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Repression kinetics

Chloroanisole and p-nitrophenol, the nitrations of which are susceptible to positive catalysis by nitrous acid, but from which the products are not prone to the oxidation which leads to autocatalysis, were the subjects of a more detailed investigation. With high concentrations of nitric acid and low concentrations of nitrous acid in acetic acid, jp-chloroanisole underwent nitration according to a zeroth-order rate law. The rate was repressed by the addition of a small concentration of nitrous acid according to the usual law rate = AQ(n-a[HN02]atoioh) -The nitration of p-nitrophenol under comparable conditions did not accord to a simple kinetic law, but nitrous acid was shown to anticatalyse the reaction. [Pg.58]

Aromatic hydrocarbons which have methyl side chains mainly behave like toluene and form aldehydes, while combustion is stimulated and selective oxidation of the nucleus is repressed. The oxidation of methyl-naphthalene, for example, exhibits a low selectivity with respect to phtha-lic anhydride formation, combustion and maleic acid formation being the dominating reactions. Durene is a special case because it resembles o-xy-lene. The oxidation of durene over a V—W—O catalyst at 420° C is reported to produce pyromellitic dianhydride, phthalic and maleic anhydride, although combustion dominates (Geiman et al. [122]). 1,2,4-Trimethyl-benzene yields dimethylbenzene and trimellitic acid if oxidized on a Sn— V—O catalyst. Kinetic data have been measured by Balsubramanian and Viswanath [37]. [Pg.220]

Table VI presents a kinetic model for preferred growth of a microorganism on cellobiose (C2) but having an extracellular / -glucosidase (E2) that is glucose inhibited and in which the glucose uptake is repressed. This model readily fits the cellobiose data shown by the solid lines in Figure 9 (20). Table VI presents a kinetic model for preferred growth of a microorganism on cellobiose (C2) but having an extracellular / -glucosidase (E2) that is glucose inhibited and in which the glucose uptake is repressed. This model readily fits the cellobiose data shown by the solid lines in Figure 9 (20).
Enzyme assays As shown previously the LMW fraction had a repressing effect on the protein digestion in the in vivo experi-ment. Accordingly, it was of interest to study in vitro the effect of this fraction on the kinetics of reactions catalyzed by proteases and peptidases present in the gastro-intestinal tract. [Pg.407]

Cyclic Steady State is the condition whereby die state at the end of each cycle is identical to that at its beginning. For a non-isotiiermal adsorption systan this may be represented by a mathematical model, comprising material, energy and momentum balances as well as adsorption equilibrium and kinetic models, the CSS can be repressed by ... [Pg.283]

Vital-Lopez et al. (2006) used a linearized kinetic model, possibly anticipating a complex problem to be solved, as the basis for maximizing serine production. In their study, gene overexpression/repression and... [Pg.403]

In later years studies on the chemical nature of FeMoco would involve detailed collaboration between our biochemists and our chemists. Again, on the physiological side, the nifH-lac fusion mentioned in Section 4.2 was exploited to study the quantitative kinetics of oxygen repression, and another nif-lac fusion was used to show that Mo had a regulatory effect on nitrogenase synthesis. [Pg.250]

These workers have also demonstrated the validity of the kinetic equations based on experimental data. However, the mechanism by which the enzyme-forming systems in derepressed cultures are not affected by repressing metabolites could not be explained. But, there exists a scope for verification of these models with the cellulose-cellulase system forming Q and C, complexes. [Pg.70]

Enzyme production kinetics in SSF have the potential to be quite complex, with complex patterns of induction and repression resulting from the multisubstrate environment. As a result, no mechanistic model of enzyme production in SSF has yet been proposed. Ramesh et al. [120] modeled the production of a-amylase and neutral protease by Bacillus licheniformis in an SSF system. They showed that production profiles of the two enzymes could be described by the logistic equation. However, although they claimed to derive the logistic equation from first principles, the derivation was based on a questionable initial assumption about the form of the equation describing product formation kinetics They did not justify why the rate of enzyme production should be independent of biomass concentration but directly proportional to the multiple of the enzyme concentration and the substrate concentration. As a result their equation must be considered as simply empirical. [Pg.92]

In summary, HCMV blocks IFN-y-stimulated MHC class II transcription through two means with distinct mechanisms and kinetics. At relatively early times after infection, there is an HCMV-mediated repression of CIITA expression or function (Heise et al. 1998 LeRoy et al. 1999). At later times after infection, HCMV blocks IFN-y-stimulated transcription factor activation, CIITA expression, and class II transcription (Miller et al. 1998). The HCMV gene products mediating these effects remain to be identified however, experiments have shown that immediate-early and/or early gene products are involved (Heise et al. 1998 LeRoy et al. 1999 Miller et al. 1998). This represents a critical HCMV immunoevasive strategy as the virus has evolved two mechanisms, operative over distinct stages of the viral replication cycle, for blocking the IFN-y-inducible MHC class II transcription system. [Pg.157]


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See also in sourсe #XX -- [ Pg.237 , Pg.248 , Pg.389 ]




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Kinetic Model Equations for Repression

Repressible

Repression

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