Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Reactants convert

For kinetic investigations and for activity measurements, either photometric assays or - because of the higher complexity of the reactants converted by biocatalysts - HPEC methods can often be used. Here the ionic liquid itself or impurities may interfere with the analytical method. [Pg.338]

STRATEGY The nuclear binding energy is the energy released in the formation of the nucleus from its nucleons. Use H atoms instead of protons to account for the masses of the electrons in the He atom produced. Write the nuclear equation for the formation of the nuclide from hydrogen atoms and neutrons, and calculate the difference in masses between the products and the reactants convert the result from a multiple... [Pg.835]

Surface area is one of the most important factors in determining throughput (amount of reactant converted per unit time per unit mass of catalyst). Many modem inorganic supports have surface areas of 100 to >1000 m g The vast majority of this area is due to the presence of internal pores these pores may be of very narrow size distribution to allow specific molecular sized species to enter or leave, or of a much broader size distribution. Materials with an average pore size of less than 1.5-2 nm are termed microporous whilst those with pore sizes above this are called mesoporous materials. Materials with very large pore sizes (>50 nm) are said to be macroporous, (see Box 4.1 for methods of determining surface area and pore size). [Pg.88]

The term reactor performance usually refers to the operating results achieved by a reactor, particularly with respect to fraction of reactant converted or product distribution... [Pg.16]

Selectivity the ratio of the amount of a desired product obtained to the amount of a key reactant converted. [Pg.232]

TOF turnover frequency (moles of reactant converted per mole of active catalyst species per unit time)... [Pg.26]

Finally, the molar enthalpy of the reaction can be calculated as described, dividing A0bsH by the amount of substance of the limiting reactant converted to products (n see equation 10.6). Alternatively, the value of the quantum yield and equation 10.13 can be used (Q = AriC s and Q = Ap e). [Pg.153]

At the start of the reaction, the overall rate of change concentration of the reactant is linear with time. As the reaction proceeds and the product accumulates the reverse reaction becomes significant, such that the measured change in reagent concentration also decreases and the rate of the reaction is said to decrease. This decrease in rate is exponential, with the system eventually reaching equilibrium, where the amount of reactant converted to product equals the amount of product converted to reactant in a given time. [Pg.44]

When conversions are not small, the change in concentration of reactant and product over the length of the catalyst bed must be taken into account. It is therefore convenient to substitute for the concentrations in Eqs. (57) and (58) so that [B] Pb(1 fn /q) [N] - Pb/n [Q] Pb/q Also, in a flow system the number of moles of reactant converted in an element of catalyst bed is equal to the reaction rate per gram times the mass of the catalyst in that element of the bed. That is. [Pg.115]

Normally, catalytic activity is expressed as the reaction rate per unit area of active surface (expressed as metre per gram) under given conditions. In a chemical reaction, catalytic conversion is defined as the fraction of reactants converted to products and selectivity is a function of the rate of formation of a desired product with respect to the overall conversion of the initial reactants. The reactant molecules transfer to the catalyst surface where adsorption may occur on an active site , with possible rearrangement of their bonds leading to a chemical adsorption (chemisorption), gas-catalyst reaction and the subsequent desorption of new species. The active site or phase is of high activity and selectivity for the desired products. Thus, the nature of the active sites is important. In many cases, it is not enough to have just activity. Selectivity to desired products is important and often modifiers or promoters are needed both to improve the... [Pg.3]

A reaction that has produced as much product as it ever will is said to be at equilibrium. Equilibrium doesn t mean that no more chemistry is occurring rather, equilibrium means that the rate at which reactant converts to product equals the rate at which product converts back into reactant. (Yes, reactions go both forward and backward at all times.) So the overall concentrations of reactants and products no longer change. [Pg.202]

Reference Reactants Products Conditions Radiation Pounds reactants converted/ hr./kw. [Pg.387]

It often is important to know the yield of a chemical reaction—that is, the percentage of reactants converted to products. The following example shows how this yield may be calculated, and how conditions may be altered to increase the yield. [Pg.257]

Yield, Quantum Yield and Rate Constant of Photochemical Reactions. The overall efficiency of a thermal reaction is given by its yield , that is the fraction of reactants convertible into products this is usually expressed in %. [Pg.92]

From the masses tabulated in the Appendices, calculate the energy release for this reaction and the percentage of the initial mass of the reactants converted to energy. [Pg.54]

