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Liquid-solid system, transition

The simplest applications of thermodynamics to chemically significant systems involve the phase transitions that pure substances undergo. The phase of a substance is a form of matter that is uniform throughout in chemical compoation and phyacal state. The word phase comes from the Gredc word for )pearance. Thus, we speak of the solid, liquid, and gas phases of a substance, and of different solid phases distingui ed by thdr ciystal structures (such as white and black phosphorus), h phase transition, spontaneous conversion of one phase to another, occurs at a characteristic temperature for a ven pressure. Thus, at 1 atm, ice is the stable phase of water below 0 C, but above 0°C the liquid is more stable. The difference indicates that, below 0°C, the chemical potential of ice is lower than that of liquid water, //(solid) < //(liquid) (Fig. 1), and that above OX, //(liquid) < //(solid). The transition temperature is the temperature at which the chemical potentials coincide and //(solid) = //(liquid). [Pg.3]

Differential thermogravimetry (DTG), differential scanning calorimetry (DSC), and thermoporometry (monitoring liquid-solid phase transitions of a pure liquid capillary condensate in a porous system)... [Pg.270]

We can also classify the systems based on the states of the reactants and products. Monofunctional monomers such as benzyl acrylate are liquids and produce liquid polymers, and we call these Tiquid/liquid systems. Figure 1 shows a schematic of the changes in properties across a liquid/liquid front. Multifunctional monomers such as 1, 6 hexanediol diacrylate (HDDA) are liquid but produce a thermoset, solid product, and these we call liquid/solid systems. Finally, solid monomers such as acrylamide (8,25) and transition metal nitrate complexes of acrylamide (26-28) can be polymerized frontally in solid/solid systems. [Pg.108]

The appearance of two stable steady states X, X3 allows the system to exist in two phases with different densities X and X3 of the species X. It may even happen that these two phases coexist in the same system separated by a phase boundary. The whole situation is very similar to the phenomenon of phase transitions in equilibrium systems such as gas-liquid or liquid-solid systems. According to this similarity, the phenomenon of different phases in a nonequilibrium system is called a nonequilibrium phase transition or a "dissipative structure". Clearly, the inclusion of coexistence between X and X3 and of phase boundaries into our theory requires the introduction of additional diffusion terms into the equation of motion (6.5) in order to account for spatial variations of X. The analogies between our autocatalytic system (for v = 2) and equilibrium phase transitions have been worked out by F. SCHLOGL (1972) on a phenomenological and by JANSSEN (1974) on a stochastic level. [Pg.98]

In general, the reduction of the liquid film thickness to fewer than 4-6 molecular layers can induce lateral ordering and lead to freezing. It has been demonstrated that water confined to nanospaces exhibits anomalous phase behaviors that are typically illustrated experimentally or via MD simula-tion. " Moreover, there is evidence that a possible liquid-solid phase transition occurs for ionic liquids in confined systems. We also reported the first simulation results of a liquid-solid freezing transition of an 1,3-dimethylimidazolium chloride ([Dmim][Cl]) ionic liquid between two parallel graphite walls. " This result is important to understand the microstructure and freezing processes of ILs in confined systems, such as lubrication, adhesion, and IL/nanomaterial composites. [Pg.207]

The main objective of nucleation (experimental) acquaintance is the determination of the nucleation rate, which is the number of supercritical stable embryos formed in the unit volume per unit of time. Another objective is the transient time, x, (otherwise called induction, incubation or delay time or even time lag), which is associated with the system crystallization ability and which non-stationarity arises from the time-dependent distribution functions and flows. It is extremely short and hardly detectable at the phase transition from the vapor to liquid. For the liquid-solid phase transitions it may differ by many orders of magnitude, for metals as low as 10 ° but for glasses up to 10 - lO". Any nucleation theory is suffering from difficulty to define appropriately the clusters and from the lack of knowledge of their basic thermodynamic properties, namely those of interfaces. Therefore necessary approximations are introduced as follows ... [Pg.227]

