Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Ethanol composition

Using the Wilson equation, calculate the activity coefficients for isopropyl alcohol (IPA) and water in a mixture of IPA, methanol, water, and ethanol composition, all mol fraction ... [Pg.344]

Alvarez Gonzalez et al. (19) stated that those systems in which the value of n is less than unity move the azeotrope to richer ethanol compositions, even to breaking the azeotrope. This was also observed for the systems presently under consideration. Reference 19 proposes a correlation of the equilibrium data by the empirical equation ... [Pg.101]

From these it can be deduced that the system with a slope of less than 1.39 moves the azeotrope toward richer ethanol composition, as was also deduced in Reference 19. [Pg.102]

Our AHw° values are in fair agreement with earlier calorimetric values (30). Our values are more positive by ca. one kcal at the highest ethanol compositions. [Pg.274]

Provided that the influence of the water-ethanol composition on the reaction involving addition of hydroxide ions to benzaldehydes can be characterized by any parameter Yj (the application of Y- used for benzoic acid dissociations in ethanol-water mixtures (28) might be doubtful), application of the relation pYt - pyo = C(Yi - Y0) would indicate that the value of C (0.638) for benzoic acids (28) and —0.573 for anilines (29) is close to zero for the benzaldehyde reaction (4). [Pg.359]

Three parameters were identified and adjusted to validate the model against the experiments. The parameters are the heat losses, the nominal tray holdup and the Murphree tray efficiency (EM). Figure 4.16 shows how EM is adjusted to match the dynamic model prediction and experimental temperature profile measured on Plate 12. Figure 4.17 shows the comparison between the experimental and model prediction of ethanol composition in the reflux drum, middle vessel and in the bottom of the column. Figures 4.16-17 show a good match between the model prediction and experiments. [Pg.100]

This glycol-AN explosive like the methanol and ethanol compositions are very efficient. Since the glycols and glycerins are in effect forms of alcohols, they perform similarly. Glycerin could be substituted for the glycol, but it s cost is even higher than glycol. Addition of a small amount of "Tide" or "Mr. Bubble" (e g. sodium dodecyl benzene sulfonate) will increase the performance and detonation rate by 15-35%. [Pg.17]

Getting pure ethanol will be difficult. Ethanol is in the third distillation region, and no obvious means exist to cross the relevant distillation boundaries. A new entrainer might be added, as was the case for the previous example. However, since the ethanol is only going to be recycled to the reactor, the required purity specification might be questioned. What is the effect of small amounts of contaminants DEM and water in the recycled ethanol The acetal formation reaction is equilibrium-controlled, so there may be some deleterious effect of including products with a reactant. However, additional analysis indicated that the effect is small, and so the ethanol composition requirement was relaxed and the overhead composition recycled to the reactor directly as produced. [Pg.58]

Attempted intermolecular coupling of ketones and nitriles under conditions similar to those used for intramolecular coupling led to mixtures of two types of ketone-nitrile coupling products and alcohols resulting from ketone electroreduction. Product selectivity could be changed altering nitrile/solvent (2-propanol or ethanol) composition. Some results for cyclohexanone/acetonitrile reductions are shown in Scheme 27. [Pg.611]

The initial guessed value of the reflux ratio in the second column was 2. The bottoms purity was very high. The reflux ratio was reduced to about RR = 0.2 without affecting the bottoms purity significantly. A second Design Spec/Vary is set to maintain the ethanol composition of the bottoms of the second column at 0.1 mol% by varying the bottoms flow rate B2. [Pg.114]

Deshmukh S.P., Li K. (1998), Effect of ethanol composition in water coagulation bath on morphology of PVDF hollow fibre membranes, J. Membrane Sci., 150, 75-85. [Pg.99]

Again, the proper selection of ethanol is crucial to the rqnoducibility of an analysis and should be clearly designated in a method. Also note that ethanol composition, if used in as part of a mobile phase, will vary lot-to-lot due to the approximate denaturant level. This means that if peak resolution is small these effects could be critical to the separation. [Pg.36]

Figure 14.3 illustrates what happens inside the first three-cell module. Temperatures decrease from cell to cell. Permeate ethanol composition increases and permeate flowrate decreases from cell to cell. The fluxes from each of the three cells (with different temperatures and compositions) are mixed to give the total vapor permeate from the module. Each module has a total area of 300 m or 100 m per cell. [Pg.440]

Figure 10.38. Vapor ethanol composition vs. feed liquid composition. (Reproduced from [336] with permission.)... Figure 10.38. Vapor ethanol composition vs. feed liquid composition. (Reproduced from [336] with permission.)...
Figure 22.2 The time variation of distillate and bottom ethanol compositions during batch fractionation of ethanol and water for constant distillate flow. Figure 22.2 The time variation of distillate and bottom ethanol compositions during batch fractionation of ethanol and water for constant distillate flow.
The results obtained for the sixteen combinations are summarized in Table 2.10. The unit energy cost was used to assess economic performance. A mass intensity index (Mil), defined as [(mass of feedstock-mass of bioethanol produced)/mass of bioethanol produced], and a water intensity index (WII), defined as (mass of fresh water/mass of ethanol produced) (El-Halwagi, 2012), were calculated. These two indices show the efficient use of basic resources, feedstocks and water. The ethanol composition after conversion is also reported. It can be observed that the best values for the WII are associated to... [Pg.53]

Deshmukh, S.P. and K. Li. 1998. Effect of Ethanol Composition in Water Coagulation Bath on Morphology of PVDF Hollow Fibre Membranes. Journal of Membrane Science 150(1) 75-85. doi 10.1016/S0376-7388(98)00196-3. [Pg.280]

The shrinkage of the polymer chains at low and high ethanol compositions is attributed to increased hydrophobic interactions and hydrogen bonding, respectively. Poly(l-methyl-5-vinylimidazole) in a solvent of low ethanol content is similarly in a tightly coiled conformation due to an increased hydrophobic interaction. This shrinkage in polymer conformation has been attributed by us to the apolar nature of the polymer s hydrocarbon backbone. [Pg.261]


See other pages where Ethanol composition is mentioned: [Pg.182]    [Pg.182]    [Pg.184]    [Pg.185]    [Pg.136]    [Pg.192]    [Pg.192]    [Pg.184]    [Pg.185]    [Pg.5]    [Pg.121]    [Pg.280]    [Pg.51]    [Pg.430]    [Pg.362]    [Pg.419]   
See also in sourсe #XX -- [ Pg.1465 ]




SEARCH



Ethanol fatty acyl composition

Ethanol percent composition

Ethanol solution composition

Ethanol temperature-composition

Ethanol-water composition, solute

Ethanol-water composition, solute solubility

© 2024 chempedia.info