 8 Effect of band broadening
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Table 1 Measurement of Molecular We
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Figure 10 Differential refractomete
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Figure 11 (A) Mark-Houwink plot of
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Table 3 Measurement of Molecular We
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size information is derived from un
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Table 5 Molecular Weight Distributi
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By measuring the scattered intensit
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8 APPENDIX: INSTRUMENT COMPANIES 8.
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53. G Marot, J Lesec. J Liq Chromat
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125. D Slootmaekers, JAPP Van Dijk,
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200. JG Bindels, GJJ Bessems, BM De
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possibly with hydrodynamic volume (
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An insurmountable limitation of SEC
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to sDR(V) when either nPS ¼nPB ¼c
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1,4-trans;and8%1,2-vynil.TheglobalC
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The goal is to find the MWD and CCD
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As expected, pS is closer to the no
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Figure 3 Example 3: MWD and BD of a
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9. BH Zimm, WH Stockmayer. The dime
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45. RO Bielsa, GR Meira. Linear cop
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solubility properties. They are use
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determination of the absolute molec
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Figure 4 Result of the PBT analysis
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Figure 8 Result of natural spider s
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7 Size Exclusion Chromatography of
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As pointed out earlier, rubber must
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Table 2 Various Solvents and Operat
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Figure 2 Typical GPC calibrations w
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© 2004 by Marcel Dekker, Inc. Figu
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Natural and Synthetic Rubbe177 vari
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Another example, shown in Fig. 5 (3
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APPENDIX: SEC CONDITIONS FOR RUBBER
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Appendix (Continued) Polymer Column
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5. J West, E Rodriguez. Rubber Chem
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associate. Girdler (67) and Speight
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Table 1 Fractions Obtained Using Co
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Figure 1 SEC analyses of an aged as
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Apparently more polar compounds are
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40% was fractionated into four frac
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Figure 7 SEC analyses of an unaged
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Figure 9 Comparison of percentage L
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Figure 11 Comparison of SEC chromat
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Figure 12 Comparisons of SEC chroma
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percentage LMS at the other locatio
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the total area into up to 12 sectio
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attempted to develop an SEC method
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parameterisbasedontheinternalpressu
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5 MODIFIED ASPHALTS The addition of
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Oxidation of the rubber and asphalt
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Figure 20 SEC chromatogram for an a
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Figure 21 Comparisons of apparent m
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© 2004 by Marcel Dekker, Inc. S/
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PS/10 4 þ 10 3 þ 500 þ 100 THF/1
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Nevertheless, SEC of asphalts is es
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56. NW Garrick, RR Biskur. Trans Re
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Asphalts 235 122. M-S Lin, JM Chaff
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Table 1 Applications of Acrylamide
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(AM/AA), and acrylamide/dimethyldia
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polymer, a large size filter of 5,
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Figure 1 Size exclusion chromatogra
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Table3 MWandMWDofaBroad-MWDPAMStand
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Another commercially available MW d
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Table 5 Weight-Average Molecular We
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Figure 6 (a) Size exclusion chromat
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compared to anormal product. By com
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StudyingtheKineticsofaChemicalReact
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this information, the higher MW pea
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46. CJ Kim, A Hamielec, A Bendek. J
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A relatively new technique utilizin
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where ais the exponent of the Mark-
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Figure 2 TDS chromatograms for full
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Figure 5 Comparison of molecular we
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Table 3 Summary of TDS Molecular We
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thepartiallyhydrolyzedPVAwiththecol
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Table 5 Summary of Conformation and
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a¼0.627andlog(K) ¼23.249.Theseare
