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Reaction velocity flow

The velocity of a chemical reaction is proportional to the product of the concentration of the species [Pg.425]

If we expand the expression in brackets, and consider the case of a near-equilibrium state, which may be specified by the inequality Aj RT 1, then we have a linear relationship between the reaction rate and the chemical affinity [Pg.425]

Very large affinity values may cause instability, and lead to new states that are no larger homogeneous in space. This causes a discontinuous decrease of entropy, and has important consequences in oscillating chemical reactions. Such reactions are far from equilibrium, and present undamped fluctuation on a macroscopic scale. Oscillations around a stationary state are possible as long as the total entropy production is positive. [Pg.426]

Some structures can only originate in a dissipative (nonequilibrium) medium and be maintained by a continuous supply of energy and matter. Such dissipative structures exist only within narrow limits due to the delicate balance between reaction rates and diffusion. If one of these factors is changed, then the balance is affected and the whole organized structure collapses. In a system of two simultaneous reactions, thermodynamic coupling allows one of the reactions to progress in a direction contrary to that imposed by its own affinity, provided that the total dissipation is positive. [Pg.426]


If we solve these equations together, we obtain the reaction (velocity) flow... [Pg.139]

To simulate a biological metabolic network, consider a special controlling mechanism so that the concentrations of S and P are maintained at prescribed levels. Therefore, the chemical system is at steady state since concentrations remain unchanged with time. However, the system in not at an equilibrium state and the reaction velocity (flow) is not zero ... [Pg.547]

Equation (a) is a measure of the distance of the chemical reaction from equilibrium. At equilibrium, the affinity A vanishes. Equation (b) shows a nonlinear relation between the reaction velocity (flow) and the affinity (thermodynamic force). If the chemical system is close to equilibrium, that is A/(RT) I flow—force relation between the reaction velocity and the affinity ... [Pg.571]

Assay of Enzymes In body fluids, enzyme levels aie measured to help in diagnosis and for monitoiing treatment of disease. Some enzymes or isoenzymes are predominant only in a particular tissue. When such tissues are damaged because of a disease, these enzymes or isoenzymes are Hberated and there is an increase in the level of the enzyme in the semm. Enzyme levels are deterrnined by the kinetic methods described, ie, the assays are set up so that the enzyme concentration is rate-limiting. The continuous flow analyzers, introduced in the early 1960s, solved the problem of the high workload of clinical laboratories. In this method, reaction velocity is measured rapidly the change in absorbance may be very small, but within the capabiUty of advanced kinetic analyzers. [Pg.40]

Although many industrial reactions are carried out in flow reactors, this procedure is not often used in mechanistic work. Most experiments in the liquid phase that are carried out for that purpose use a constant-volume batch reactor. Thus, we shall not consider the kinetics of reactions in flow reactors, which only complicate the algebraic treatments. Because the reaction volume in solution reactions is very nearly constant, the rate is expressed as the change in the concentration of a reactant or product per unit time. Reaction rates and derived constants are preferably expressed with the second as the unit of time, even when the working unit in the laboratory is an hour or a microsecond. Molarity (mol L-1 or mol dm"3, sometimes abbreviated M) is the preferred unit of concentration. Therefore, the reaction rate, or velocity, symbolized in this book as v, has the units mol L-1 s-1. [Pg.3]

The fluctuation of the temperature in the mixing device, reaction coil, and flow cell affects the CL reaction velocity and emission duration thus affecting the sensitivity and reproducibility. Therefore, it is preferable to keep a constant temperature [11],... [Pg.402]

Reaction rate constant Reaction order Flow velocity Volume... [Pg.319]

Deflagration Chemical reaction in which the output of heat is sufficient to enable the reaction to proceed and be accelerated without heat from another source a surface phenomenon in which reaction products flow away from the unreacted material along the surface at subsonic velocity. The result of a true deflagration under confinement is an explosion. [Pg.22]

Regardless of such diffusion effects, the flow rate may act as the limiting factor of the reaction velocity. Although this can easily be detected, it has sometimes led to serious errors. Cases of comparable flow and reaction rates have been treated by Schwab and Drikos (6). [Pg.253]

In the gas reversion process the recycle and outside C3-C4 stocks are heated separately for partial conversion before admixture with the naphtha. This bridges the difference in reaction velocity between the two types of charge and is helpful since the conversion rate of naphtha is approximately four times that of propane and twice that of butane, thereby decreasing the volume of C3-C4 recycle. Figure 10 shows a simplified flow diagram of a typical gas reversion operation. The extent to which outside C3-C4 stocks can be utilized is not limited, and the process can revert to thermal polymerization as the proportion is... [Pg.89]

A specially designed thin-film machine can be used to process very viscous, non-Newtonian materials. The apparatus can also be used to remove solvents from polymers and polycondensation processes having viscosities exceeding 10,000 poises. The Luwa thin-film machine has a small clearance between the heated wall and rotor blade. This clearance results in high shear gradients and considerably reduces apparent viscosity. The increased turbulence and improved surface renewal that ensue improve reaction velocities and aid the required forced product flow on the walls of the apparatus. [Pg.63]

