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Butanal, synthesis from 1-butene

It is evident that 1-propanol produced n-butane or n-butenes with a high activity but that most, or all, of the /-butane or /-butene was formed directly from the unlabeled CO. The results for the synthesis when 2-propanol was added are just the opposite the iso-alcohol produces labeled iso-C hydrocarbons but the n-C4 hydrocarbons are mostly, or exclusively, formed from the unlabeled CO. These above results were clearly presented... [Pg.68]

Butene oligomerization, phenol synthesis from benzene, butane partial oxidation, and other reactions carried out in membrane reactors... [Pg.641]

Raffinate-II typically consists of40 % 1-butene, 40 % 2-butene and 20 % butane isomers. [RhH(CO)(TPPTS)3] does not catalyze the hydroformylation of internal olefins, neither their isomerization to terminal alkenes. It follows, that in addition to the 20 % butane in the feed, the 2-butene content will not react either. Following separation of the aqueous catalyts phase and the organic phase of aldehydes, the latter is freed from dissolved 2-butene and butane with a counter flow of synthesis gas. The crude aldehyde mixture is fractionated to yield n-valeraldehyde (95 %) and isovaleraldehyde (5 %) which are then oxidized to valeric add. Esters of n-valeric acid are used as lubricants. Unreacted butenes (mostly 2-butene) are hydroformylated and hydrogenated in a high pressure cobalt-catalyzed process to a mixture of isomeric amyl alcohols, while the remaining unreactive components (mostly butane) are used for power generation. Production of valeraldehydes was 12.000 t in 1995 [8] and was expected to increase later. [Pg.112]

In 1992, refiners began to choose a variety of routes to the synthesis of MTBE [51]. Valero Refining Marketing, in its MTBE synthesis plant, uses a butane/butylene mixture from the heavy oil cracker vapor recovery unit which on hydrogenation converts butadiene to butylene. This is then mixed with methanol in the MTBE synthesis unit, the MTBE product is separated and the butane/butene stream is charged to the alkylation unit. The butadiene is removed from the alkylation unit. This improves alkylate quality and reduces acid consumption. A block diagram of this unit is shown in Figure 3.29. [Pg.161]

The most widely used kinetic equation for the MTBE synthesis reaction is probably that proposed by Rehfmger and Hoffmann [1]. It was obtained from experiments made in similar conditions than those of the present work, but in the use of inerts (1-butene and/or n-butane) as... [Pg.541]

Poly(chloroprene) was one of the first synthetic elastomers. It came on the market in 1931, and was developed at the Du Pont factory as part of their search for elastomers for special areas of application. The industrial synthesis of the monomer became possible when Nieuwland discovered mono vinyl acetylene. Today, chloroprene is produced from monovinyl acetylene C4H4, butadiene butene C4H8, or butane C4Hio-... [Pg.894]


See other pages where Butanal, synthesis from 1-butene is mentioned: [Pg.767]    [Pg.292]    [Pg.238]    [Pg.3]    [Pg.253]    [Pg.254]    [Pg.605]    [Pg.343]    [Pg.161]    [Pg.265]    [Pg.230]    [Pg.66]    [Pg.411]    [Pg.398]   
See also in sourсe #XX -- [ Pg.376 ]




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