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Hydroformylation reaction isomerization during

The composition of the products of reactions involving intermediates formed by metaHation depends on whether the measured composition results from kinetic control or from thermodynamic control. Thus the addition of diborane to 2-butene initially yields tri-j iAbutylboraneTri-j -butylborane. If heated and allowed to react further, this product isomerizes about 93% to the tributylborane, the product initially obtained from 1-butene (15). Similar effects are observed during hydroformylation reactions however, interpretation is more compHcated because the relative rates of isomerization and of carbonylation of the reaction intermediate depend on temperature and on hydrogen and carbon monoxide pressures (16). [Pg.364]

Asymmetric hydroformylation of the three isomeric straight-chain butenes provided evidence that asymmetric induction in both rhodium- and platinum-catalyzed reactions occurs during and before the formation of the alkylmetal intermediate.66 67... [Pg.377]

Thus, the isomerization of linear a-alkenes to internal alkenes during the hydroformylation reaction is an unwanted side reaction since internal alkenes accumulate in the reaction mixture. Table 6 summarizes the selectivity with respect to isomer formation in the two-phase hydroformylation of 1-pentene at different pressure levels. It is concluded that the isomerization can be suppressed most effectively by employing higher pressures. [Pg.398]

The cluster [MoCoNi( 3-CMe)Cp2(CO)s] (11) was found to isomerize 1-pentene, a competition reaction observed during hydroformylation catalysis, and hydrogenate 2-pentene and styrenesj ° ° Hydroformylation of styrene was also inves-... [Pg.630]

Cyclooctadiene-1,5 is also partly isomerized during the reaction to cyclo6ctadiene-l,3 (VIII). Only the mono-aldehyde (VII) or monool (II) is obtained from (VIII), since conjugated dienes are hydrogenated rapidly to olefins (IX) in the hydroformylation reaction [10, 251]. (VIII) reacts practically quantitively through (IX) to (VII). [Pg.44]

Diels-Alder reactions, 133, 135 epoxidation, 69-72, 516 grafting on polyethylene, 462 hydroformylation, 44 hydrogenation, 41, 42 isomerization catalysts, 133, 484 isomerization during polymerizations, 484 isomerization kinetics, 484 isopropyl alcohol radical reaction, 207 MA copolymerization, 532, 534, 541 Michael reactions, 63-66 nitrone adducts, 224, 225 olefin copolymerization, 288 olefin ene reactions, 162 phenanthrene adducts, 181 plasticizers use, 14 production—synthesis, 14, 78-81 radical copolymerization, 270, 275-277, 307, 315, 317, 333, 345, 365, 379 radical polymerization, 239, 264, 287 reaction with allyl alcohol, 46 reaction with sodium bisulfite, 53 styrene copolymerization, 365, 483 tetraalkyl methylenediphosphonate adduct, 66 transesterification, 46 /7-xylylene copolymerization, 359 dialkyl stannyl, PVC stabilizer, 275 diaryl, synthesis from MA, 80 pyridinium, betaine intermediate, 216... [Pg.841]

The isomerization of the olefin prior to its hydroformylation has been the explanation of this question (3) and the formation of isomeric aldehydes was related to the presence of isomeric free olefins during the hydroformylation. This explanation, however, is being questioned in the literature. The formation of (+) (S) -4-methylhexanal with an optical yield of more than 98% by hydroformylation of (+) (S)-3-methyl-l-pentene (2, 6) is inconsistent with the olefin isomerization explanation. Another inconsistency has been the constance of the hydroformylation product composition and the contemporary absence of isomeric olefins throughout the whole reaction in hydroformylation experiments carried out with 4-methyl-1-pentene and 1-pentene under high carbon monoxide partial pressure. The data reported in Ref. 4 on the isomeric composition of the hydroformylation products of 1-pentene under high carbon monoxide pressure at different olefin conversions have recently been checked. The ratio of n-hexanal 2-methylpentanal 2-ethylbutanal was constant throughout the reaction and equal to 82 15.5 2.5 at 100°C and 90 atm carbon monoxide. [Pg.293]

