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Reaction controlled processes

Preventive measures provide conditions where the incident is unlikely to happen, but its occurrence cannot be totally avoided. In this category, we find measures such as inventory reduction for critical substances, the choice of a continuous rather than a batch process leading to smaller reactor volumes, and a semi-batch rather than a full batch process providing additional means of reaction control. Process automation, safety maintenance plans, etc. are also preventative measures. The aim of these measures is to avoid triggering the incident and thus reducing its consequences. In the frame of mnaway risks, a mnaway remains theoretically possible, but due to process control, its severity is limited and the probability of occurrence reduced, such that it can be controlled before it leads to a critical situation. [Pg.15]

Figure 3 Dissolution is a surface-reaction controlled process throughout late diagenesis (a) dissolution of an epidote grain from the subsurface Plio-Pleistocene sequence offshore Louisiana SEM image and (b) Ca-plagioclase, Frio Formation, Oligocene, South Texas, SEM image ((a) is reproduced by permission of SEPM (Society for Sedimentary Geology) from J. Sedim. Figure 3 Dissolution is a surface-reaction controlled process throughout late diagenesis (a) dissolution of an epidote grain from the subsurface Plio-Pleistocene sequence offshore Louisiana SEM image and (b) Ca-plagioclase, Frio Formation, Oligocene, South Texas, SEM image ((a) is reproduced by permission of SEPM (Society for Sedimentary Geology) from J. Sedim.
Another factor that affects the solute extraction is the temperature. This is significant in case of reaction-controlled processes such as thiocyanate extraction by trimethyl ammonium chloride [86]. Thiocyanate ions are rapidly transported into the membrane with increase in temperature. This is due to the strong influence of temperature on the reaction rate constants. [Pg.175]

At the highest applied temperature (841 K solid symbols in Fig. 70) the plots decrease rapidly to 20% of the initial concentration, followed by a slow decrease to zero. This evolution is typical for a chemical reaction control process. The rate velocity of such a process can be described using Eq. 19 [321]... [Pg.182]

For the exponent in Eq. 21 a variable is used to fit the data points for the aromatic and imide system in Fig. 70. At the highest temperature (solid symbols), a value of 3.0 0.1 is obtained for the exponent. This shows that this step is a chemical reaction control process. [Pg.183]

Temperature In case of a reaction controlled process, changes of reaction temperature would influence the rate of the process [34]. However, experiments with a reagent inflow rate of 0.3 mol/h and a specific energy input of 0.16 W/kg showed no distinct influence of temperature for either of the two solution types tested (see Figure 4 (c)). Based on the evidence presented above the crystal growth of HH is concluded to be a diffusion controlled linear process under the investigated conditions. A more detailed discussion can be found in a previous publication [28]. [Pg.383]

For shrinking core model and reaction-controlled process, m = 2/3. [Pg.362]

Fig. 22 Bode Plot magnitude vs frequency (EIS) showing separation of losses through resistances, / is the time constant of the physical process, Tc the time constant of the mass transport processes, Tb the time constant of the reaction controlled processes and the time constant for the ohmic processes. Fig. 22 Bode Plot magnitude vs frequency (EIS) showing separation of losses through resistances, / is the time constant of the physical process, Tc the time constant of the mass transport processes, Tb the time constant of the reaction controlled processes and the time constant for the ohmic processes.
Particle formation processes can further be subdivided into transport-and reaction-controlled processes. Typically one assumes that the synthesis in the gas phase is not controlled by any mass transfer limitations, whereas mass transfer issues are very common in liquid phase synthesis. Prior discussing mixing and reaction-controUed systems in more detail, it needs to be mentioned that perfect stabilization is assumed for the time being. Effects of coagulation would completely change the PSD. [Pg.23]

Zewail A H 1995 Femtosecond dynamics of reactions elementary processes of controlled solvation Ber. Bunsenges. Phys. Chem. 99 474-7... [Pg.2149]

Under natural conditions the rates of dissolution of most minerals are too slow to depend on mass transfer of the reactants or products in the aqueous phase. This restricts the case to one either of weathering reactions where the rate-controlling mechanism is the mass transfer of reactants and products in the soHd phase, or of reactions controlled by a surface process and the related detachment process of reactants. [Pg.214]

