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Low reaction

The ester and catalj st are usually employed in equimoleciilar amounts. With R =CjHs (phenyl propionate), the products are o- and p-propiophenol with R = CH3 (phenyl acetate), o- and p-hydroxyacetophenone are formed. The nature of the product is influenced by the structure of the ester, by the temperature, the solvent and the amount of aluminium chloride used generally, low reaction temperatures favour the formation of p-hydroxy ketones. It is usually possible to separate the two hydroxy ketones by fractional distillation under diminished pressure through an efficient fractionating column or by steam distillation the ortho compounds, being chelated, are more volatile in steam It may be mentioned that Clemmensen reduction (compare Section IV,6) of the hj droxy ketones affords an excellent route to the substituted phenols. [Pg.664]

The simplest of all Diels-Alder reactions cycloaddition of ethylene to 1 3 butadi ene does not proceed readily It has a high activation energy and a low reaction rate Substituents such as C=0 or C=N however when directly attached to the double bond of the dienophile increase its reactivity and compounds of this type give high yields of Diels-Alder adducts at modest temperatures... [Pg.409]

Wnte a structural formula for the principal organic product or products of each of the fol lowing reactions... [Pg.878]

Isomerization. Stmctural isomerization of / -butane to isobutane is commercially useful when additional isobutane feedstock is needed for alkylation (qv). The catalysts permit low reaction temperatures which favor high proportions of isobutane in the product. The Butamer process also is well known for isomerization of / -butane. [Pg.402]

Phtha/k anhydride is the most important type of dibasic acid derivative ki alkyd preparation because of its low cost and the excellent overall properties it imparts to the reski. The anhydride stmcture allows a fast esterification to form half-esters at relatively low reaction temperatures without hberatkig water, thereby avoiding the danger of excessive foaming ki the reactor. However, skice the two carboxyl groups of phthaUc anhydride are ki the ortho position to each other on the benzene ring, cycHc stmctures may and do occur ki the reski molecules. [Pg.32]

Details for the nonsolvent batch oleum sulfonation process for the production of BAB sulfonic acid have been described, including an exceUent critique of processing variables (257). Relatively low reaction temperatures (ca 25—30°C) are necessary in order to obtain acceptable colored sulfonate, which requires refrigerated cooling (Table 9, example D). [Pg.85]

Plug FI low Reactions The differential relations in a cyhndrical vessel are... [Pg.702]

To minimize racemization, the use of nonpolar solvents, a minimum of base, low reaction temperatures, and carbamate protective groups (R = O-alkyl or O-aryl) is effective. (A carbamate, R = O-r-Bu, has been reported to form an oxazolone that appears not to racemize during base-catalyzed coupling.) ... [Pg.316]

To minimize racemization, the use of nonpolar solvents, a minimum of base, low-reaction temperatures, and carbamate protective groups (R = O-alkyl or O-aryl) are effective. [Pg.503]

Low reaction rate for poorly water-miscible substrate... [Pg.260]

The N-aminoaziridine version7 of the a,/3-epoxyketone->alkynone fragmentation is a possible alternative in situations where the simple tosylhydrazone version6-9 fails. The tosylhydrazone method often gives good yields at low reaction temperatures, but it tends to be unsuccessful with the epoxides of enones that are not cyclic or are not fully substituted at the /5-carbon atom. For example, it has been reported9 that 2,3-epoxycyclohexanone docs not produce 5-hexynal by the tosylhydrazone route. The A-aminoaziridine method can also be recommended for the preparation of acetylenic aldehydes as well as ketones. [Pg.55]

Low reaction T are preferred and THF-CH2CI2 solvent mixtures are used. [Pg.47]

For Ef < Ef, increasing the temperature shifts the equilibrium in the wrong direction, but the forward reaction rate still increases with increasing temperature. There is an optimum temperature for this case. A very low reaction temperature gives a low yield of B because the forward rate is low. A very high reaction temperature also gives a low yield of B because the equilibrium is shifted toward the left. [Pg.155]

Power law expressions are useful as long as the approximate orders of reactant concentration are constant over a particular concentration course. A change in the order of the reaction corresponds to a change in the surface concentration of a particular reactant. A low reaction order usually implies a high surface concentration, a low reaction order, and a low surface reaction of the corresponding adsorbed intermediates. In order to deduce (Eq. (1.17b)) the rate of surface carbon hydrogenation, the power law of Eq. (1.18) has been used. [Pg.14]

Ammonia activation by Pt, to be discussed in the next section, is an interesting example, because it illustrates the basic principle that provides chemical direction to the identification of surface topologies that give low reaction barriers in surface reactions. This holds specifically for elementary reactions that require a surface ensemble of atoms. [Pg.25]

A 5% CoOj/Ti02 catalyst is quite active for the wet TCE oxidation at very low reaction temperatures, such as 310 K, and our proposed model of different forms of CoO species existing with the fresh catalyst can reasonably explain the unsteady-state catalytic behavior at the initial period during the wet catalysis. [Pg.308]

The catalytic activity of ln/H-ZSM-5 for the selective reduction of nitric oxide (NO) with methane was improved by the addition of Pt and Ir which catalyzed NO oxidation, even in the presence of water vapor. It was also found that the precious metal, particularly Ir loaded in/H-ZSM-5 gave a low reaction order with respect to NO, and then showed a high catalytic activity for the reduction of NO at low concentrations, if compared with ln/H-ZSM-5. The latter effect of the precious metal is attributed to the enhancement of the chemisorption of NO and also to the increase in the amount of NO2 adsorbed on in sites. [Pg.671]


See other pages where Low reaction is mentioned: [Pg.29]    [Pg.418]    [Pg.33]    [Pg.54]    [Pg.33]    [Pg.490]    [Pg.27]    [Pg.496]    [Pg.19]    [Pg.58]    [Pg.321]    [Pg.418]    [Pg.61]    [Pg.62]    [Pg.347]    [Pg.145]    [Pg.217]    [Pg.561]    [Pg.120]    [Pg.122]    [Pg.1004]    [Pg.225]    [Pg.142]    [Pg.95]    [Pg.290]    [Pg.317]    [Pg.171]    [Pg.165]    [Pg.399]    [Pg.169]    [Pg.849]    [Pg.300]    [Pg.511]   


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