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The limits of detection of the PVA
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Figure 12 PVAc broad molecular weig
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4 SUMMARY Advances in SEC character
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2.1 Molecular Weight Grades of PVP
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exclusion chromatography with low-a
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weightandmolecularweightdistributio
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© 2004 by Marcel Dekker, Inc. Figu
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Figure 4 PEOcalibrationofUltrahydro
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Figure 6 Overlay of GPC chromatogra
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plus Ultrahydrogel 120 A ˚ ,Shodex
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Figure 10 SEC traces of PVP/AA copo
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Figure 11 Molecular weight distribu
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2 CHEMICAL, MACROMOLECULAR AND MORP
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Table 2 The Relative Composition of
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considered to be 3. After the DS ha
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een extensively studied by methods
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The silylation was performed in LiC
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observed using column materials hav
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Table 6 (Continued) Packing materia
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4.5 Other Cellulose Derivatives Bes
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Table 8 SEC Conditions for Characte
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dextrans swell too much in cadoxen
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stirring at room temperature for an
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Figure 2 MMDofunbleached(HP)andblea
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Figure 4 MMDofbirchkraftpulpdegrade
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adequate when evaluating the influe
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differential refractive index (DRI)
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30. HA Krässig. Effects of structu
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67. E Sjöholm, K Gustafsson, A Col
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104. B Fleury, J Dubois, C Léonard
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136. D Miller, D Senior, R Sutcliff
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166. SS Cutié, CG Smith. Determina
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200. R Berggren, F Berthold, E Sjö
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13 Molar Mass and Size Distribution
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measurements, and vapor pressure os
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The calibration of SEC columns by c
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The division according to eluent ty
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Apolymer produced by UV irradiation
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Because DMAC/LiCl is also agood sol
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compoundsandwasexplainedbyadsorptio
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isolated lignins because they are e
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The Separon HEMA and Separon HEMA B
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Figure 4 GPC elution curves of the
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liquor is highest throughout the co
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topological anisotropy in the polym
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29. M Ristolainen, R Alen, J Knuuti
Page 397 and 398:
eds. Proc Int Symp 1998. Canton, Pe
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92. L Jurasek. Towards a three dime
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Table 1 Selected Industries Connect
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into C3-metabolites, which then may
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Table 4 Key Enzymes in the Biosynth
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Table 5 Cloned Mutants of Starch En
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Figure 3 Modeled x-ray diffraction
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In the native environment (plant ce
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Figure 6 (a) Large starch granules
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number of branching points); crossl
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Both absolute approaches are extrao
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Table 7 (Continued) Approach Experi
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structures, excluded volumes, and t
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Figure 10 (a) SEC elution profile o
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Figure 12 Wheat glucans: DRI elutio
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Figure 13 Wheat glucans. Normalized
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Figure 16 Wheat glucan. Normalized
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Figure 18 Wheat glucan.Elution prof
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Figure 20 Wheat glucans. Absolute m
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Figure 22 Wheat glucan. (a) Intrins
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Figure 24 Wheat PA-glucan. Elution
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an Ubbelohde-viscometer for concent
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Rheological investigations of stabi
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shifts to applied laser light, whic
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Table 8 Characteristic Parameters f
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Table 8 (Continued) and H2O. A part
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10. SG Ball, MHBJ van de Wal, RGF V
Page 451 and 452:
52. W Praznik, R Beck. J Chromatogr
Page 453 and 454:
Page 455 and 456:
3 PROTEIN PARTITIONING IN SEC 3.1 G
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Figure 1 Plot of Kav vs. log M for
Page 459 and 460:
yconsideringtheproteinsolutestobesp
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globular proteins and selected flex
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silanol groups (52-54); even capped
