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Termination models

The arrangement of monomer units in copolymer chains is determined by the monomer reactivity ratios which can be influenced by the reaction medium and various additives. The average sequence distribution to the triad level can often be measured by NMR (Section 7.3.3.2) and in special cases by other techniques.100 101 Longer sequences are usually difficult to determine experimentally, however, by assuming a model (terminal, penultimate, etc.) they can be predicted.7 102 Where sequence distributions can be accurately determined Lhey provide, in principle, a powerful method for determining monomer reactivity ratios. [Pg.354]

Models terminated to a given order, e.g., the MP2 energy is the energy of the second-order Moller-Plesset Model (or MP2). [Pg.765]

MP2 Model. A Moller-Plesset Model terminated to be second order in the energy. [Pg.765]

Fig. 16a d. Fractions of isolated Mj(a), M2(c) units in copolymer of styrene with acrylonitrile M2, and fractions of isolated pairs of these units MjM, (b) and M2M2 (d) Experimental points are compared to the plots calculated via various models terminal (- -), penultimate (----------), CR-1 (---------), CR-2 (--------) [282]... [Pg.68]

Pt (110) (fee) (2x1) Missing-row model is better than buckled-row, paired-row or saw-tooth models. Terminated-bulk positions assumed for remaining atoms. LEIS/13/... [Pg.134]

All models were fit using FOCE-I. The reference model was the reduced 2-compartment model where clearance was modeled using a power function of CrCL and IOV was included (OFV of -139.627). The LRT for each model had one degree of freedom. Legend (I) denotes that model terminated due to infinite objective function. [Pg.325]

The parallel capacitance Cp will be frequency dependent, even if Cg is not. Cp converges to zero at high frequencies. Cp is now the capacitance as seen from the outside (Cext) different from C, because we do not have direct access to Cg from the model terminals. [Pg.339]

Ratio of soUd volume concentration of solids to liquid concentration Settling velocity in the stratilred flow model Terminal velocity of the soUd particle... [Pg.226]

Strictly speaking, the Smoluchowski model is not apphcable to free-radical termination reactions. The derivation of this model comprises the assumption of an A + B reaction in which one of the reactants is present in large excess a so-called single-sink model. Termination, however, represents a multi-sink problem in which, all A and B species can react with each other. Nevertheless, the Smoluchowski equation has proved to be an accurate description for the termination kinetics of small radials [20, 31]. [Pg.40]

Brar and Sunita [58] described a method for the analysis of acrylonitrile-butyl acrylate (A/B) copolymers of different monomer compositions. Copolymer compositions were determined by elemental analyses and comonomers reactivity ratios were determined using a non-linear least squares errors-in-variables model. Terminal and penultimate reactivity ratios were calculated using the observed distribution determined from C( H)-NMR spectra. The triad sequence distribution was used to calculate diad concentrations, conditional probability parameters, number-average sequence lengths and block character of the copolymers. The observed triad sequence concentrations determined from C( H)-NMR spectra agreed well with those calculated from reactivity ratios. [Pg.177]

Model Termination Reaction - Tritylsodium was prepared as followsl Under nitrogen, a sodium dispersion (50% in xylene),... [Pg.296]

The study of the mechanisms of copolymerization reactions has attracted the attention of polymer scientists over many years. Copolymerization reactions have been described in terms of various mathematical models, terminal, penultimate, complex, etc., which are characterized by a particular set of reactivity ratios. These mathematical models can be used to make predictions about the variation of the copolymer composition or the copolymer microstructure (for example, the triad fractions, number average sequence lengths, etc.) with comonomer feed composition or monomer conversion (1). [Pg.237]

Coarse-grained molecular models Bead-spring model Generalized Maxwell model Terminal relaxation Hydrodynamic interaction Ideal rubber elasticity Packing length... [Pg.409]


See other pages where Termination models is mentioned: [Pg.235]    [Pg.252]    [Pg.253]    [Pg.316]    [Pg.169]    [Pg.56]    [Pg.236]    [Pg.709]    [Pg.369]    [Pg.48]    [Pg.412]    [Pg.172]    [Pg.68]    [Pg.239]    [Pg.255]    [Pg.160]    [Pg.214]   
See also in sourсe #XX -- [ Pg.4 ]




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Binary Copolymer Composition - Terminal Model

Binary copolymerization according to the terminal model

Chain copolymerization terminal model

Copolymerization equation terminal model

Deviations from Terminal Copolymerization Model

Diffusion-mean termination models

Geometric-mean termination models

Mayo-Lewis terminal model

Reaction diffusion terminal model

Terminal Model Monomer Reactivity Ratios

Terminal Model Revisited

Terminal Model for Rate of Radical Copolymerization

Terminal and Penultimate Models

Terminal model

Terminal model

Terminal model copolymerization

Terminal model deviations from

Terminal model for copolymerization

Terminal model of copolymerization

Terminal model reactivity ratios

Terminal model stereochemistry

Transient Network Models for Viscoelastic Properties in the Terminal Zone

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