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Semiconductor and pharmaceutical industries often produce waste alcohol mixtures. This study discusses a reactive distillation process of a mixed alcohol feed containing n-amyl alcohol and n-hexanol to react with acetic acid to produce useful esters. In an earlier paper (Lee et al. Ind. Eng. Chem. Res. 2009 48, 7186–7204), optimal design of the same Type-III mixed-alcohol reactive distillation process containing n-butanol and n-amyl alcohol was developed. In that paper, the indirect sequence containing a reactive distillation column with heavier amyl acetate bottom product and a second column to produce butyl acetate gives the lowest total annual cost. In this study, with different mixed alcohol feed (although of the same reaction type), it is found that an alternative direct sequence design is much more economically favorable with 34% reduction in total annual cost as compared to the indirect sequence. The reason for the seemingly contradictory results can be explained by differences in relative volatili...

Nano-TiO2 powder was synthesized by the continous-orderly-controlled-explosive nucleation method [1]. The experiment has effectively degenerated the n-amyl alcohol gas, and investigated its influencing factor by using the Nano-TiO2 photocatalytic activity[2]. When the initial density of the n-amyl alcohol gas is 1714.7mg/m3, the TiO2 calcination temperature is 450°C, the dosage of catalyst is 9.98g. The experiment reacts 40 minutes later, degeneration rate of the n-amyl alcohol achieves above 98%, and the degeneration rate increases constantly with the extension of reaction time. This study provides a solution for the environment pollution problem which the n-amyl alcohol produces.

Manufacturing processes in the semiconductor and pharmaceutical industries often produce alcohol mixture byproducts. Therefore, the esterification of alcohol mixtures may be an important step in re...

Esterifications of n-amyl alcohol with propionic acid catalyzed by macroporous (Amberlyst-15) and microporous (Dowex 50 W and Amberlite IR-120) polymeric ion-ex6hange resins were carried out between 333-348 K. When these catalysts were used as commercially available, Amberlyst-15 was observed to be the most effective catalyst with respect to rate constants, but after drying it became the less effective one. The reaction rate increased with increase in catalyst concentration and reaction temperature. Stirrer speed and different mesh sizes had virtually no effect on the rate under the experimental conditions. The effect of divinylbenzene content was examined for the micro porous resin Dowex 50 W, and the results showed that the propionic acid conversion decreased as the divinylbenzene content was increased. The rate data were correlated with a second-order homogeneous reaction model. The apparent activation energies, reaction enthalpies and entropy values were calculated for each catalyst. Reaction monitoring is simple and fast by volumetric method and the reproducibility of this method was the order of +/- %2.54.

Vapor-liquid equilibria were measured for the three binary systems made of methyl ethyl ketone with acetone, methyl acetate, or n-amyl alcohol at 100 kPa of pressure by the dew-point-bubble-point temperature apparatus previously proposed by the authors was modified in the present study. Combining the experimental dew-point and bubble-point temperature curves, vapor-liquid equilibria were obtained without using any analytical instrument

n-Amyl alcohol, dissolved in corn oil, was administered to rats by oral intubation at dose levels of 0 (control), 50, 150 or 1000 mg/kg body weight/day for 13 wk. The treatment had no demonstrable effect on body-weight gain, food and water consumption, haematological values, serum and urine analyses, renal function, organ weights or histopathology. The no-untoward-effect level was 1000 mg/kg/day. which is about 2000 times the estimated maximum likely intake by man.

The adsorption of n-amyl alcohol on the (111) and (100) faces of silver has been investigated. Some adsorption parameters have been estimated. It is shown that the (100) face adsorbs organic molecules more strongly.

Vapor-llquld equHMwn data for the blnary 8ystems ethylene glycol (1,?4hanedbl) wlth n-amyl alcohol (1-pentanol) and ethylene glycol wlth Isoamyl alcohol (3-methyi-l-bulanol) have been measured at 100 mmHg (13.33 kPa) by ushg a reclrculatbn stll a8 propowd by Rbck and Sleg. From these data, Uquld-phare activity coetfldents were flttod by wing the MarguJes, van Laar, Wilson, and UNIQUAC equations. Vapor-prereure meawr(MIBnts of the pure substances were carrled out, and the data were correlated wlth the Antolne equatlon. The Wnaty data were used for the determlnatlon of UNIFAC parameters.

An empirical equation relating sound velocity to temperature and pressure ia given for n‐amyl alcohol together with the coefficients for the equation. The change in velocity with the addition of CH2 groups is shown for five primary alcohols.