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Point-type reactions

Confidence is needed in order to justify risking precious starting materials, reagents, and research time. Researchers may spend long hours faithfully reproducing a narrow set of conditions known to work on smaller scale. Point-type reaction conditions, i.e., those in which a small change affords a dramatic drop in product yield or quality [1], can be tolerated for a few runs when the goal is to immediately provide key amounts of material. [Pg.28]

Turner has described two reaction-type extremes, plateau-type and point-type reactions, based on the reaction yield vs. optimum reaction conditions. While the reaction conditions first disclosed by Weiss were an improvement over the existing methods to assemble the bicyclo[3.3.0] scaffold, the overall yield was low and very sensitive to reaction conditions, i.e., a point-type reaction. To increase the synthetic utility of this chemistry, reaction conditions were investigated to transition it to a plateau-type reaction. [Pg.184]

Another interesting example is SHMT. This enzyme catalyzes decarboxylation of a-amino-a-methylmalonate with the aid of pyridoxal-5 -phosphate (PLP). This is an unique enzyme in that it promotes various types of reactions of a-amino acids. It promotes aldol/retro-aldol type reactions and transamination reaction in addition to decarboxylation reaction. Although the types of apparent reactions are different, the common point of these reactions is the formation of a complex with PLP. In addition, the initial step of each reaction is the decomposition of the Schiff base formed between the substrate and pyridoxal coenzyme (Fig. 7-3). [Pg.309]

Enzyme Catalyzed. The enzyme aldolases are the most important catalysts for catalyzing carbon-carbon bond formations in nature.248 A multienzyme system has also been developed for forming C-C bonds.249 Recently, an antibody was developed by Schultz and co-workers that can catalyze the retro-aldol reaction and Henry-type reactions.250 These results demonstrate that antibodies can stabilize the aldol transition state but point to the need for improved strategies for enolate formation under aqueous conditions. [Pg.268]

In most chemical reactions the rates are dominated by collisions of two species that may have the capability to react. Thus, most simple reactions are second-order. Other reactions are dominated by a loose bond-breaking step and thus are first-order. Most of these latter type reactions fall in the class of decomposition processes. Isomerization reactions are also found to be first-order. According to Lindemann s theory [1, 4] of first-order processes, first-order reactions occur as a result of a two-step process. This point will be discussed in a subsequent section. [Pg.45]

First-Order Reversible Reactions. Though no reaction ever goes to completion, we can consider many reactions to be essentially irreversible because of the large value of the equilibrium constant. These are the situations we have examined up to this point. Let us now consider reactions for which complete conversion cannot be assumed. The simplest case is the opposed unimolecular-type reaction... [Pg.56]

The analogy of these dimerization processes to thermal Diels-Alder type reactions which sometimes also yield cyclobutane structures is worth noting and may be taken as one of the arguments for a diradical structure of the transition in the latter process. Also, it may be pointed out that the photoexcited state involved is presumably the same one involved in the well-known photochemical trans-cis interconversion of such olefins. [Pg.92]

An important steric hindrance of the carbon in the a-position to the oxygen (or a bicyclic structure) reduces or even inhibits formation of the phosphoryl group by substitution reaction on this carbon. It must be pointed out that phosphoryl formation occurs, generally, in Arbuzov-type reactions, by a substitution process, but can take place also by a -elimination which is favoured by major steric hindrance. [Pg.96]

In Section 4.7, we discussed the relaxation process of SE s in a closed system where the number of lattice sites is conserved (see Eqn. (4.137)). A set of coupled differential equations was established, the kinetic parameters (v(x,iq,x )) of which describe the rate at which particles (iq) change from sublattice x to x. We will discuss rate parameters in closed systems in Section 5.3.3 where we deal with diffusion controlled homogeneous point defect reactions, a type of reaction which is well known in chemical kinetics. [Pg.117]

