Chemical kinetics zero-order reactions

Based on these rate laws, various equations have been developed to describe kinetics of soil chemical processes. As a function of the adsorbent and adsorbate properties, the equations describe mainly first-order, second-order, or zero-order reactions. For example. Sparks and Jardine (1984) studied the kinetics of potassium adsorption on kaolinite, montmorillonite (a smectite mineral), and vermiculite (Fig. 5.3), finding that a single-order reaction describes the data for kaolinite and smectite, while two first-order reactions describe adsorption on vermiculite. 

V = V max [S]// m- A reaction of higher order is called pseudo-first-order if all but one of the reactants are high in concentration and do not change appreciably in concentration over the time course of the reaction. In such cases, these concentrations can be treated as constants. See Order of Reaction Half-Life Second-Order Reaction Zero-Order Reaction Molecularity Michaelis-Menten Equation Chemical Kinetics... 

CHEMICAL KINETICS RATE SATURATION MICHAELIS-MENTEN EQUATION ZERO-ORDER REACTIONS ORDER OF REACTION MOLECULARITY... 

The fact that a plot of H2 volumes initially generated vs. time gave a straight line is indicative of pseudo zero order kinetics. For borohydride hydrolysis, Kaufman and Sen3 and Holbrook and Twist4 also found zero order kinetics. Zero order kinetics for Reaction [1] imply that hydrolysis is independent of the concentrations of the reacting chemical species. This can be explained by assuming that the initial reaction step probably involves a surface catalyzed reaction, most likely BH" adsorption on the catalyst. Since the number... 

When an explosive slowly decomposes, the products may not follow the previously described hierarchy or be at the maximum oxidation states. The nitro, nitrate, nitramines, acids, etc., in an explosive molecule can break down slowly. This is due to low-temperature kinetics as well as the influence of light, infrared, and ultraviolet radiation, and any other mechanism that feeds energy into the molecule. Upon decomposition, products such as NO, NO2, H2O, N2, acids, aldehydes, ketones, etc., are formed. Large radicals of the parent explosive molecule are left, and these react with their neighbors. As long as the explosive is at a temperature above absolute zero, decomposition occurs. At lower temperatures the rate of decomposition is infinitesimally small. As the temperature increases, the decomposition rate increases. Although we do not always, and in fact seldom do, know the exact chemical mechanism, we do know that most explosives, in the use range of temperatures, decompose with a zero-order reaction rate. This means that the rate of decomposition is usually independent of... 

The kinetics data analysis carried out using the curve fitting method were second-order reactions for chemical oxidation and carbon adsorption processes cept in the following cases K hiO and Salicylic acid 100 mg/l (zero-order reaction) BCMnO and Salicylic acid 500 mg/l (first-order reacfion), Norit PAC 20B and Resorcinol 500 mg/l (first-order reaction), while the reaction orders determined by tune analysis method confirmed the results of the curve fitting analysis in some cases, in other cases, the reaction orders were greater than 2. 

If the mass transfer is accompanied by a chemical reaction at the catalyst surface on the reactor wall, the mass transfer depends on the reaction kinetics [55]. For a zero-order reaction, the rate is independent of the concentration and the mass flow from the bulk to the wall is constant, whereas the reactant concentration at the catalytic wall varies along the reactor length. For this situation the asymptotic Sh in circular tube reactors becomes Sh. = 4.36 [55]. The same value is obtained when reaction rates are low compared to the rate of mass transfer. If the reaction rate is high (very fast reactions), the concentration at the reactor wall can be approximated to zero within the whole reactor and the asymptotic value for Sh is = 3.66. As a consequence, the Sh in the reacting system depends on the ratio of the reaction rate to the rate of mass transfer characterized by the second Damkohler number defined in Equation 6.11. 

The first detailed investigation of the reaction kinetics was reported in 1984 (68). The reaction of bis(pentachlorophenyl) oxalate [1173-75-7] (PCPO) and hydrogen peroxide cataly2ed by sodium saUcylate in chlorobenzene produced chemiluminescence from diphenylamine (DPA) as a simple time—intensity profile from which a chemiluminescence decay rate constant could be determined. These studies demonstrated a first-order dependence for both PCPO and hydrogen peroxide and a zero-order dependence on the fluorescer in accord with an earher study (9). Furthermore, the chemiluminescence quantum efficiencies Qc) are dependent on the ease of oxidation of the fluorescer, an unstable, short-hved intermediate (r = 0.5 /is) serves as the chemical activator, and such a short-hved species "is not consistent with attempts to identify a relatively stable dioxetane as the intermediate" (68). 

