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Enzyme operation, parameters

Compared to synthetic catalysts, enzymes have many advantages. First of all, being natural products, they are environmentally benign and therefore their use does not meet pubhc opposition. Enzymes act at atmospheric pressure, ambient temperature, and at pH between 4 and 9, thus avoiding extreme conditions, which might result in undesired side reactions. Enzymes are extremely selective (see below). There are also, of course, some drawbacks of biocatalysts. For example, enzymes are known in only one enantiomeric form, as they consist of natural enantiomeric (homochiral) amino acids their possible modifications are difficult to achieve (see Section 5.3.2) they are prone to deactivation owing to inappropriate operation parameters and to inhibition phenomena. [Pg.95]

Cellhouse operating parameters, 26 572t Cell interconnects, SOFC, 72 226 Cell macromolecules, enzyme immunoassay for, 74 143 Cell-mediated immune response (CMI),... [Pg.155]

Information concerning the effects of system operation parameters, such as temperature and pH and their effects on the optimum activity of digester-resident hydrolytic enzyme systems, may provide for the development of strategies for increased process rates. [Pg.33]

Enzyme techniques are primarily developed for commercial reasons, and so information about immobilization and process conditions is usually limited. A commercially available immobilized penicillin V acylase is made by glutaraldehyde cross-linking of a cell homogenate. It can be used in batch stirred tank or recycled packed-bed reactors with typical operating parameters as indicated in Table 2 (38). Further development may lead to the creation of acylases and processes that can also be used for attaching side chains by enzymatic synthesis. [Pg.292]

The efficiency of the operation is conditioned by three main factors (1) active enzyme concentration, (2) mass transfer rate, and (3) operational parameters, such as plugging. Mass transfer rate depends in large part upon the linear velocity of the fluid through the bed. Hence, in order to maximize the efficiency, high L/D ratios are required, which may also reduce back mixing. However, the length of the bed is limited by the pressure that immobilized particles may withstand [116]. Flow rate, L/D ratio, pH, and temperature are some of the operational parameters that should be optimized for an efficient operation. In Shukla et al., a fixed bed reactor is used for phenol oxidation by HRP [87]. At least three cycles were needed for 80% phenol removal under the optimal L/D ratio, HRT, temperature, and substrate concentration. [Pg.263]

The enzyme, i.e. lysine decarboxylase, that is required for the conversion of lysine into cadaverine, and thus the first step of alkaloid biosynthesis, has been isolated from chloroplasts of L. polyphyllus,28 Like the majority of amino-acid decarboxylases, this enzyme is dependent on pyridoxal 5 phosphate. Its activity was found not to be affected by the presence or absence of quinolizidine alkaloids. Control of the enzyme by simple product feedback inhibition therefore seems unlikely. The operational parameters of this enzyme resemble those of the 17-oxosparteine synthase. Co-operation between the two enzymes would explain why cadaverine is almost undetectable in vivo. [Pg.7]

The design of a stirred tank fermenter for the production of an industrial enzyme at an annual rate of 800 5% mt/yr is illustrated below. Product recovery efficiency is 80% and the expected yield (product concentration) is 75kg/m. Maximum oxygen uptake demand is 185 mmol 02/L/hr. Operational parameters and media physical properties are listed as follows. [Pg.962]

While the Michaelis parameters are an important guide as to the integrity of the adsorbed sample, they are not of primary concern. By contrast, voltammetry reveals activity as a function of potential which can be varied and tuned to control and probe the enzyme in different ways. We will see that many enzymes display a "potential optimum , i.e. they have maximum activity at a particular potential. Many enzymes operate well in both redox directions, and the "bias can be measured precisely by running the voltammetry in the presence of both oxidised and reduced substrates. The exact form of the catalytic wave provides important mechanistic details, and this is often more easily analysed by taking the derivative of the catalytic current (dz/d ). [Pg.99]

Various research groups have developed enzyme electrodes for the determination of sucrose. The operational parameters of these sensors are listed in Table 10. [Pg.187]

Use of two enzymes has some disadvantages regarding the optimization of the operational parameters of these two enzymatic reactions. The second alternative is by using only AChE enzyme, and in this case... [Pg.338]

Figures 7.15-7.18 show how reactor capacity (i.e., maximum productivity, g product/g enzyme/min) is affected by operational parameters. Enzyme and substrate concentration appear to affect reactor capacity to a large extent (Figures 7.15 and 7.16) especially at lower enzyme concentrations. Effects of permeate flux and reactor volume on conversion are related to each other by means of substrate residence time in the reaction vessel. Ingreasing residence time, that is increasing reactor volume or lowering fluxes, results in higher conversions at the expense of lower capacities (Figures 7.17 and 7.18). Figures 7.15-7.18 show how reactor capacity (i.e., maximum productivity, g product/g enzyme/min) is affected by operational parameters. Enzyme and substrate concentration appear to affect reactor capacity to a large extent (Figures 7.15 and 7.16) especially at lower enzyme concentrations. Effects of permeate flux and reactor volume on conversion are related to each other by means of substrate residence time in the reaction vessel. Ingreasing residence time, that is increasing reactor volume or lowering fluxes, results in higher conversions at the expense of lower capacities (Figures 7.17 and 7.18).
In the process of biodiesel production, reaction temperature, methanol quantity, and reaction time were found to be significant operating parameters, which are closely associated with energy costs from an economic perspective [3]. Figure 6 shows the effects of reaction time on enzyme-catalyzed rapeseed oil methanolysis at the following conditions 5% (w/w) Novozym, 3 1 methanol/oil molar ratio, and 40 °C. Within lOh, the reaction proceeded very fast and in a linear fashion. Rapeseed oil was converted at a rate greater than 67.7% within 12h and achieved an equilibrium state after approximately 24h. [Pg.644]

The microenvironment within the enzyme cavity has a great influence on the reaction catalyzed by enzymes. Most of the effective parameters on enzyme operation—such as substrate preorganization, restricted substrate motion, protein dynamics, covalent binding of the transition state, and desolvation of the substrate—are induced by this microenvironment [5]. Therefore, designing a binding cavity in the structure of artificial enzymes is of great importance [2,6]. [Pg.1]

Immobilized Derivatives of Enzymes.— Numerous reviews have appeared surveying the field of enzyme immobilization. - Diffusional influences on the parametric sensitivity of immobilized enzyme catalysts have been mathematically analysed. Particular account was taken of external mass transfer and intraparticle diffusion effects which can significantly influence the dependence of the observed reaction rate on operating parameters such as temperature and pH. [Pg.568]


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