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Branching Processibility, effect

A further replacement of H2 with CO sees the limit moving back to higher ambient temperature, as indicated in the figure. This inhibitory effect arises for systems with low [H2] for which the extra termination step (10) involving CO becomes able to compete with the branching process (3). Using the reactions... [Pg.527]

Keywords Branching process, Gelation, Cyclization, Excluded volume effects, Dimension, Concentration invariant, High concentration expansion, High dimension expansion, Gel point, Percolation threshold, Critical dimension. [Pg.138]

Relations between conversion and molecular parameters In nonlinear radical reactions have been developed by Macosko and Miller (18) using the recursive nature of the branching process and elementary laws of probability. One of the assumptions underlying this theory Is that of no Intramolecular reaction, l.e. no cycllzatlon. As discussed previously, this Is not valid for vlnyl-dlvlnyl co-polymerlzatlon. A revision of this recursive theory to Include the effects of cycllzatlon Is necessary. [Pg.35]

Branching type short- Type of PE Polymerization process Effects of increased... [Pg.59]

Table XII shows how polybutadiene microstructure and macrostructure, i.e., molecular weight, Mw, and Mn, polydispersity, and branching can effect the processability of a polymer [14]. A study with both cobalt- and neodenium-catalyzed polybutadiene showed the relationship between polydispersity or molecular weight distribution and increases in stress relaxation. Increases in stress relaxation, as measured by the Mooney viscometer, will infer greater... Table XII shows how polybutadiene microstructure and macrostructure, i.e., molecular weight, Mw, and Mn, polydispersity, and branching can effect the processability of a polymer [14]. A study with both cobalt- and neodenium-catalyzed polybutadiene showed the relationship between polydispersity or molecular weight distribution and increases in stress relaxation. Increases in stress relaxation, as measured by the Mooney viscometer, will infer greater...
Reproduction of the chain carriers does not occur in the propagation stage of the nonbranching chain reactions discussed above. If reproduction of chain carriers occurs in the propagation stage then a fundamentally new effect is available. In this case a newly generated chain carriers results in several chains [2,3] due to the branching process. [Pg.5]

Moreover, a branching process like also leads to an accelerating effect of oxygen. [Pg.45]

Gordon [20, 28] recognized that nonlinear polymers in the absence of intramolecular reaction can be described by a Galton-Watson branching process. Relatively complex chemical systems, presenting substitution effects, became tractable, and even some properties of polymer networks relevant to rubber elasticity theory [29] and average radius of gyration [30] as well as other polymer properties [31-33] could be computed. [Pg.68]

After the initial instants, the rate increases exponentially with time. The branching processes dominate the termination process there is an autocatalytic effect which leads eventually to an explosion. The primary cause of such an explosion is the increase in active chain carriers, and not the increase in temperature that is also present in an exothermic reaction. The rate of reaction tends to infinity, but above a certain limit the reaction develops the characteristics of the explosive reactions. [Pg.314]

If chain termination on the wall occurs rather efficiently (e 1), then near the lowest limit with respect to pressure chain termination is limited by the diffusion of active centers to the surface. In these cases, the critical condition depends on the competition of two processes effective collision of the active center with the reactant followed by chain branching and collision of the active center with the wall with chain termination. This process produces a gradient of the concentration of active centers over the reactor cross section the closer to the surface, the lower the concentration of active centers. The rigid solution to this problem can be obtained in the framework of the diffusion equation. For the cylindrical reactor, the solution of this equation results in the expression - 23Dcf, where d is the diameter of the vessel. Since in gas the diffusion coefficient is D = D the critical condition g = /takes the form... [Pg.372]


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See also in sourсe #XX -- [ Pg.29 , Pg.68 , Pg.72 , Pg.81 ]




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