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Source, continuous distribution function

Synthetic copolymers are always polydisperse, i.e. they consist of a large number of similar chemical species with different molar masses and different chemical composition. Further sources of polydispersity are differences in the number of short- and long-chain branches, tactidty, sequence length, and other characterization variables. When block copolymers are considered, additional polydispersities, for example, in block length, in the number of blocks, and in the arrangement of blocks, have to be taken into account. Owing to this polydispersity, characterization of copolymers does not usually provide the number of the individual molecules or their mole fractions, mass fractions, etc. but requires the use of continuous distribution functions or their averages. [Pg.51]

The history and fundamentals of continuous thermodynamics will be briefly presented here and has been discussed in detail elsewhere. Before the 1980 s many authors applied continuous distribution functions to specific cases of non-equilibrium thermodynamics, statistical thermodynamics, the VLE of petroleum fractions and the LLE of polydisperse polymer systems. Starting in 1980 a consistent version of chemical thermodynamics directly based on continuous distribution functions was developed and called continuous thermodynamics. The work of Kehlen and Ratzsch," " Gualtieri et al., Salacuse and Stell, Briano and Glandt," are to be mentioned as sources of information. In the following years several groups applied continuous thermodynamics to nearly all important types of polydisperse systems." Cotterman and Prausnitz reviewed the literature up until about 1990. In the 1980 s continuous modelling of phase equilibria was mostly focused on polymer systems, petroleum fractions and natural gases. In the last ten years, this has been expanded to also include problems with asphaltene precipitation from crude oils and wax precipitation from hydrocarbon mixtures. In section 9.4 the more recent papers are discussed. [Pg.285]

Using a continuum rather than cellular model implies that the growing foam is regarded as a fluid with a continuously distributed source of flow. Hence, the flow rate is also a function of position the (hydrodynamic) pressure gradient is resulted from inertia, gravity and stress mechanisms operating in the fluid. [Pg.168]

Fig. 7-5. Coagulation behavior of particles produced by nucleation. [Adapted from Walter (1973).] A continuous generation of embryos with 1.2x 10 3 pm radius is assumed. Left Variation of the distribution function with time in the absence of preexisting particles production rate q = 106 cm" s"1. Right Steady-state distributions for different concentrations of preexisting large particles (r > 0.1 pm) production rate q = 102 cm 3 s-1 number density of preexisting large particles N0 = 270/3. The dashed curve (for /3 = 1) is obtained from the steady-state distribution 12 h after terminating the source of embryos. The apparent lifetime of Aitken particles for coagulation is here greater than that indicated in Fig. 7-4 because of the smaller number density of particles. Fig. 7-5. Coagulation behavior of particles produced by nucleation. [Adapted from Walter (1973).] A continuous generation of embryos with 1.2x 10 3 pm radius is assumed. Left Variation of the distribution function with time in the absence of preexisting particles production rate q = 106 cm" s"1. Right Steady-state distributions for different concentrations of preexisting large particles (r > 0.1 pm) production rate q = 102 cm 3 s-1 number density of preexisting large particles N0 = 270/3. The dashed curve (for /3 = 1) is obtained from the steady-state distribution 12 h after terminating the source of embryos. The apparent lifetime of Aitken particles for coagulation is here greater than that indicated in Fig. 7-4 because of the smaller number density of particles.
C We want to explore the dynamics of aerosol size distributions undergoing simultaneous growth by condensation and removal at a rate dependent on the aerosol concentration, with a continuous source of new particles. The size distribution function in such a case is governed by... [Pg.625]

In H2S decomposition, A represents the sulfur clusters, which diffuse and drift in the centrifugal field. Consider the cluster size n as a continuous coordinate (varying from 1 to 00). Another coordinate is the radial one, x, varying from 0 to the radius of the discharge tube, R. Clusterization in the centrifugal field can be considered an evolution of the distribution function f n, x, t) in the space n, x) of cluster sizes. Dissociation of H2S takes into account a source A (sulfur atoms) that is located at the point x = 0. Thus, evolution of the cluster distribution function can be described by the continuity equation in the space (n, x) of cluster sizes (Macheret, Rusanov, Fridman, 1985) ... [Pg.746]

After a decade of development and application, a number of original papers on continuous thermodynamics have appeared in the literature. Rtosch and Kehlen [28 30] reviewed the state-of-the-art on systems containing synthetic polymers [28, 29] and those containing petrol fractions and other multicomponent low molecular hydrocarbon systems [30]. Therefore, this overview focuses on systems containing copolymers characterized by multivariate distribution functions and those containing block copolymers. Of source, all important aspects regarding homopolymer systems are automatically included in our discussion. [Pg.52]

These source term expressions contain the continuous particle number density function, /(, r, t). However, in order to close the equation the source terms must be expressed entirely in terms of the dependent variable j(r, f). The fixed pivot technique is based on the idea of birth modification. The pivot concentrates the particles in the interval at a single representative point. The number density distribution function/i(, r, t) can be approximated as ... [Pg.1207]


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