Acetone in aldol condensation

Aldol condensation is another undesirable reaction that can occur during saponification. Carotenals undergo aldol condensation, with the extension of the polyene chain in the presence of alkali and acetone remaining from the extraction 

Aldol chemicals refer to a variety of substances desired from acetone involving an aldol condensation in a portion of their synthesis. The most important of these chemicals is methyl isobutyl ketone (MIBK), a common solvent for many coatings, pesticides, adhesives, and pharmaceuticals. Approximately 0.17 billion lb of MIBK were made in recent years. The synthesis is outlined on the next page. 

The aldol condensation of acetone to diacetone alcohol is the first step in a three-step process in the traditional method for the production of methyl isobutyl ketone (MIBK). This reaction is catalysed by aqueous NaOH in the liquid phase. (3) The second step involves the acid catalysed dehydration of diacetone alcohol (DAA) to mesityl oxide (MO) by H2S04 at 373 K. Finally the MO is hydrogenated to MIBK using Cu or Ni catalysts at 288 - 473 K and 3- 10 bar (3). 

One of the most thoroughly investigated aldol condensations is the selfcondensation of acetone. This is an important industrial reaction for the production of diacetone alcohol (DA) (Scheme 11), which is valuable as a chloride-free solvent and an intermediate in the synthesis of industrially important products such as mesityl oxide (MO), isophorone, methyl isobutyl ketone, and 3,5-xylenol. The reaction is exothermic, with the yield of DA decreasing with increasing reaction temperature it is usually performed with NaOH or KOH as a basic catalyst 118). 

Acetone, 1 160-177 14 562, 570, 582 acrylamide solubility in, l 290t aldol condensation of, 16 332 in association reactions, 10 682 azeotrope with chloroform, 8 747 azeotrope with water and 2-propanol, 8 795-796 

Another important example is the cross-aldol condensation of citral and acetone, which yields pseudoionone (Scheme 14), an intermediate in the commercial production of vitamin A. Numerous commercial routes to the preparation of pseu-doionones are based on the aldol condensation using conventional homogeneous catalysts, such as aqueous alkali metal hydroxide solutions, alcoholates in alcohol or benzene solvents (126-129). The yields of the cross-condensation product vary between 50% and 80%, depending on the type of catalyst and conditions such as catalyst concentration, ratio of reagents, and temperature. 

Rate and equilibrium constants have been determined for the aldol condensation of a, a ,a -trifluoroacetophenone (34) and acetone, and the subsequent dehydration of the ketol (35) to the cis- and fraw -isomeric enones (36a) and (36b)." Hydration of the acetophenone, and the hydrate acting as an acid, were allowed for. Both steps of the aldol reaction had previously been subjected to Marcus analyses," and a prediction that the rate constant for the aldol addition step would be 10" times faster than that for acetophenone itself is borne out. The isomeric enones are found to equilibrate in base more rapidly than they hydrate back to the ketol, consistent with interconversion via the enolate of the ketol (37), which loses hydroxide faster than it can protonate at carbon. 

DIBK can be produced by the hydrogenation of phorone which, in turn, is produced by the acid-catalyzed aldol condensation of acetone. It is also a by-product in the manufacture of methyl isobutyl ketone. Diisobutyl ketone ( 1.37/kg, October 1994) is produced in the United States by Union Carbide (Institute, West Virginia) and Eastman (Kingsport, Teimessee) (47), and is mainly used as a coating solvent. Catalytic hydrogenation of diisobutyl ketone produces the alcohol 2,6-dimethyl-4-heptanol [108-82-7]. 

The netv reaction conditions effectively suppressed aldehyde self-aldolization. The main side product vas now the corresponding acetone cross aldol condensation product, typically formed in comparable yields vrith the desired aldol addition product. 

The condensation of acetone can also occur over acidic sites as shown by a number of authors [1,9], Generally, when this occurs other products are formed such as isobutene and acetic acid, by the cracking of DAA. Additionally mesitylene can be formed by the internal 2,7-aldol condensation of 4,6-dimethylhepta-3,5-dien-2-one which is in turn obtained by the aldol condensation of MO with a deprotonated acetone molecule [7, 8], As these species are not observed we can concluded that any acidic sites on the silica support are playing no significant role in the condensation of acetone. 

The mechanism of the reaction is undoubtedly as follows when the sulfuric acid and acetone are in contact for long periods of time, several molecules of the acetone condense to form aldol condensation products. These do not break down into mesitylene until the temperature is raised in the second part of the experiment. 

As in the case of homogeneous acids as catalyst, we would also benefit from using solid ba.ses instead of dissolved bases as catalyst. A number of industrially important reactions are carried out with bases as catalyst. A well know example is the aldol condensation of acetone to diacetone alcohol, where dissolved NaOH in ethyl alcohol is u.sed as a catalyst at about 200 to 300 ppm level. However, heterogeneous pelleted sodamide can be used as a catalyst for this reaction and it obviates the problem of alkali removal from the product, which would otherwise lead to reversion of diacetone alcohol to acetone during distillation of the product mixture. 

Kelkar and McCarthy (1995) proposed another method to use the feedforward experiments to develop a kinetic model in a CSTR. An initial experimental design is augmented in a stepwise manner with additional experiments until a satisfactory model is developed. For augmenting data, experiments are selected in a way to increase the determinant of the correlation matrix. The method is demonstrated on kinetic model development for the aldol condensation of acetone over a mixed oxide catalyst. 

Microorganisms have also been developed to produce alternative products, such as lactic acid [65], propane-1,3-diol [67], 3-hydroxypropionic acid [68], butane-2,3-diol [69] and numerous other intermediates. For instance, bacteria such as the Clostridium acetobutylicum ferment free sugars to C4 oxygenates such as butyric acid or butanol. They form the C4 oxygenates by Aldol condensation of the acetaldehyde intermediates. The Weizmann process exploits this property to ferment starch feedstock anaerobically at 37 °C to produce a mixture of w-butanol, acetone and ethanol in a volume ratio of 70 25 5 [3], 

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