For a chemically controlled process, conversion depends only on the residence time and not on which phase is dispersed, whereas the interfacial area and, consequently, the rate or mass transfer will change when the relative volumes of the phases are changed. If a reaction is known to occur in a particular phase, and the conversion is... [Pg.2117]

The corrosion rate is controlled mainly hy cathodic reaction rates. Cathodic Reactions 5.2 and 5.3 are usually much slower than anodic Reaction 5.1. The slower reaction controls the corrosion rate. If water pH is depressed. Reaction 5.3 is favored, speeding attack. If oxygen concentration is high. Reaction 5.2 is aided, also increasing wastage hy a process called depolarization. Depolarization is simply hydrogen-ion removal from solution near the cathode. [Pg.98]

Inert gas pressure, temperature, and conversion were selected as these are the critical variables that disclose the nature of the basic rate controlling process. The effect of temperature gives an estimate for the energy of activation. For a catalytic process, this is expected to be about 90 to 100 kJ/mol or 20-25 kcal/mol. It is higher for higher temperature processes, so a better estimate is that of the Arrhenius number, y = E/RT which is about 20. If it is more, a homogeneous reaction can interfere. If it is significantly less, pore diffusion can interact. [Pg.110]

Suggest mechanisms for the following reactions. Classify the orbital symmetry-controlled process as clearly as you can with respect to type. [Pg.659]

The reactions of bis(trifluoromethyl)-subsatuted hetero 1,3 dienes are predomi nantly LLJMO controlled processes [238] With polar or highly polarizable dieno philes, the tendency to undergo stepwise cycloaddition reactions is considerable Notably these hetero-1,3-dienes react with a,(l unsaturated hetero multiple bond systems across the hetero multiple bond exclusively [243, 246 248] (equation 53)... [Pg.872]

Uranium-235 and U-238 behave differently in the presence of a controlled nuclear reaction. Uranium-235 is naturally fissile. A fissile element is one that splits when bombarded by a neutron during a controlled process of nuclear fission (like that which occurs in a nuclear reactor). Uranium-235 is the only naturally fissile isotope of uranium. Uranium-238 is fertile. A fertile element is one that is not itself fissile, but one that can produce a fissile element. When a U-238 atom is struck by a neutron, it likely will absorb the neutron to form U-239. Through spontaneous radioactive decay, the U-239 will turn into plutonium (Pu-239). This new isotope of plutonium is fissile, and if struck by a neutron, will likely split. [Pg.868]

A striking example of the interaction of solution velocity and concentration is given by Zembura who found that for copper in aerated 0-1 N H2SO4, the controlling process was the oxygen reduction reaction and that up to 50°C, the slow step is the activation process for that reaction. At 75 C the process is now controlled by diffiision, and increasing solution velocity has a large effect on the corrosion rate (Fig. 2.5), but little effect at temperatures below 50 C. This study shows how unwise it is to separate these various... [Pg.322]

If the PBR is less than unity, the oxide will be non-protective and oxidation will follow a linear rate law, governed by surface reaction kinetics. However, if the PBR is greater than unity, then a protective oxide scale may form and oxidation will follow a reaction rate law governed by the speed of transport of metal or environmental species through the scale. Then the degree of conversion of metal to oxide will be dependent upon the time for which the reaction is allowed to proceed. For a diffusion-controlled process, integration of Pick s First Law of Diffusion with respect to time yields the classic Tammann relationship commonly referred to as the Parabolic Rate Law ... [Pg.965]


See other pages where Reaction controlled processes is mentioned: [Pg.104]    [Pg.148]    [Pg.153]    [Pg.127]    [Pg.246]    [Pg.187]    [Pg.395]    [Pg.104]    [Pg.148]    [Pg.153]    [Pg.127]    [Pg.246]    [Pg.187]    [Pg.395]    [Pg.362]    [Pg.301]    [Pg.576]    [Pg.521]    [Pg.63]    [Pg.19]    [Pg.733]    [Pg.2268]    [Pg.2]    [Pg.277]    [Pg.235]    [Pg.2]    [Pg.870]    [Pg.360]    [Pg.178]    [Pg.307]    [Pg.431]    [Pg.974]    [Pg.1198]    [Pg.879]    [Pg.230]    [Pg.246]   
See also in sourсe #XX -- [ Pg.362 ]




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