Figure 8.23 (Solid + liquid) phase diagram for (. 1CCI4 +. yiCHjCN), an example of a system with large positive deviations from ideal solution behavior. The solid line represents the experimental results and the dashed line is the ideal solution prediction. Solid-phase transitions (represented by horizontal lines) are present in both CCI4 and CH3CN. The CH3CN transition occurs at a temperature lower than the eutectic temperature. It is shown as a dashed line that intersects the ideal CH3CN (solid + liquid) equilibrium line. Figure 8.23 (Solid + liquid) phase diagram for (. 1CCI4 +. yiCHjCN), an example of a system with large positive deviations from ideal solution behavior. The solid line represents the experimental results and the dashed line is the ideal solution prediction. Solid-phase transitions (represented by horizontal lines) are present in both CCI4 and CH3CN. The CH3CN transition occurs at a temperature lower than the eutectic temperature. It is shown as a dashed line that intersects the ideal CH3CN (solid + liquid) equilibrium line.
Figure 5.6 Flow pattern map for a gas/liquid flow regime in micro channels. Annular flow wavy annular flow (WA) wavy annular-dry flow (WAD) slug flow bubbly flow annular-dry flow (AD). Transition lines for nitrogen/acetonitrile flows in a triangular channel (224 pm) (solid line). Transition lines for air/water flows in triangular channels (1.097 mm) (dashed lines). Region 2 presents flow conditions in the dual-channel reactor ( ), with the acetonitrile/nitrogen system between the limits of channeling (I) and partially dried walls (III). Flow conditions in rectangular channels for a 32-channel reactor (150 pm) (T) and singlechannel reactor (500 pm) (A) [13]. Figure 5.6 Flow pattern map for a gas/liquid flow regime in micro channels. Annular flow wavy annular flow (WA) wavy annular-dry flow (WAD) slug flow bubbly flow annular-dry flow (AD). Transition lines for nitrogen/acetonitrile flows in a triangular channel (224 pm) (solid line). Transition lines for air/water flows in triangular channels (1.097 mm) (dashed lines). Region 2 presents flow conditions in the dual-channel reactor ( ), with the acetonitrile/nitrogen system between the limits of channeling (I) and partially dried walls (III). Flow conditions in rectangular channels for a 32-channel reactor (150 pm) (T) and singlechannel reactor (500 pm) (A) [13].
Beyond the notion of physical networks in which flexible strands are connected by junctions, we will use the term physical gelation in the widest possible sense for polymeric systems which undergo liquid-solid transition due to any... [Pg.201]

The liquid-solid transition for these systems seems to have the same features as for chemical gelation, namely divergence of the longest relaxation time and power law spectrum with negative exponent. [Pg.202]

Fig. 3 Liquid-liquid demixing curves (dashed lines denoted by T ) and liquid-solid transition curves (solid lines denoted by Tm) of polymer solutions with variable energy parameter sets [denoted by T(EV/EC, B/Ec)]. The solution system is made of 32-mers in a 32-sized cubic box. a Theoretical curves b simulation results in the optimized approach [14]... Fig. 3 Liquid-liquid demixing curves (dashed lines denoted by T ) and liquid-solid transition curves (solid lines denoted by Tm) of polymer solutions with variable energy parameter sets [denoted by T(EV/EC, B/Ec)]. The solution system is made of 32-mers in a 32-sized cubic box. a Theoretical curves b simulation results in the optimized approach [14]...
Transition matrix estimators have received less attention than the multicanonical and Wang-Landau methods, but have been applied to a small collection of informative examples. Smith and Bruce [111, 112] applied the transition probability approach to the determination of solid-solid phase coexistence in a square-well model of colloids. Erring ton and coworkers [113, 114] have also used the method to determine liquid-vapor and solid-liquid [115] equilibria in the Lennard-Jones system. Transition matrices have also been used to generate high-quality data for the evaluation of surface tension [114, 116] and for the estimation of order parameter weights in phase-switch simulations [117]. [Pg.380]

The heat transfer characteristics of liquid-solid fluidised systems, in which the heat capacity per unit volume of the solids is of the same order as that of the fluid are of considerable interest. The first investigation into such a system was carried out by Lemlich and Caldas193, although most of their results were obtained in the transitional region between streamline and turbulent flow and are therefore difficult to assess. Mitson194 and Smith(20) measured heat transfer coefficients for systems in which a number of different solids were fluidised by water in a 50 mm diameter brass tube, fitted with an annular heating jacket. [Pg.334]

As the him is compressed, a transition to a solid him is observed, which collapses at higher surface pressure. The II versus A isotherms, below the transition temperatures, show the liquid to solid phase transition. These solid hlms have been also called condensed films. They are observed in such systems where the molecules adhere to each other through van der Waals forces very strongly. The Tl-A isotherm shows generally no change in II at high A, while at a rather low A value, a sudden... [Pg.77]


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