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Chemical reactions predicting extent

Although thermodynamics can be used to predict the direction and extent of chemical change, it does not tell us how the reaction takes place or how fast. We have seen that some spontaneous reactions—such as the decomposition of benzene into carbon and hydrogen—do not seem to proceed at all, whereas other reactions—such as proton transfer reactions—reach equilibrium very rapidly. In this chapter, we examine the intimate details of how reactions proceed, what determines their rates, and how to control those rates. The study of the rates of chemical reactions is called chemical kinetics. When studying thermodynamics, we consider only the initial and final states of a chemical process (its origin and destination) and ignore what happens between them (the journey itself, with all its obstacles). In chemical kinetics, we are interested only in the journey—the changes that take place in the course of reactions. [Pg.649]

We have already emphasized our view that the evaluation of chemical reactions and synthetic pathways is of preeminent importance in any system for computer-assisted synthesis design or reaction prediction. The quality of the evaluation process will determine to a large extent the overall quality of such a system. [Pg.38]

Thermodynamics is a powerful tool. It states that at constant temperature and pressure, the system always moves to a state of lower Gibbs free energy. Equilibrium is achieved when the lowest Gibbs free energy of the system is attained. Given an initial state, thermodynamics can predict the direction of a chemical reaction, and the maximum extent of the reaction. Macroscopically, reactions... [Pg.3]

Such reactions often proceed slowly over hours, days, and even years, so the extent of this sorption due to organic chemical organic chemical reactions is difficult to predict. Furthermore, such bond-forming sorption is sometimes irreversible on the timescales of interest, and we might not wish to include these effects in a Ki6 expression reflecting sorption equilibrium. Nonetheless, this condensation-type sorption is very important to reducing the mobility and bioavailability of such compounds (Li et al., 2000 Weber et al., 2001). [Pg.441]

Definition of enthalpy and entropy Definition of free energy Enthalpy (a measure of the change in heat content of the reactants and products) and entropy (a measure of the change in the randomness or disorder of reactants and products) determine the direction and extent to which a chemical reaction will proceed. When combined mathematically, they can be used to define a third quantity, free energy, which predicts the direction in which a reaction will spontaneously proceed. [Pg.474]

In natural waters organisms and their abiotic environment are interrelated and interact upon each other. Such ecological systems are never in equilibrium because of the continuous input of solar energy (photosynthesis) necessary to maintain life. Free energy concepts can only describe the thermodynamically stable state and characterize the direction and extent of processes that are approaching equilibrium. Discrepancies between predicted equilibrium calculations and the available data of the real systems give valuable insight into those cases where chemical reactions are not understood sufficiently, where nonequilibrium conditions prevail, or where the analytical data are not sufficiently accurate or specific. Such discrepancies thus provide an incentive for future research and the development of more refined models. [Pg.6]

Knowing the value of the equilibrium constant for a chemical reaction lets us judge the extent of the reaction, predict the direction of the reaction, and calculate equilibrium concentrations from any initial concentrations. Let s look at each possibility. [Pg.539]

As we saw in Section 13.5, the extent of any particular reaction is described by the value of its equilibrium constant K A value of K much larger than 1 indicates that the reaction goes far toward completion, and a value of K much smaller than 1 means that the reaction does not proceed very far before reaching an equilibrium state. But what determines the value of the equilibrium constant, and can we predict its value without measuring it Put another way, what fundamental properties of nature determine the direction and extent of a particular chemical reaction For answers to these questions, we turn to thermodynamics, the area of science that deals with the interconversion of heat and other forms of energy. [Pg.722]

Thermodynamics deals with the interconversion of heat and other forms of energy and allows us to predict the direction and extent of chemical reactions and other spontaneous processes. A spontaneous process proceeds on its own without any external influence. All spontaneous reactions move toward equilibrium. [Pg.752]

Jensen Webb (Ref 43) examined the data predicting the extent of afterburning in fuel-rich exhausts of metal-modified double-base proplnt rocket motors so as to determine the amt of an individual metal which is required to suppress this afterburning. The investigatory means they used consisted of a series of computer codes. First, an equilibrium chemistry code to calculate conditions at the nozzle throat then a nonequilibrium code to derive nozzle plane exit compn, temp and velocity and, finally, a plume prediction code which incorporates fully coupled turbulent kinetic energy boundary-layer and nonequilibrium chemical reaction mechanisms. Used for all the code calcns were the theoretical environment of a static 300 N (67-lb) thrust std research motor operating at a chamber press of S.SMNm 2 (500psi), with expansion thru a conical nozzle to atm press and a mass flow rate... [Pg.899]