Hydrocarbon oxidation may also be considered a free radical chain-type reaction. At elevated temperatures, hydrocarbon free radicals (R) are formed which react with oxygen lo form peroxy radicals (R(X These, in turn, take up a hydrogen atom from the hydrocarbon to form a hydroperoxide (ROOH) and another hydrocarbon free radical. The cycle repeals itself with the addition of oxygen. The unstable hydroperoxides remaining are the major points for degradation and lead to rancidity and color development in oils, fats, and waxes decomposition and gum formation in gasolines sludging in lubricants and breakdown of plastics and rubber products. Antioxidants, such as amines and phenols, are often introduced into hydrocarbon systems in order lo prevent this free radical oxidation sequence. [Pg.680]

Methyl esterification of fatty acids with methanol is generally conducted in the presence of acid catalyst at an elevated temperature close to the boiling point of methanol. Recently, we found that fatty acids could be successfully methyl esterified in supercritical methanol without the use of a catalyst (10). In addition, from a comparative study between transesterification of vegetable oil and alkyl esterification of fatty acids with supercritical alcohols at 300°C in a batch-type reaction system, the reaction rates of alkyl esterification were found to be faster than those of transesterification (11). An additional finding was that alkyl esterification of fatty acids could be performed at a lower reaction temperature than transesterification. [Pg.782]

The reaction media for Wacker-type reactions are highly corrosive. This is due to the presence of free acids (acetic acid for vinyl acetate), ions like Cl, and dioxygen. For any successful technology development, the material of construction for the reactors is a major point of concern (see Section 3.1.4). Some progress in this respect has recently been made by the incorporation of heteropolyions such as [PV14042]9 in the catalytic system. The heteropolyions probably act as redox catalysts. A seminonaqueous system is used for this modified catalytic system, and the use of low pH for dissolving copper and palladium salts is avoided. [Pg.174]

Although the reaction system stated above has extended the substrate applicability in Mannich reactions in water, there is still a drawback that the silicon enolates, which are prepared from the corresponding carbonyl compounds usually under anhydrous conditions, have to be used. From atom-economical and practical points of view, it is desirable to develop an efficient system for Mannich-type reactions in which the parent carbonyl compounds are directly used. Along this line, we next investigated three-component Mannich-type reactions in water using ketones, instead of silicon enolates, as nucleophilic components, and found that DBSA was also an effective catalyst [36]. An example is shown in Equation (7), where only 1 mol% DBSA was sufficient to give the desired product. [Pg.279]

Traditionally, relative stabilities of carbocations have been derived from the comparison of the rates of solvolysis reactions following the SN1 mechanism, for which the designation Dm + An has recently been proposed [36], The comparison of solvolytic rate constants for substrates of a large structural variety is hampered by the fact that the published solvolysis rates refer to different solvents, different temperatures, and precursors with different leaving groups. Dau-Schmidt has, therefore, converted solvolysis rates of a manifold of alkyl chlorides and bromides to standard conditions, i.e., soiv of RC1 in 100% EtOH at 25° C (Scheme 6) [37]. Although from a theoretical point of view, ethanol is not an ideal solvent for observing unassisted SN 1-type reactions (nucleophilic solvent participation), it has been selected as the reference solvent because most available experimental data have been collected in solvents of comparable nucleophilicity, a fact which made conversions to 100% ethanol relatively unproblematic [38],... [Pg.58]


See other pages where Point-type reactions is mentioned: [Pg.2317]    [Pg.41]    [Pg.31]    [Pg.211]    [Pg.267]    [Pg.368]    [Pg.36]    [Pg.13]    [Pg.418]    [Pg.143]    [Pg.402]    [Pg.323]    [Pg.562]    [Pg.181]    [Pg.179]    [Pg.136]    [Pg.916]    [Pg.86]    [Pg.41]    [Pg.511]    [Pg.150]    [Pg.790]    [Pg.150]    [Pg.36]    [Pg.319]    [Pg.265]    [Pg.375]    [Pg.50]    [Pg.56]    [Pg.143]    [Pg.263]    [Pg.187]    [Pg.202]    [Pg.418]    [Pg.180]   
See also in sourсe #XX -- [ Pg.184 ]




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Point-type reaction conditions

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