In this thin-film machine, the small clearance between heated wall and rotor blade, together with the high peripheral blade velocity, results in high shear gradients, whereby the apparent viscosity in the film is considerably reduced. The resulting increased turbulence and better surface renewal improve heat transfer, increase reaction velocities, and aid the required forced product flow on the wall. On the basis of test... [Pg.77]

The parameter B2 is chosen for this project in order to gain some insight into possible consequences of varying the capability of the acetylcholinesterase to hydrolyze the neurotransmitter. Imbalances in this capability give rise to devastating diseases such as Alzheimer s and Parkinson s. The enzyme activity is included in the grouped parameter B2, which includes the maximum reaction velocity in reaction 2. The parameter B2 itself includes the enzyme activity together with three constants for the enzyme system, namely the concentration of acetylcholinesterase in compartment (II), the volume V2 of compartment (II), and the flow rate q. [Pg.249]

The chemical process gives the enthalpy of reaction, the flow rate, the reaction time, and the required reaction temperature. The first step in the sizing procedure is to calculate the required number of channels for the heat exchanger. Then the pass arrangement is selected in order to achieve the highest possible Reynolds number within an acceptable pressure drop. For example, if the total number of channels is fixed by the residence time channels in series will induce high velocities and high pressure drop channels in parallel will induce low velocities and low pressure drop. The second step is to estimate the heat transfer coefficient and to check that the heat flux can effectively be controlled by the secondary fluid (the lower heat transfer coefficient should be on the reaction side). [Pg.170]

After it is confirmed that the flow in the vessel has attained a steady state under a fixed Re, the velocity fluctuations are measured at the fixed impeller discharge flow region by using an electrode reaction velocity meter. The measured ESD is fitted by the new ESD defined by Eq. (4.7). [Pg.109]

Complicated Reactions and Flow. The ideal turbulence model must deal with multiscale effects within the subgrid model. If there is a delay as velocity cascades to the short wavelength end of the spectrum due to chemical kinetics or buoyancy, for example, the model must be capable of representing this. Otherwise bursts and intermittency phenomena cannot be calculated. [Pg.339]

Coulson, R.A. (1993). The flow theory of enzyme kinetics role of solid geometry in the control of reaction velocity in live animals. Inti. J. Biochem. 25 1445-1474. [Pg.95]

To illustrate the relation between the different flows and the two reaction velocities, we remark that the flows 23, 34, and 45 are obviously the velocity of the main reaction, r, while the flows 12 and 50 equals the velocity s of the side reaction. This is shown in Fig. 5 by means of letters and arrows. The diagram also shows the symbolic analogy between our flows and real physical flows. Thus we may speak of sources and sinks, 1 being a source and 0 a sink, and of translational and rotational flows for example, we may say that the flow s62 is a superposition of a translational flow ( — s) and a rotational flow (r). s may be assumed to be always positive. The case s = 0 is in principle the same as the one treated above (p. 322), where we may speak of catalysis with X2 as a catalyst. As the chain (23452) is broken in this case only by the reaction 21, the chain length then has its maximum, but its numerical value cannot be defined unless we know the kinetics of the reactions (12) and (21), which may be unknown compare the discussion in the literature of the hydrogen-bromine reaction (see also p. 334). [Pg.324]

Equation (3.353) proves that with the linear reaction flows, the entropy7 production is minimized at nonequihb-rium stationary state where the reaction velocities are equal to each other Jn. /r2. [Pg.149]

At equilibrium, the affinities vanish (A] = 0,A2 = 0). Therefore, Jrl - Jt3 = 0 and. /r2. Jr3 0 and the thermodynamic equilibrium does not require that all the reaction velocities vanish they all become equal. Under equilibrium conditions, then, the reaction system may circulate indefinitely without producing entropy and without violating any of the thermodynamic laws. However, according to the principle of detailed balance, the individual reaction velocities for every reaction should also vanish, as well as the independent flows (velocities). This concept is closely related to the principle of microscopic reversibility, which states that under equilibrium, any molecular process and the reverse of that process take place, on average, at the same rate. [Pg.422]

However, the hydrolysis of ATP can pump the ions only if some degrees of coupling exist between the reaction velocity and the mass flow. The efficiency of energy conversion for pumping a substrate with the help of a chemical reaction may be related to the degree of coupling by using Eq. (9.105)... [Pg.476]


See other pages where Reaction velocity flow is mentioned: [Pg.425]    [Pg.425]    [Pg.390]    [Pg.425]    [Pg.425]    [Pg.425]    [Pg.425]    [Pg.390]    [Pg.425]    [Pg.425]    [Pg.159]    [Pg.87]    [Pg.190]    [Pg.252]    [Pg.252]    [Pg.185]    [Pg.496]    [Pg.246]    [Pg.112]    [Pg.246]    [Pg.115]    [Pg.553]    [Pg.554]    [Pg.90]    [Pg.465]    [Pg.470]    [Pg.475]    [Pg.478]   


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