Saturation kinetics are also called zero-order kinetics or Michaelis-Menten kinetics. The Michaelis-Menten equation is mainly used to characterize the interactions of enzymes and substrates, but it is also widely applied to characterize the elimination of chemical compounds from the body. The substrate concentration that produces half-maximal velocity of an enzymatic reaction, termed value or Michaelis constant, can be determined experimentally by graphing r/, as a function of substrate concentration, [S]. 

The reaction was studied for all coinage metal nanoparticles. In the case of GMEs the rate follows zero-order kinetics with IT for all the coinage metal cases. The observed IT for the Cu catalyzed reaction was maximum but its rate of reduction was found to be minimum. Just the reverse was the case for Au and an intermediate value was obtained for the Ag catalyzed reaction (Figure 7). The adsorption of substrates is driven by chemical interaction between the particle surface and the substrates. Here phe-nolate ions get adsorbed onto the particle surface when present in the aqueous medium. This caused a blue shift of the plasmon band. A strong nucleophile such as NaBH4, because of its diffusive nature and high electron injection capability, transfers electrons to the substrate via metal particles. This helps to overcome the kinetic barrier of the reaction. 

The parameter [3 is related to the contrast. If (3A> > 1, equation 1 reduces to that of a simple first order reaction (such as CEL materials are usually assumed to follow (6)). If 3A< < 1, the reaction becomes second order in A In a similar manner, the sensitized reaction varies between zero order and first order. For the anthracene loadings required by the PIE process (13,15), A is close to 1M, so (3 > > 1 is required for first order unsensitized kinetics. Although in solution, 3 for DMA is -500, and -25 for DPA (20), we have found [3 =3 for DMA/PEMA, and (3=1 for DPA/PBMA. Thus although the chemical trends are in the same direction in the polymer as in solution, the numbers are quite different, indicating a substantial... 

Referring to reactions in which the reaction velocity is independent of the reactant under consideration. For example, for the reaction A + B C, if the empirical rate expression is v = A [B], the reaction is first order with respect to B but zero order with respect to A. See Chemical Kinetics Rate Saturation Michaelis-Menten Equation... 

In Chapter 8, we addressed proton transfer reactions, which we have assumed to occur at much higher rates as compared to all other processes. So in this case we always considered equilibrium to be established instantaneously. For the reactions discussed in the following chapters, however, this assumption does not generally hold, since we are dealing with reactions that occur at much slower rates. Hence, our major focus will not be on thermodynamic, but rather on kinetic aspects of transformation reactions of organic chemicals. In Section 12.3 we will therefore discuss the mathematical framework that we need to describe zero-, first- and second-order reactions. We will also show how to solve somewhat more complicated problems such as enzyme kinetics. 

Chemical kinetics focuses on the rate of a reaction through studying the concentration profile with time. Based on the number of reactants involved in the chemical reaction, the reaction can be classified as zero, first, or second order. Third-order reactions are rare because the probability of three reactants colliding and reacting is low. The following are simplified mathematic descriptions of the chemical kinetics of the various orders. 

It is known from the theory of chemical kinetics that a system of S chemical substances in dynamic equilibrium can be described by rate constants of the pseudo-first order, K, a (i = 1, 2,..., S a= 1,2,..., Q). Some of the rates may assume zero values. The rate of depletion of substance A-t in the reaction co(er), Vrw(o), and that of its formation in the reverse reaction a, Vj+tt, must equal each other at equilibrium ... 

Reaction Order. Studies of the reaction of oxygen with carbon at temperatures of interest for AFBC s suggest that it is near zero order in oxygen (62). Most models have been based on an assumed first order reaction but they can be readily modified to accommodate the more realistic lower reaction order (63, 64). The correction for order of reaction will be most important for the prediction of the combustion of recycled fines which are in the size range in which chemical kinetics dominate and for predicting the performance of pressurized fluidized beds. 

Degradation is a chemical transformation of the drug substance and can be expressed as a chemical reaction with the specific kinetics. These reactions can have different orders, which are characterized by the different rate of parent compound decomposition. The most common are zero, first and second order reactions. It is not a subject of this chapter to discuss reaction kinetics in details however, specific preformulation-related discussions can be found in reference 6, and a general approach with examples is very well described by Martin [44]. 

Rel. (9) indicates that the kinetics of a catalytic reaction described by equation (7) does not depend on the concentration of the reacting gas (is of zero order as a function of gas concentration). For rel. (9) the evaluation of k is based on statistical thermodynamics applied to transition state theory for chemical reactions [12]. This theory shows that k has the following expression ... 

Although first-order models have been used widely to describe the kinetics of chemical reactions on natural materials, a number of other simple kinetic models, such as zero-order, second-order, Elovich, power function, and parabolic diffusion models have also been employed. The final forms of these equations are given in Table 5.1. Complete details and applications of these models can be obtained in work by Sparks (1990, 1999, 2003). 

---