This conclusion was challenged by Johnson (72), who followed the formation of isomeric aldehydes and isomeric olefins during the hydroformylation of 4-methyl-1-pentene. He found that 2-olefin was formed very rapidly under Oxo conditions and suggested that this did not affect the preferential formation of terminal aldehyde significantly, due to the fact that 2-olefin was so much less reactive to hydroformylation. These results have now been checked by Piacenti et al. (115), who found that 2-olefin was only rapidly formed if the rate of the reaction was sufficiently high that the solution was no longer saturated with carbon monoxide. By using a lower catalyst concentration in benzene solvent they were able to avoid this deficiency and found very little olefin isomerization. [Pg.132]

A major interest for those practicing hydroformylation syntheses is the selectivity to the product desired. The factors which affect the yield of a specific aldehyde are (1) the structure of the olefinic substrate (a-olefin or internal olefin, branching, cyclic), (2) the isomers formed during the reaction (directly, with concomitant isomerization), (3) the effects of functional groups, and (4) the subsequent reactions of the product aldehyde. [Pg.509]

The fact that terminal olefin is recovered indicates that, although doublebond isomerization occurs at a rate which is significant compared with the rate of hydroformylation, it is considerably slower than hydroformylation kz > ki). The hydroformylation of terminal olefins is faster than that of, internal olefins, and there is an accumulation of internal olefins during the reaction. [Pg.599]

If fci, the rate of isomerization of 1-pentene, is almost seven times greater than the rate of its hydroformylation as is calculated above, one would expect a rapid build-up of 2-pentene during the course of a 1-pentene reaction. This is decidedly not the case. Thus, the difference between the observed rates of reaction is not great enough to be accounted for by isomerization rates. [Pg.616]

The structures of anionic, triple-nuclear osmium and iron cluster catalysts supported on copolymers of styrene and divinylbenzene were analyzed by means of IR spectroscopy. Their catalytic activity during 1-hexene hydroformylation [250] and C5H5NO2 carbonylation [251] were investigated. It was found that isomerization proceeds simultaneously in the presence conventional catalysts. In the absence of moisture, a triple-nuclear osmium complex could be removed from a polymeric support after reaction. This suggests catalytic activity for this complex, particularly in the fixed state. Furthermore, a definite correlation was found to exist between polynuclearity and selectivity of heptanol formation. For iron, however, the cluster structure altered during the course of the reaction. [Pg.125]

Reactions of internal olefins can even generate terminal alkylnitriles by a pathway that involves isomerization of intermediate cyanometal-alkyl complexes. Tlus isomerization is similar to the isomerization that occurs during the hydroformylation of internal olefins discussed in Chapter 17. In fact, the nickel catalyst rapidly isomerizes hexene to the equilibrium ratio of olefins faster than it adds HCN to the C=C bond. Thus, internal hexenes generate the terminal alkane nitrile. [Pg.669]

With nonfunctionalized terminal olefins, the formation of internal olefins is favored. Less than 5% of the terminal olefins may be present in thermodynamic equilibrium. Slow isomerization in comparison to the subsequent hydroformylation may lead to a continuous erosion of the regioselectivity during the reaction [18]. -01efins are more stable than Z-isomers, therefore, double bond migration can commence with a Z/ -isomerization step [19]. [Pg.382]

Fatty acid compounds usually contain single or multiple double bonds with varying E/Z geometries. Under hydroformylation conditions, they can be hydrogenated before hydroformylation takes place [21]. A special problem is Z/ isomerization or the migration of double bonds, since most hydroformylation catalysts are also active isomerization catalysts. Isomerization may take place before, during, or after (multiple double bonds ) the reaction with syngas. [Pg.591]


See other pages where Hydroformylation reaction isomerization during is mentioned: [Pg.284]    [Pg.207]    [Pg.284]    [Pg.509]    [Pg.563]    [Pg.56]    [Pg.117]    [Pg.165]    [Pg.184]    [Pg.126]    [Pg.237]    [Pg.51]    [Pg.456]    [Pg.184]    [Pg.232]    [Pg.12]    [Pg.547]    [Pg.125]    [Pg.446]    [Pg.16]    [Pg.120]   
See also in sourсe #XX -- [ Pg.609 ]




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