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most proteins to be maximally stabl
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Figure 4 Chromatograms of BSA and P
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concentrated) steps of protein puri
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Table 3 Characteristics of Dextran-
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preparative SEC. The capabilities o
Page 475 and 476:
37. GR Noll, N Nagle, JO Baker, DJ
Page 477 and 478:
Page 479 and 480:
Figure 2 Separation of total E. col
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Figure 3 Separation of HaeIII-cleav
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The recovery of DNA fragments has b
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Endotoxin should also be removed fr
Page 487 and 488:
Table 3 Best Columns for the Separa
Page 489 and 490:
Figure 10 Dependence of HETP on flo
Page 491 and 492:
Appendix (Continued ) Polymer Colum
Page 493 and 494:
REFERENCES 1. CT Wehr, SR Abbott. J
Page 495 and 496:
MALDI-MS has been applied to determ
Page 497 and 498:
Figure 1 Calibration curvesof SEC c
Page 499 and 500:
Figure 3 Chromatograms of epoxy res
Page 501 and 502:
wherenandn0 aretheRIsofthesample an
Page 503 and 504:
Figure 5 SEC chromatogram of n-alka
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Figure 7 Refractive indexes of comm
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Another detector recently applied i
Page 509 and 510:
Figure 11 Absolute MW calibration p
Page 511 and 512:
Figure 12 Chromatogram of Acrawax C
Page 513 and 514:
18 Two-Dimensional Liquid Chromatog
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largerispressuredropandresultingexp
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elations between molar masses and s
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Figure 2 (Continued) chapter, one o
Page 521 and 522:
where Nis the column efficiency exp
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composition/architecture/molar mass
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solvent. Here again, solvent-solven
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or repulsive interactions between m
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macromolecules may strongly differ
Page 531 and 532:
temperature. The efficacy of an ads
Page 533 and 534:
however, aliphatic bonded groups ma
Page 535 and 536:
Figure 10 Schematic representation
Page 537 and 538:
packing materials for SEC of synthe
Page 539 and 540:
Quantitative relations between sila
Page 541 and 542:
Both strength and thermodynamic qua
Page 543 and 544:
where Cand Dare constants for apart
Page 545 and 546:
ThisisimportantwhenLCCCisappliedtoc
Page 547 and 548:
Page 549 and 550:
Page 551 and 552: However, strong adsorption of macro
Page 553 and 554: elution step may be sufficient for
Page 555 and 556: Figure 16 Block scheme of a full ad
Page 557 and 558: processing of 2D-HPLC data. Knowled
Page 559 and 560: Figure 20 Set of full retention-elu
Page 561 and 562: distributions of complex polymers a
Page 563 and 564: constituents were not discriminated
Page 565 and 566: (Sec. 7) and therefore they can be
Page 567 and 568: 2. Identify sample solvents. First
Page 569 and 570: 1 Segmental interaction energy para
Page 571 and 572: 58. BG Belenkii. Pure Appl Chem 51:
Page 573 and 574: 19 Methods and Columns for High-Spe
Page 575 and 576: Table 1 Summary of Methods for Incr
Page 577 and 578: not savealot of time and solvent, d
Page 579 and 580: Figure 3 Conventional SEC chromatog
Page 581 and 582: chromatogram at 4mL/min, which is f
Page 583 and 584: Sincethereductionoftheinternaldiame
Page 585 and 586: Table 3 Summary of Column Performan
Page 587 and 588: Figure 11 Dependence of column perf
Page 589 and 590: . Two-dimensional chromatography ru
Page 591 and 592: The standard deviations for the mol
Page 593 and 594: Figure 15 Comparison of time requir
Page 595 and 596: Figure 17 Accuracy and precision of
Page 597 and 598: polymer analysis. Samples are “ru
Page 599 and 600: just ignoring the fractionation of
Page 601: 20 Automatic Continuous Mixing Tech
Page 605 and 606: educed viscosity, h r, to be comput
Page 607 and 608: © 2004 by Marcel Dekker, Inc. Figu
Page 609 and 610: Figure 2 Raw ACOMP signals from mul
Page 611 and 612: Figure 4 Mw vs. monomer conversion,
Page 613 and 614: decreases smoothly and monotonicall
Page 615 and 616: Figure 7 Effects of fluctuating rea
Page 617 and 618: Finally, the use of a light-scatter
Page 619 and 620: Figure 8 Linear and cubic increases
Page 621 and 622: where r(t) is now given by 2 6 r(t)
Page 623 and 624: Figure 11 Light scattering from sol
Page 625 and 626: 3.1 ASimple System: Equilibrium Cha
Page 627 and 628: Figure 13 (a) ACM applied to the ch
Page 629 and 630: Also of note in Fig. 13b is how hig
Page 631 and 632: 15. JM Starita, CL Rohn. Rheologica
Page 633 and 634: 52. M Hulden. Hydrophobically modif
Page 635 and 636: 21 Light Scattering and the Solutio
Page 637 and 638: therefore, is to remove any lingeri
Page 639 and 640: is often found in the literature wh
Page 641 and 642: Figure 2 Configuration of an SEC se
Page 643 and 644: 5 THE IMPORTANCE OF SOFTWARE Like a
Page 645 and 646: standard deviations of the measured
Page 647 and 648: These include the differential weig
Page 649 and 650: Figure 8 Data of Fig. 7corrected fo
Page 651 and 652: Figure 11 Data of Fig. 10 with spik
Page 653 and 654:
Figure 13 Fitstodatacollectedatasli
Page 655 and 656:
Table 1 Errors (in %) Characteristi
Page 657 and 658:
homogeneous copolymer, that is, tak
Page 659 and 660:
process may be used to identify the
Page 661 and 662:
fractionated sample. They represent
Page 663 and 664:
Figure 16 An example of poor SEC ch
Page 665 and 666:
on) methods, whereby the average di
Page 667 and 668:
23. WH Stockmayer, LD Moore Jr, M F
Page 669 and 670:
condition, as is explained in this
Page 671 and 672:
Figure 2 Partition coefficients KL
Page 673 and 674:
4 COLUMNS FOR HOPC Detailsaregiveni
Page 675 and 676:
and concomitant clogging of columns
Page 677 and 678:
Figure 5 Concentration dependence o
Page 679 and 680:
Table 1 Solution Volume, Polymer Ma
Page 681 and 682:
in Fig. 4a. The middle fractions (8
Page 683 and 684:
Figure 10 SEC chromatograms for som
Page 685 and 686:
appropriate for the early fractions
Page 687 and 688:
23 Size Exclusion/ Hydrodynamic Chr
Page 689 and 690:
Figure 2 Calibration curve for the
Page 691 and 692:
Figure 5 Elutionbehaviorofpolystyre
Page 693 and 694:
Table 1 Comparison Between SEC and
Page 695 and 696:
egular SEC column in which the pore
Page 697:
Such an ideal separation can be obt
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