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Polymers model

The PRDDO (partial retention of diatomic differential overlap) method is an attempt to get the optimal ratio of accuracy to CPU time. It has been parameterized for the periodic elements through Br, including the 3rd row transition metals. It was parameterized to reproduce ah initio results. PRDDO has been used primarily for inorganic compounds, organometallics, solid-state calculations, and polymer modeling. This method has seen less use than other methods of similar accuracy mostly due to the fact that it has not been incorporated into the most widely used semiempirical software. [Pg.36]

Review artieles eovering polymer modeling in general are... [Pg.316]

The voluminous experimental information about the linkage between structural variables and properties of polymers is assembled in books, notably that by van Krevelen (1990). In effect, such books encapsulate much empirical knowledge on how to formulate polymers for specific applications (Uhlherr and Theodorou 1998). What polymer modellers and simulators strive to achieve is to establish more rigorous links between structural variables and properties, to foster more rational design of polymers in future. [Pg.479]

KleD81 Klein, D. J. Rigorous results for branched polymer models with excluded volume. J. Chem. Phys. 75 (1981) 5186-5189. [Pg.142]

Fig. 27 a and b. Schematic representation of the molecular structure of a side chain polymeric liquid crystals b polymer model membranes studied by 2H NMR... [Pg.51]

Fig. 31. 2H spectra of a polymer model membrane, cf. Fig. 27b), methyl deuterated at the head group. The spectra are compared for the monomer as well as the polymer lamellar phases at the same temperatures, respectively... [Pg.54]

Calculated Molecular Weight Distributions. The calculated weight fraction distributions for the micro-mixed, segregated, and micro-mixed reactor with dead-polymer models for Runs 2, 5,... [Pg.316]

The micro-mixed reactor with dead-polymer model was developed to account for the large values of the polydispersity index observed experimentally. The effect of increasing the fraction of dead-polymer in the reactor feed while maintaining the same monomer conversion is to broaden the product polymer distribution and therefore to increase the polydispersity index. As illustrated in Table V, this model, with its adjustable parameter, can exactly match experiment average molecular weights and easily account for values of the polydispersity index significantly greater than 2. [Pg.322]

The fair degree of consistency observed in the values of <()j) for Seeds II and III and the excellent agreement between the experimental molecular weight distribution and those calculated with, lends credibility to the dead-polymer model. The... [Pg.322]

To differentiate between the micro-mixed reactor with dead-polymer and the by-pass reactor models in this investigation, the effect of mixing speed on the value of "( )" was observed. As illustrated in Table V, the value (j>" is not observed to increase with decreasing mixing speed as would be expected for a by-pass reactor. This rules out the possibility of a by-pass model and further substantiates the dead-polymer model. [Pg.322]

The micro-mixed reactor with dead-polymer model simulated the product of the laboratory reactor well within experimental accuracy. [Pg.323]

Elmoijani, K., Thievin, M., Michon, T., Popineau, Y., HaUet, J.N., and Gueguen, J., Synthetic genes specifying periodic polymers modelled on the repetitive domain of wheat gliadins Conception and expression, Biochem. Biophys. Res. Commun., 239(1), 240-246, 1997. [Pg.273]

Vorontsov-Velyaminov, P. N. Yolkov, N. A. Yurchenko, A. A., Entropic sampling of simple polymer models within Wang-Landau algorithm, J. Phys. A 2004, 37, 1573— 1588... [Pg.386]

Scola et al. [67] studied the kinetics of the MW cure of a phenylethyl-terminated imide polymer model compound and an oligomer using a variable frequency MW source and found that the activation energy of the MW cures were 68% and 51% of the thermal cure respectively. It should be noted that the reactions were performed in the liquid phase in the absence of solvent. [Pg.134]

This chapter is concerned with the application of liquid state methods to the behavior of polymers at surfaces. The focus is on computer simulation and liquid state theories for the structure of continuous-space or off-lattice models of polymers near surfaces. The first computer simulations of off-lattice models of polymers at surfaces appeared in the late 1980s, and the first theory was reported in 1991. Since then there have been many theoretical and simulation studies on a number of polymer models using a variety of techniques. This chapter does not address or discuss the considerable body of literature on the adsorption of a single chain to a surface, the scaling behavior of polymers confined to narrow spaces, or self-consistent field theories and simulations of lattice models of polymers. The interested reader is instead guided to review articles [9-11] and books [12-15] that cover these topics. [Pg.90]

A regular solution type parameter can be added to the ideal polymer model... [Pg.284]

Coarse-grained polymer models neglect the chemical detail of a specific polymer chain and include only excluded volume and topology (chain connectivity) as the properties determining universal behavior of polymers. They can be formulated for the continuum (off-lattice) as well as for a lattice. For all coarse-grained models, the repeat unit or monomer unit represents a section of a chemically realistic chain. MD techniques are employed to study dynamics with off-lattice models, whereas MC techniques are used for the lattice models and for efficient equilibration of the continuum models.36 2 A tutorial on coarse-grained modeling can be found in this book series.43... [Pg.11]

The inclusion of chain connectivity prevents polymer strands from crossing one another in the course of a computer simulation. In bead-spring polymer models, this typically means that one has to limit the maximal (or typical) extension of a spring connecting the beads that represent the monomers along the chain. This process is most often performed using the so-called finitely extensible, nonlinear elastic (FENE) type potentials44 of Eq. [17]... [Pg.11]

The two main sources for slow relaxation in polymers are entanglement effects and the glass transition. The first is entropic in origin, whereas the second—at least in chemically realistic polymer models—is primarily enthalpic. We write the largest relaxation time in the melt as... [Pg.14]


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