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Azeotropic distillation process alcohol dehydration

It would lead us beyond the scope of this book to mention aU the processes of azeotropic distillation known at the present time, since the publications and patents on this subject are numerous the two examples selected show the wide possibilities that exist. Another field of azeotropic distillation is the dehydration of organic compoimds,. such as formic acid, acetic acid and pyridine. Further, mention may be made of the separation of hydrocarbons from alcohols, the purification of aromatic... [Pg.318]

Azeotropic Distillation. The concept of azeotropic distillation is not new. The use of benzene to dehydrate ethyl alcohol and butyl acetate to dehydrate acetic acid has been in commercial operation for many years. However, it was only during World War II that entrainers other than steam were used by the petroleum industry. Two azeotropic processes for the segregation of toluene from refinery streams were developed and placed in operation. One used methyl ethyl ketone and water as the azeo-troping agent (81) the other employed methanol (1). [Pg.207]

Ma, Xu, Liu, and Sun (2010) used perfluorosulfonic acid-poly(vinyl alcohol)-Si02/ poly(vinyl alcohol)/polyacrylonitrile (PFSA-PVA-Si02/PVA/PAN) bifunctional hollow-fiber composite membranes. The catalytic and the selective layer of the membrane were independently optimized. These membranes were synthesized by dipcoating. The performance of these bifunctional membranes was evaluated by dehydrating the ternary azeotropic composed of a water, ethanol, and ethyl acetate system (top product of a reactive distillation process of esterification of acetic acid with ethanol), obtaining separation factors of water/ethanol up to 379. An extensive assessment on the esterification reaction of ethanol-acetic acid was later published (Lu, Xu, Ma, Cao, 2013). In this case, the reaction equilibrium was broken in less than 5 h, and a 90% conversion of acetic acid was achieved after 55 h. [Pg.588]

Separation of alcohols, such as ethanol and butanol, from the fermentation broth is traditionally done by distillation. The higher the alcohol concentration in the fermentation broth, the lower the energy required for distillation. For ethanol fermentation, the broth usually contains 10-15% (w/w) ethanol. After distillation, ethanol concentration in the distillate is about 90% (w/w). The distillation process will not yield more than 93% (w/w) ethanol, which is the azeotropic mixture of ethanol-water. Azeotropic mixtures cannot be separated by distillation because the compositions of ethanol in the vapor and liquid phases are the same. Therefore, azeotropic distillation with benzene or dehydration with molecular sieves is usually used to remove the remaining water and produce fuel grade ethanol (99.9 wt-%). [Pg.199]


See other pages where Azeotropic distillation process alcohol dehydration is mentioned: [Pg.53]    [Pg.189]    [Pg.446]    [Pg.108]    [Pg.288]    [Pg.182]    [Pg.209]    [Pg.257]    [Pg.366]    [Pg.16]    [Pg.336]    [Pg.134]    [Pg.373]    [Pg.118]    [Pg.215]    [Pg.260]    [Pg.27]   
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Azeotropic dehydration

Azeotropic distillation

Azeotropic distillation azeotropes

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Distillation azeotropes

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