The objective of the following model is to investigate the extent to which Computational Fluid Mixing (CFM) models can be used as a tool in the design of industrial reactors. The commercially available program, Fluent , is used to calculate the flow pattern and the transport and reaction of chemical species in stirred tanks. The blend time predictions are compared with a literature correlation for blend time. The product distribution for a pair of competing chemical reactions is compared with experimental data from the literature. [Pg.795]

Stability constants are not always the best predictive tool for measuring the ease and the extent of chemical reactions involving complexes nor their stability with time, because their kinetic behavior can often be even more crucial. For example, when ligand exchange reactions of ML (e.g., [FeEDTA]) with other metal ions (e.g., Zn2+ or Ca2+) are ki-netically slow, they do not significantly influence ligand speciation. Another typical example of the thermodynamics vs kinetics competition is the fact that the degradability of some metal complexes (e.g., metal-NTA) is related to their kinetic lability, rather than to their thermodynamic stability constants. Kinetic rather than thermodynamic data are then used to classify metal complexes as labile, quasi-labile, slowly labile, and inert (or stable). See Section 3.2.6. [Pg.52]

Work in chemical reaction characterization and analysis enables the prediction of missing enzymes and pathways. The concept of modules of compounds, or compound scopes, defines the extent to which a particular chemical compound plays a role in the metabolic compound network. This research aids... [Pg.1819]

Acceleration of some chemical reactions is possible when high-pressure techniques are employed. The effects on a given reaction can be predicted to a certain extent because the thermodynamic properties of solutions are well known. The rate of a reaction can be expressed in terms of the activation volume,... [Pg.413]

Figure 14-9 C curves in closed vessels for various extents of back-mixing as predicted by the dispersion model. (From O. Levenspiel, Chemical Reaction Engineering, 2nd ed. Copyright 1972 John Wiley Sons, Inc. Reprinted by permission of John Wiley Sons, Inc. All rights reserved.) [Note. D = D ]... Figure 14-9 C curves in closed vessels for various extents of back-mixing as predicted by the dispersion model. (From O. Levenspiel, Chemical Reaction Engineering, 2nd ed. Copyright 1972 John Wiley Sons, Inc. Reprinted by permission of John Wiley Sons, Inc. All rights reserved.) [Note. D = D ]...
Chemical equilibrium appears to be the most helpful model concept initially to facilitate identification of key variables relevant in determining water-mineral relations and water-atmosphere relations, thereby establishing the chemical boundaries of aquatic environments. Molar Gibbs free energies (chemical potentials) describe the thermodynamically stable state and characterize the direction and extent of processes approaching equilibrium. Discrepancies between predicted equilibrium composition and the data for the actual system provide valuable insight into those cases in which important chemical reactions have not been identified, in which non-equilibrium conditions prevail, or where analytical data for the system are not sufficiently accurate or specific. Such discrepancies are incentive for research and the improvement of existing models. [Pg.3]

After chemical concentrations are converted to activities, the latter can be used to predict the probabilities and extents of specific chemical reactions based on the concept of jree energy, the energy available in a chemical system to do work. This thermodynamically based method is founded on energetic relations that can be established for a chemical species or reaction system. The fundamental energetic property of a given chemical species is its standard free energy of... [Pg.73]

During sublimation, constituents of the solid are directly transferred to the gas phase without the intervention of a liquid phase. Gilles [39] has provided six "principles of vaporization reactions", (i) All substances vaporize, but in different modes (see below) and at different rates depending upon the temperature and the environment, (ii) Vaporization processes may be represented by chemical reactions, (iii) Thermodynamic factors determine the maximum extent of vaporization, (iv) Kinetic factors determine the actual processes and the predicted extent of vaporization may not be reached, (v) The possibihty of formation of solid-solutions should be considered, as should (vi) the reactivities of all constituents (e.g. residual gases, sample containers, etc.) of the systems under examination. [Pg.40]


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