If there are two or more reactants involved in the reaction, both can be converted completely in a single pass only if they are fed to the reactor in the stoichiometric proportion. In many cases, the stoichiometric ratio of reactants may be the best, but in some instances, where one reactant (especially water or air) is very much cheaper than the other, it may be economically advantageous to use it in excess. For a given size of reactor, the object is to increase the conversion of the more costly reactant, possibly at the expense of a substantial decrease in the fraction of the cheaper reactant converted. Examination of the kinetics of the reaction is required to determine whether this can be achieved, and to calculate quantitatively the effects of varying the reactant ratio. Another and perhaps more common reason for departing from the stoichiometric proportions of reactants is to minimise the amount of byproducts formed. This question is discussed further in Section 1.10.4. [Pg.15]

Calculation of the time required to reach a particular conversion is the main objective in the design of batch reactors. Knowing the amount of reactant converted, i.e. the amount of the desired product formed per unit volume in this reaction time, the volume of reactor required for a given production rate can be found by simple scale-up as shown in the example on ethyl acetate below. [Pg.27]

If the reaction mixture is a fluid whose density remains constant throughout the reaction, equation 1.35 may be written in terms of x moles of reactant converted per unit volume of fluid. Since x- °aCa0, equation 1.35 becomes ... [Pg.36]

The thermal potential is at its maximum at the beginning of the reaction, when conversion has not yet occurred and it decreases as the reactants convert. Thus, the MTSR is given by... [Pg.127]

In heterogeneous catalysis, the term active site is also used extensively [7,8], The density of active sites per unit surface area of the catalyst is an important parameter in catalyst analysis and development [9], However, whereas the surface area is relatively easily determined experimentally [10], the number of active sites in heterogeneous catalysts is not easily estimated. Therefore, although both fields use turnover numbers (reactant converted per unit time per active site) to describe activity, only the enzymologists can be sure that the quantitation of this parameter is adequate. [Pg.24]

The Houk group recently compared several artificial catalytic Diels-Alderase systems, including the ribozymes described here [11]. This study came to the conclusion that in none of these artificial systems there is a significant specific stabilization of the transition state. Acceleration arises predominantly from binding of the reactants, converting a second-order reaction of diene with dienophile into a first-order reaction of the termolecular complex of host, diene, and dienophile. The simultaneous presence of the two components of an intermolecular Diels-Alder reaction within the confined space of a cavity is the driving force that facilitates the reaction. [Pg.433]

The fractional conversion XA for a given reactant A is defined as the fraction of the reactant converted into product or... [Pg.119]

Linder typical conditions the reaction of acetone with hydrogen cyanide (K = 32) has most of the reactants converted to the product at equilibrium. This allows the cyanohydrin to be obtained in acceptable isolated yield (78%). In contrast, the amount of cyanohydrin product that is present at equilibrium in the reaction of acetophenone (K = 0.77) is too low for the reaction to be synthetically useful unless some method is used to drive the equilibrium toward the product. [Pg.749]

In many processes multiple reaction pathways are possible and it is the role of the catalyst and reaction conditions to maximize the rate along the desired path. Selectivity is defined as the amount of desired product divided by reactant converted. A practical example of the catalyst directing reactants to a selective product is shown by the oxidation of ammonia to nitric oxide, which is used in the production of fertilizers. [Pg.278]

Selectivity is another catalyst attribute that is often considered when ranking catalysts. Selectivity may be defined as the ratio of the molar amount of key reactant converted to the desired product to the total molar amount of the key reactant converted. As such, selectivity is a measure of the efficiency of the catalyst in promoting the formation of the desired product as compared to other products. Since selectivity is a function of the relative rates of reaction with a given reaction system, selectivity will be a function of reaction temperature, space velocity, feed composition, reactor geometry, and degree of conversion. Comparing selec-tivities of different catalysts is therefore only meaningful when all the latter parameters are constant. [Pg.117]

Selectivity is sometimes called efficiency. As a result, selectivity can be confused with product yield. Yield is usually best defined as the ratio of molar amount of key reactant converted to the desired product to the total molar amount of the key reactant fed into the reactor system. Consequently, it follows that... [Pg.117]


See other pages where Reactants convert is mentioned: [Pg.79]    [Pg.324]    [Pg.84]    [Pg.84]    [Pg.85]    [Pg.72]    [Pg.168]    [Pg.101]    [Pg.148]    [Pg.688]    [Pg.388]    [Pg.10]    [Pg.297]    [Pg.298]    [Pg.51]    [Pg.4]    [Pg.278]    [Pg.566]    [Pg.285]    [Pg.72]    [Pg.101]   
See also in sourсe #XX -- [ Pg.131 ]




SEARCH



Converting Reactants to Products

© 2024 chempedia.info